Calcium carbonate-comprising material with high bio-based carbon content for polymer formulations

The present invention relates to a calcium carbonate-comprising material having a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the material, a process for the preparation of the calcium carbonate-comprising material, a polymer formulation comprising the calcium carbonate-comprising material, an article formed from the polymer formulation, a process for preparing the article as well as the use of the calcium carbonate-comprising material in a polymer formulation.

It is common in the art to add certain fillers to polymer compositions. For example, fillers such as calcium carbonate-comprising materials are added to polymeric products in order to improve its mechanical properties. For example, EP3192837 A1 refers to a surface-modified calcium carbonate, which is surface-treated with an anhydride or acid or salt thereof, and suggests its use inter alia in polymer compositions, papermaking, paints, adhesives, sealants, pharma applications, crosslinking of rubbers, polyolefins, polyvinyl chlorides, in unsaturated polyesters and in alkyd resins. EP2554358 A1 refers to a moisture-permeable and waterproof film that is biodegradable comprising polylactic acid and an inorganic filler. The inorganic filler is selected from the group consisting of calcium carbonate, barium carbonate, calcium sulfate, barium sulfate, magnesium hydroxide, aluminum hydroxide, calcium hydroxide, magnesium oxide, titanium oxide, zinc oxide, silicon oxide and talc.

W02009/152427 A1 refers to a biaxially oriented laminate film including a core layer including a blend of crystalline polylactic acid polymer and an inorganic antiblock particle. EP1254766 A1 refers to multilayer films comprising a layer comprising a thermoplastic polymer, such as an aliphatic-aromatic copolyester (AAPE), with or without filler, and a layer comprising a filled thermoplastic polymer.

However, when adding fillers such as calcium carbonate to a polymer, its bio-based carbon content according to EN 16640 generally decreases as e.g. calcium carbonate is not considered biobased. The foregoing is even more pronounced for the growing market of bio-based polymers. But calcium carbonate can be needed to achieve the desired mechanical properties or economical viability of the products.

Therefore, there is an ongoing need for a calcium carbonate-comprising material providing a high content of bio-based carbon, which is especially suitable for use in polymers.

Accordingly, it is an object of the present invention to provide a calcium carbonate-comprising material having a high content of bio-based carbon. Furthermore, it is desirable that the calcium carbonate-comprising material having a high content of bio-based carbon can be used in polymers, especially bio-based polymers. Furthermore, it is desirable that the calcium carbonate-comprising material having a high content of bio-based carbon provides sufficient properties such as mechanical properties, rheological properties and processing stability for a use in these demanding applications.

The foregoing and other objects are solved by the subject-matter as defined in the independent claims. Advantageous embodiments of the present invention are defined in the corresponding subclaims. According to one aspect of the present invention, a calcium carbonate-comprising material is provided having

- a weight median particle size cko of < 60 pm,

- a top cut particle size dgs of < 500 pm, and

- a residual total moisture content of < 1 .0 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, wherein the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the material.

According to one embodiment, the calcium carbonate-comprising material has

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, and/or

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, and/or

- a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277, and/or

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, and/or

- a content of bio-based carbon determined according to DIN EN 16640:2017 of at least

60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material.

According to another embodiment, the calcium carbonate-comprising material is based on eggshells, seashells and/or oystershells.

According to yet another embodiment, the calcium carbonate-comprising material is a treated calcium carbonate-comprising material comprising a treatment layer on the surface of the calcium carbonate-comprising material, preferably the treatment layer comprises a surface-treatment agent selected from the group consisting of

I) a phosphoric acid ester blend of one or more phosphoric acid mono ester and/or salts thereof and/or reaction products thereof and/or one or more phosphoric acid di-ester and/or salts thereof and/or reaction products thereof , or

II) at least one saturated or unsaturated aliphatic linear or branched carboxylic acid and/or salts thereof and/or reaction products thereof , preferably at least one aliphatic carboxylic acid having a total amount of carbon atoms from C4 to C24 and/or salts thereof and/or reaction products thereof , more preferably at least one aliphatic carboxylic acid having a total amount of carbon atoms from C12 to C20 and/or salts thereof and/or reaction products thereof , most preferably at least one aliphatic carboxylic acid having a total amount of carbon atoms from C16 to C18 and/or salts thereof and/or reaction products thereof , or

III) at least one mono-substituted succinic anhydride consisting of succinic anhydride mono-substituted with a group selected from a linear, branched, aliphatic and cyclic group having a total amount of carbon atoms from at least C2 to C30 in the substituent and/or salts thereof and/or reaction products thereof , and/or

IV) at least one polydialkylsiloxane, and/or

V) at least one cross-linkable compound comprising at least two functional groups, wherein at least one functional group is suitable for cross-linking a polymer resin and wherein at least one functional group is suitable for reacting with the calcium carbonate-comprising material, and/or

VI) at least one grafted polymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a homo- or copolymer comprising butadiene units and optionally styrene units and/or salts thereof and/or reaction products thereof , or

VII) mixtures of one or more materials according to I) to VI), more preferably the treatment layer comprises a surface-treatment agent selected from at least one mono-substituted succinic anhydride consisting of succinic anhydride mono-substituted with a group selected from a linear, branched, aliphatic and cyclic group having a total amount of carbon atoms from at least C2 to C30 in the substituent and/or salts thereof and/or reaction products thereof .

According to one embodiment, the treated calcium carbonate-comprising material comprises the treatment layer in an amount ranging from 0.1 to 3 wt.-%, preferably from 0.1 to 1 .2 wt.-% based on the total weight of the treated calcium carbonate-comprising material, and/or in an amount ranging from 0.2 to 5.0 mg/m ² of the BET specific surface area of the calcium carbonate-comprising material and preferably from 0.5 to 3.0 mg/m ² of the BET specific surface area of the calcium carbonate- comprising material.

According to another embodiment, the treated calcium carbonate-comprising material has

- a residual total moisture content of < 0.7 wt.-%, preferably of < 0.5 wt.-%, more preferably < 0.3 wt.-% and most preferably of < 0.2 wt.-%,, based on the total dry weight of the treated calcium carbonate-comprising material, and/or

- a moisture pick-up susceptibility of < 6 mg/g, preferably < 3 mg/g, more preferably < 2 mg/g, and most preferably < 1 .5 mg/g, based on the total dry weight of the treated calcium carbonate- comprising material.

According to another aspect, a process for the preparation of the calcium carbonate- comprising material as defined herein is provided, the process comprising the steps of: a) providing a calcium carbonate-comprising material having a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the material, preferably the calcium carbonate-comprising material is based on eggshells, seashells and/or oystershells, and b) grinding the calcium carbonate-comprising material of step a) to

- a weight median particle size cko of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably < 2 pm,

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm.

According to one embodiment, the grinding is carried out in the absence of dispersant(s). According to another embodiment, the grinding is a dry grinding or wet grinding, preferably wet grinding at solids content in the range from 1 to 40 wt.-%, preferably from 2 to 35 wt.-%.

According to yet another embodiment, the process further comprises step c) in which the calcium carbonate-comprising material is contacted under mixing, in one or more steps, with a surface-treatment agent such that a treatment layer comprising the surface-treatment agent and/or salts thereof and/or reaction products thereof is formed on the surface of the calcium carbonate- comprising material.

According to one embodiment, step c) is carried out at a temperature that is at least 2°C, preferably 5°C above the melting point of the surface-treatment agent and/or at a temperature ranging from 50 to 130°C, preferably from 60 to 120°C.

According to another embodiment, the process further comprising d) a step of drying the calcium carbonate-comprising material before and/or after grinding step b) and optionally before surface-treating step c), and/or e) a step of grinding, cleaning, washing and/or bleaching the calcium carbonate- comprising material before and/or after grinding step b).

According to another aspect, a polymer formulation is provided comprising a) a polymer resin, and b) the calcium carbonate-comprising material as defined herein, wherein the calcium carbonate-comprising material is dispersed in the polymer resin. According to one embodiment, the polymer resin is selected from the group comprising polyester, polyolefin, polyamide and mixtures thereof, preferably polyethylene, polypropylene, polylactic acid, polylactic acid-based polymer, polyhydroxyalkanoates (PHA), e.g. polyhydroxybutyrate (PHB), poly-3- hydroxy butyrate (P3HB), poly3-hydroxybutyrate-co-3-hydroxyhexanoate (PHBH), polyhydroxyvalerate, polyhydroxybutyrate-polyhydroxyvalerate copolymer, poly(3-hydroxybutyrate-co- 3-hydroxyvalerate) (PHBV); polybutyrate-adipate-terephthalate (PBAT), polyglyconate, polyethylene terephthalate (PET), polycarbonate (PC), poly(dioxanone), polybutylene succinate (PBS), polycaprolactone (PCL), polycaprolactone-poly(ethylene glycol) copolymer, polycaprolactonepolylactic acid copolymer, polyvinylalcohol (PVA), polyethylene succinate) (PES), polypropylene succinate) (PPS), and mixtures thereof, more preferably polylactic acid, polylactic acid-based polymer, poly(3-hydroxybutyrate-co-3-hydroxyvalerate) (PHBV), polyhydroxyalkanoates (PHA) polyethylene terephthalate (PET), and mixtures thereof or the polymer resin is an elastomer resin, preferably an elastomer resin selected from natural or synthetic rubber, more preferably from the group consisting of acrylic rubber, butadiene rubber, acrylonitrile-butadiene rubber, epichlorhydrin rubber, isoprene rubber, ethylene-propylene rubber, ethylene-propylene-diene monomer rubber, nitrile-butadiene rubber, butyl rubber, styrene-butadiene rubber, polyisoprene, hydrogenated nitrile-butadiene rubber, carboxylated nitrile-butadiene rubber, chloroprene rubber, isoprene isobutylene rubber, chloro- isobutene-isoprene rubber, brominated isobutene-isoprene rubber, silicone rubber, fluorocarbon rubber, polyurethane rubber, polysulfide rubber, thermoplastic rubber, thermoplastic starch (TPS), and mixtures thereof. According to another embodiment, the polymer formulation comprises the calcium carbonate- comprising material in an amount ranging from 3 to 85 wt.-%, preferably from 3 to 82 wt.-%, based on the total weight of the formulation.

According to yet another embodiment, the polymer resin is a bio-based polymer resin, preferably a bio-based polyolefin, thermoplastic starch or polyester resin or mixtures thereof, and most preferably a bio-based polyester.

According to one embodiment, the formulation further comprises additives such as colouring pigments, fibers, e.g. cellulose, glass or wood fibers, dyes, waxes, lubricants, oxidative- and/or UV- stabilizers, antioxidants and other fillers, such as carbon black, TiC>2, mica, clay, precipitated silica, talc or calcined kaolin.

According to another aspect, an article formed from the polymer formulation as defined herein is provided, preferably the article is selected from the group comprising hygiene products, medical and healthcare products, filter products, geotextile products, agriculture and horticulture products, clothing, footwear and baggage products, household and industrial products, packaging products, construction products, automotive parts, bottles, cups, bags, straws, flooring products, and the like.

According to another aspect, a process for preparing an article as defined herein is provided, wherein the process comprises the steps of a) providing a polymer resin, b) providing a calcium carbonate-comprising material as defined herein as filler, c) optionally providing further additives such as colouring pigments, fibers, e.g. cellulose, glass or wood fibers, dyes, waxes, lubricants, oxidative- and/or UV-stabilizers, antioxidants and other fillers, such as carbon black, TiC>2, mica, clay, precipitated silica, talc or calcined kaolin, d) contacting the components of step a), step b), and optionally step c) in any order to form a polymer formulation, and e) forming the polymer formulation of step d) such that an article is obtained.

According to another aspect, the use of the calcium carbonate-comprising material as defined herein in a polymer formulation comprising a polymer resin is provided, preferably the polymer resin is selected from the group comprising polyester, polyolefin, polyamide and mixtures thereof, more preferably polyethylene, polypropylene, polylactic acid, polylactic acid-based polymer, polyhydroxyalkanoates (PHA), e.g. polyhydroxybutyrate (PHB), poly-3- hydroxy butyrate (P3HB), poly3-hydroxybutyrate-co-3-hydroxyhexanoate (PHBH), polyhydroxyvalerate, polyhydroxybutyratepolyhydroxyvalerate copolymer, poly(3- hydroxybutyrate-co-3-hydroxyvalerate) (PHBV); polybutyrate- adipate-terephthalate (PBAT), polyglyconate, polyethylene terephthalate (PET), polycarbonate (PC), poly(dioxanone), polybutylene succinate (PBS), polycaprolactone (PCL), polycaprolactone- poly(ethylene glycol) copolymer, polycaprolactone-polylactic acid copolymer, polyvinylalcohol (PVA), polyethylene succinate) (PES), polypropylene succinate) (PPS), and mixtures thereof, most preferably polylactic acid, polylactic acid-based polymer, poly(3- hydroxy butyrate-co-3- hydroxyvalerate) (PHBV), polyhydroxyalkanoates (PHA) polyethylene terephthalate (PET), and mixtures thereof or the polymer resin is an elastomer resin, preferably an elastomer resin selected from natural or synthetic rubber, more preferably from the group consisting of acrylic rubber, butadiene rubber, acrylonitrile-butadiene rubber, epichlorhydrin rubber, isoprene rubber, ethylene-propylene rubber, ethylene-propylene-diene monomer rubber, nitrile-butadiene rubber, butyl rubber, styrenebutadiene rubber, polyisoprene, hydrogenated nitrile-butadiene rubber, carboxylated nitrile-butadiene rubber, chloroprene rubber, isoprene isobutylene rubber, chloro-isobutene-isoprene rubber, brominated isobutene-isoprene rubber, silicone rubber, fluorocarbon rubber, polyurethane rubber, polysulfide rubber, thermoplastic rubber, thermoplastic starch (TPS), and mixtures thereof.

It should be understood that for the purpose of the present invention, the following terms have the following meaning:

As used herein the term “polymer” generally includes homopolymers and co-polymers such as, for example, block, graft, random and alternating copolymers, as well as blends and modifications thereof. The polymer can be an amorphous polymer, a crystalline polymer, or a semi-crystalline polymer, i.e. a polymer comprising crystalline and amorphous fractions. The degree of crystallinity is specified in percent and can be determined by differential scanning calorimetry (DSC). An amorphous polymer may be characterized by its glass transition temperature and a crystalline polymer may be characterized by its melting point. A semi-crystalline polymer may be characterized by its glass transition temperature and/or its melting point.

The term “copolymer” as used herein refers to a polymer derived from more than one species of monomer. Copolymers that are obtained by copolymerization of two monomer species may also be termed bipolymers, those obtained from three monomers terpolymers, those obtained from four monomers quaterpolymers, etc. (cf. IUPAC Compendium of Chemical Terminology 2014, “copolymer”). Accordingly, the term “homopolymer” refers to a polymer derived from one species of monomer.

The term “glass transition temperature” in the meaning of the present invention refers to the temperature at which the glass transition occurs, which is a reversible transition in amorphous materials (or in amorphous regions within semi-crystalline materials) from a hard and relatively brittle state into a molten or rubber-like state. The glass-transition temperature is always lower than the melting point of the crystalline state of the material, if one exists. The term “melting point” in the meaning of the present invention refers to the temperature at which a solid changes state from solid to liquid at atmospheric pressure. At the melting point, the solid and liquid phase exist in equilibrium. Glass-transition temperature and melting point are determined by ISO 1 1357 with a heating rate of 10°C/min.

The term “treated” or “surface-treated” in the meaning of the present invention refers to a material which has been contacted with a surface treatment agent such as to obtain a coating layer on at least a part of the surface of the material.

The “particle size” of particulate materials is described herein by its weight-based distribution of particle sizes c/ _x . Therein, the value c/ _x represents the diameter relative to which x % by weight of the particles have diameters less than c/ _x . This means that, for example, the cfeo value is the particle size at which 20 wt.-% of all particles are smaller than that particle size. The cko value is thus the weight median particle size, i.e. 50 wt.-% of all particles are smaller than this particle size. For the purpose of the present invention, the particle size is specified as weight median particle size cfeo(wt) unless indicated otherwise. Particle sizes were determined by using a Sedigraph™ 5120 instrument of Micromeritics Instrument Corporation. The method and the instrument are known to the skilled person and are commonly used to determine the particle size of fillers and pigments. The measurements were carried out in an aqueous solution of 0.1 wt.-% Na4P2O?.

The “content of bio-based carbon” as used throughout the present application is determined according to DIN EN 16640:2017 as a fraction of total carbon. It is to be noted that in case of a treated calcium carbonate-comprising material, the bio-based carbon content is determined on the (surface-) treated calcium carbonate-comprising material.

The “specific surface area” (expressed in m ² /g) of a material as used throughout the present application can be determined by the Brunauer Emmett Teller (BET) method with nitrogen as adsorbing gas and by use of a ASAP 2460 instrument from Micromeritics. The method is well known to the skilled person and defined in ISO 9277:2010. Samples are conditioned at 100 °C under vacuum for a period of 30 min prior to measurement. The total surface area (in m ² ) of said material can be obtained by multiplication of the specific surface area (in m ² /g) and the mass (in g) of the material.

Unless specified otherwise, the term “drying” refers to a process according to which at least a portion of water is removed from a material to be dried such that a constant weight of the obtained “dried” material at 200°C is reached. Moreover, a “dried” or “dry” material may be defined by its total moisture content which, unless specified otherwise, is generally less than or equal to 1 .0 wt.-%, preferably < 0.8 wt.-%, more preferably < 0.5 wt.-% and most preferably < 0.3 wt.-%, based on the total weight of the dried material. The foregoing especially refers to intermediate products obtained by the process for the preparation of the calcium carbonate-comprising material as defined herein. As regards the calcium carbonate-comprising material of the present invention, the “dried” or “dry” calcium carbonate-comprising material has a total moisture content of less than or equal to 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably < 0.2 wt.-%, based on the total weight of the dried material.

Where an indefinite or definite article is used when referring to a singular noun, e.g., “a”, “an” or “the”, this includes a plural of that noun unless anything else is specifically stated.

Where the term “comprising” is used in the present description and claims, it does not exclude other elements. For the purposes of the present invention, the term “consisting of’ is considered to be a preferred embodiment of the term “comprising”. If hereinafter a group is defined to comprise at least a certain number of embodiments, this is also to be understood to disclose a group, which preferably consists only of these embodiments.

Terms like “obtainable” or “definable” and “obtained” or “defined” are used interchangeably. This, for example, means that, unless the context clearly dictates otherwise, the term “obtained” does not mean to indicate that, for example, an embodiment must be obtained by, for example, the sequence of steps following the term “obtained” though such a limited understanding is always included by the terms “obtained” or “defined” as a preferred embodiment.

Whenever the terms “including” or “having” are used, these terms are meant to be equivalent to “comprising” as defined hereinabove.

The calcium carbonate-comprising material of the present invention has

- a weight median particle size cko of < 60 pm,

- a top cut particle size dgs of < 500 pm, and

- a residual total moisture content of < 1 .0 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, wherein the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material.

In the following, preferred embodiments of the inventive products will be set out in more detail. It is to be understood that these embodiments and details also apply to the inventive methods fortheir preparation and their uses described herein.

The calcium carbonate-comprising material

The calcium carbonate-comprising material of the present invention has a content of biobased carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material.

For example, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material.

In addition thereto, the calcium carbonate-comprising material has

- a weight median particle size cko of < 60 pm,

- a top cut particle size dgs of < 500 pm, and

- a residual total moisture content of < 1 .0 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

For example, the calcium carbonate-comprising material has a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm.

Additionally or alternatively, the calcium carbonate-comprising material has a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm.

Additionally or alternatively, the calcium carbonate-comprising material has a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

Thus, the calcium carbonate-comprising material has

- a weight median particle size dso of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably < 2 pm, and

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm, and

- a residual total moisture content of < 1 .0 wt.-%, preferably < 0.5 wt.-%, more preferably

< 0.3 wt.-% and most preferably < 0.2 wt.-%, based on the total dry weight of the calcium carbonate- comprising material, and

- a content of bio-based carbon determined according to DIN EN 16640:2017 of at least

50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material.

In one embodiment, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, and/or

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, and/or

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

For example, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size cko of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, or

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, or

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, and

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, or

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, or

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, and

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, and

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, and

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material. For example, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size cko of < 2 pm, or

- a top cut particle size dgs of < 8 pm, or

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 2 pm, and

- a top cut particle size dgs of < 8 pm, or

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 2 pm, or

- a top cut particle size dgs of < 8 pm, and

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 2 pm, and

- a top cut particle size dgs of < 8 pm, and

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

Preferably, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, and/or

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, and/or

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

For example, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size cko of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, or

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, or

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, and

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, or

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, or

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, and

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, and

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, and

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

For example, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size cko of < 2 pm, or

- a top cut particle size dgs of < 8 pm, or

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 2 pm, and

- a top cut particle size dgs of < 8 pm, or

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 2 pm, or

- a top cut particle size dgs of < 8 pm, and

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 2 pm, and

- a top cut particle size dgs of < 8 pm, and

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

In one embodiment, the calcium carbonate-comprising material has a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Thus, in one embodiment, the calcium carbonate-comprising material has a content of biobased carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

In another embodiment, the calcium carbonate-comprising material has

- a weight median particle size dso of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably < 2 pm, and

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm and

- a residual total moisture content of < 1 .0 wt.-%, preferably < 0.5 wt.-%, more preferably

< 0.3 wt.-% and most preferably < 0.2 wt.-%, based on the total dry weight of the calcium carbonate- comprising material, and

- a content of bio-based carbon determined according to DIN EN 16640:2017 of at least

50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

For example, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size cko of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, and/or

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, and/or

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, and/or

- a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

For example, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, or

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, or

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, or

- a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, and - a top cut particle size d of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, or

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, or

- a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size cko of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, or

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, and

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, and

- a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, or

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, and

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, or

- a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, and

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, or

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, and - a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size cko of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, and

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, and

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, and

- a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

For example, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 2 pm, or

- a top cut particle size dgs of < 8 pm, or

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, or

- a specific surface area (BET) in the range from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 2 pm, and

- a top cut particle size dgs of < 8 pm, or

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, or

- a specific surface area (BET) in the range from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 2 pm, or

- a top cut particle size dgs of < 8 pm, and

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, and - a specific surface area (BET) in the range from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size cko of < 2 pm, or

- a top cut particle size dgs of < 8 pm, and

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, or

- a specific surface area (BET) in the range from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 2 pm, and

- a top cut particle size dgs of < 8 pm, or

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, and

- a specific surface area (BET) in the range from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a weight median particle size dso of < 2 pm, and

- a top cut particle size dgs of < 8 pm, and

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, and

- a specific surface area (BET) in the range from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Preferably, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, and/or

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, and/or

- a residual total moisture content of < < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, and/or - a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

For example, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size cko of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, or

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, or

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, or

- a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, and

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, or

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, or

- a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, or

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, and

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, and - a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size cko of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, or

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, and

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, or

- a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, and

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, or

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, and

- a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 20 pm, preferably < 6 pm, more preferably < 3 pm, and most preferably < 2 pm, and

- a top cut particle size dgs of < 200 pm, preferably < 20 pm, more preferably < 10 pm, and most preferably < 8 pm, and

- a residual total moisture content of < 0.5 wt.-%, preferably < 0.3 wt.-% and most preferably

< 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, and - a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably from 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

For example, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size cko of < 2 pm, or

- a top cut particle size dgs of < 8 pm, or

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, or

- a specific surface area (BET) in the range from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 2 pm, and

- a top cut particle size dgs of < 8 pm, or

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, or

- a specific surface area (BET) in the range from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 2 pm, or

- a top cut particle size dgs of < 8 pm, and

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, and

- a specific surface area (BET) in the range from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 2 pm, or

- a top cut particle size dgs of < 8 pm, and

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, or - a specific surface area (BET) in the range from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size cko of < 2 pm, and

- a top cut particle size dgs of < 8 pm, or

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, and

- a specific surface area (BET) in the range from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Alternatively, the calcium carbonate-comprising material has a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate- comprising material, and

- a weight median particle size dso of < 2 pm, and

- a top cut particle size dgs of < 8 pm, and

- a residual total moisture content of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate-comprising material, and

- a specific surface area (BET) in the range from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

It is appreciated that the calcium carbonate-comprising material is based on eggshells, seashells and/or oystershells. For example, the calcium carbonate-comprising material is based on eggshells or seashells or oystershells. Preferably, the calcium carbonate-comprising material is based on eggshells or oystershells. Most preferably, the calcium carbonate-comprising material is based on eggshells.

Preferably, the calcium carbonate-comprising material consists of eggshells, seashells and/or oystershells. For example, the calcium carbonate-comprising material consists of eggshells or seashells or oystershells.

In one embodiment, the calcium carbonate-comprising material is a mixture of materials comprising, preferably consisting of, eggshells and seashells. Alternatively, the calcium carbonate- comprising material is a mixture of materials comprising, preferably consisting of, eggshells and oystershells. Alternatively, the calcium carbonate-comprising material is a mixture of materials comprising, preferably consisting of, seashells and oystershells.

This is advantageous for obtaining a calcium carbonate-comprising material having a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material.

In one embodiment, the calcium carbonate-comprising material is a treated calcium carbonate-comprising material. That is to say, the calcium carbonate-comprising material is a treated calcium carbonate-comprising material comprising a treatment layer on the surface of the calcium carbonate-comprising material.

It is preferred that the treatment layer comprises a surface-treatment agent selected from the group consisting of

I) a phosphoric acid ester blend of one or more phosphoric acid mono ester and/or salts thereof and/or reaction products thereof and/or one or more phosphoric acid di-ester and/or salts thereof and/or reaction products thereof, or

II) at least one saturated or unsaturated aliphatic linear or branched carboxylic acid and/or salts thereof and/or reaction products thereof, preferably at least one aliphatic carboxylic acid having a total amount of carbon atoms from C4 to C24 and/or salts thereof and/or reaction products thereof, more preferably at least one aliphatic carboxylic acid having a total amount of carbon atoms from C12 to C20 and/or salts thereof and/or reaction products thereof, most preferably at least one aliphatic carboxylic acid having a total amount of carbon atoms from C16 to C18 and/or salts thereof and/or reaction products thereof, or

III) at least one mono-substituted succinic anhydride consisting of succinic anhydride mono-substituted with a group selected from a linear, branched, aliphatic and cyclic group having a total amount of carbon atoms from at least C2 to C30 in the substituent and/or salts thereof and/or reaction products thereof, and/or

IV) at least one polydialkylsiloxane, and/or

V) at least one cross-linkable compound comprising at least two functional groups, wherein at least one functional group is suitable for cross-linking a polymer resin and wherein at least one functional group is suitable for reacting with the calcium carbonate-comprising material, and/or

VI) at least one grafted polymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a homo- or copolymer comprising butadiene units and optionally styrene units and/or salts thereof and/or reaction products thereof, or

VII) mixtures of one or more materials according to I) to VI).

It is appreciated that the bio-based carbon content of the treated calcium carbonate- comprising material is at most 15 %, preferably at most 10 wt.-% and most preferably at most 5 wt.-% below the bio-based carbon content of the untreated calcium carbonate-comprising material.

In a preferred embodiment, the treatment layer comprises a surface-treatment agent selected from at least one mono-substituted succinic anhydride consisting of succinic anhydride monosubstituted with a group selected from a linear, branched, aliphatic and cyclic group having a total amount of carbon atoms from at least C2 to C30 in the substituent and/or reaction products thereof.

According to one embodiment of the present invention, the surface-treatment agent is a phosphoric acid ester blend of one or more phosphoric acid mono-ester and/or salts thereof and/or reaction products thereof and/or one or more phosphoric acid di-ester and/or salts thereof and/or reaction products thereof .

In one embodiment of the present invention, the one or more phosphoric acid mono-ester consists of an o-phosphoric acid molecule esterified with one alcohol selected from saturated, branched or linear, aliphatic or aromatic alcohols having a total amount of carbon atoms from C6 to C30 in the alcohol substituent. For example, the one or more phosphoric acid mono-ester consists of an o-phosphoric acid molecule esterified with one alcohol selected from saturated, branched or linear, aliphatic or aromatic alcohols having a total amount of carbon atoms from C8 to C22, more preferably from C8 to C20 and most preferably from C8 to C18 in the alcohol substituent.

Alkyl esters of phosphoric acid are well known in the industry especially as surfactants, lubricants and antistatic agents (Die Tenside; Kosswig und Stache, Carl Hanser Verlag Munchen, 1993).

The synthesis of alkyl esters of phosphoric acid by different methods and the surface treatment of minerals with alkyl esters of phosphoric acid are well known by the skilled man, e.g. from Pesticide Formulations and Application Systems: 17th Volume; Collins HM, Hall FR, Hopkinson M, STP1268; Published: 1996, US 3,897,519 A, US 4,921 ,990 A, US 4,350,645 A, US 6,710,199 B2, US 4,126,650 A, US 5,554,781 A, EP 1092000 B1 and WO 2008/023076 A1 .

In one embodiment of the present invention, the one or more phosphoric acid mono-ester consists of an o-phosphoric acid molecule esterified with one alcohol selected from saturated and linear or branched and aliphatic alcohols having a total amount of carbon atoms from Ce to C30 in the alcohol substituent. For example, the one or more phosphoric acid mono-ester consists of an 0- phosphoric acid molecule esterified with one alcohol selected from saturated and linear or branched and aliphatic alcohols having a total amount of carbon atoms from C8 to C22, more preferably from C8 to C20 and most preferably from C8 to C18 in the alcohol substituent.

In one embodiment of the present invention, the one or more phosphoric acid mono-ester consists of an o-phosphoric acid molecule esterified with one alcohol selected from saturated and linear and aliphatic alcohols having a total amount of carbon atoms from C6 to C30, preferably from C8 to C22, more preferably from C8 to C20 and most preferably from C8 to C18 in the alcohol substituent. Alternatively, the one or more phosphoric acid mono-ester consists of an o-phosphoric acid molecule esterified with one alcohol selected from saturated and branched and aliphatic alcohols having a total amount of carbon atoms from C6 to C30, preferably from C8 to C22, more preferably from C8 to C20 and most preferably from C8 to C18 in the alcohol substituent.

In one embodiment of the present invention, the one or more phosphoric acid mono-ester is selected from the group comprising hexyl phosphoric acid mono-ester, heptyl phosphoric acid monoester, octyl phosphoric acid mono-ester, 2-ethylhexyl phosphoric acid mono-ester, nonyl phosphoric acid mono-ester, decyl phosphoric acid mono-ester, undecyl phosphoric acid mono-ester, dodecyl phosphoric acid mono-ester, tetradecyl phosphoric acid mono-ester, hexadecyl phosphoric acid monoester, heptylnonyl phosphoric acid mono-ester, octadecyl phosphoric acid mono-ester, 2-octyl-1- decylphosphoric acid mono-ester, 2-octyl-1 -dodecylphosphoric acid mono-ester and mixtures thereof.

For example, the one or more phosphoric acid mono-ester is selected from the group comprising 2-ethylhexyl phosphoric acid mono-ester, hexadecyl phosphoric acid mono-ester, heptylnonyl phosphoric acid mono-ester, octadecyl phosphoric acid mono-ester, 2-octyl-1- decylphosphoric acid mono-ester, 2-octyl-1 -dodecylphosphoric acid mono-ester and mixtures thereof. In one embodiment of the present invention, the one or more phosphoric acid mono-ester is 2-octyl-1- dodecylphosphoric acid mono-ester. It is appreciated that the expression “one or more” phosphoric acid di-ester means that one or more kinds of phosphoric acid di-ester may be present in the treatment layer of the surface-treated material product and/or the phosphoric acid ester blend.

Accordingly, it should be noted that the one or more phosphoric acid di-ester may be one kind of phosphoric acid di-ester. Alternatively, the one or more phosphoric acid di-ester may be a mixture of two or more kinds of phosphoric acid di-ester. For example, the one or more phosphoric acid di-ester may be a mixture of two or three kinds of phosphoric acid di-ester, like two kinds of phosphoric acid diester.

In one embodiment of the present invention, the one or more phosphoric acid di-ester consists of an o-phosphoric acid molecule esterified with two alcohols selected from saturated, branched or linear, aliphatic or aromatic alcohols having a total amount of carbon atoms from C6 to C30 in the alcohol substituent. For example, the one or more phosphoric acid di-ester consists of an o- phosphoric acid molecule esterified with two fatty alcohols selected from saturated, branched or linear, aliphatic or aromatic alcohols having a total amount of carbon atoms from C8 to C22, more preferably from C8 to C20 and most preferably from C8 to C18 in the alcohol substituent.

It is appreciated that the two alcohols used for esterifying the phosphoric acid may be independently selected from the same or different saturated, branched or linear, aliphatic or aromatic alcohols having a total amount of carbon atoms from C6 to C30 in the alcohol substituent. In other words, the one or more phosphoric acid di-ester may comprise two substituents being derived from the same alcohols or the phosphoric acid di-ester molecule may comprise two substituents being derived from different alcohols.

In one embodiment of the present invention, the one or more phosphoric acid di-ester consists of an o-phosphoric acid molecule esterified with two alcohols selected from the same or different, saturated and linear or branched and aliphatic alcohols having a total amount of carbon atoms from C6 to C30 in the alcohol substituent. For example, the one or more phosphoric acid di-ester consists of an o-phosphoric acid molecule esterified with two alcohols selected from the same or different, saturated and linear or branched and aliphatic alcohols having a total amount of carbon atoms from C8 to C22, more preferably from C8 to C20 and most preferably from C8 to C18 in the alcohol substituent.

In one embodiment of the present invention, the one or more phosphoric acid di-ester consists of an o-phosphoric acid molecule esterified with two alcohols selected from the same or different, saturated and linear and aliphatic alcohols having a total amount of carbon atoms from C6 to C30, preferably from C8 to C22, more preferably from C8 to C20 and most preferably from C8 to C18 in the alcohol substituent. Alternatively, the one or more phosphoric acid di-ester consists of an o-phosphoric acid molecule esterified with two alcohols selected from the same or different, saturated and branched and aliphatic alcohols having a total amount of carbon atoms from C6 to C30, preferably from C8 to C22, more preferably from C8 to C20 and most preferably from C8 to C18 in the alcohol substituent.

In one embodiment of the present invention, the one or more phosphoric acid di-ester is selected from the group comprising hexyl phosphoric acid di-ester, heptyl phosphoric acid di-ester, octyl phosphoric acid di-ester, 2-ethylhexyl phosphoric acid di-ester, nonyl phosphoric acid di-ester, decyl phosphoric acid di-ester, undecyl phosphoric acid di-ester, dodecyl phosphoric acid di-ester, tetradecyl phosphoric acid di-ester, hexadecyl phosphoric acid di-ester, heptylnonyl phosphoric acid di-ester, octadecyl phosphoric acid di-ester, 2-octyl-1 -decylphosphoric acid di-ester, 2-octyl-1 -dodecylphosphoric acid di-ester and mixtures thereof.

For example, the one or more phosphoric acid di-ester is selected from the group comprising 2-ethylhexyl phosphoric acid di-ester, hexadecyl phosphoric acid di-ester, heptylnonyl phosphoric acid di-ester, octadecyl phosphoric acid di-ester, 2-octyl-1 -decylphosphoric acid di-ester, 2-octyl-1 -dodecylphosphoric acid di-ester and mixtures thereof. In one embodiment of the present invention, the one or more phosphoric acid di-ester is 2-octyl-1 -dodecylphosphoric acid di-ester.

In one embodiment of the present invention, the one or more phosphoric acid mono-ester is selected from the group comprising 2-ethylhexyl phosphoric acid mono-ester, hexadecyl phosphoric acid mono-ester, heptylnonyl phosphoric acid mono-ester, octadecyl phosphoric acid mono-ester, 2-octyl-1 -decylphosphoric acid mono-ester, 2-octyl-1 -dodecylphosphoric acid mono-ester and mixtures thereof and the one or more phosphoric acid di-ester is selected from the group comprising 2-ethylhexyl phosphoric acid di-ester, hexadecyl phosphoric acid di-ester, heptylnonyl phosphoric acid di-ester, octadecyl phosphoric acid di-ester, 2-octyl-1 -decylphosphoric acid di-ester, 2-octyl-1 -dodecylphosphoric acid di-ester and mixtures thereof.

According to another embodiment of the present invention, the surface-treatment agent is at least one saturated or unsaturated aliphatic linear or branched carboxylic acid and/or salts thereof and/or reaction products thereof preferably at least one aliphatic carboxylic acid having a total amount of carbon atoms from C4 to C24 and/or salts thereof and/or reaction products thereof, more preferably at least one aliphatic carboxylic acid having a total amount of carbon atoms from C12 to C20 and/or salts thereof and/or reaction products thereof, most preferably at least one aliphatic carboxylic acid having a total amount of carbon atoms from C16 to C18 and/or salts thereof and/or reaction products thereof.

The carboxylic acid in the meaning of the present invention may be selected from one or more linear chain, branched chain, saturated, or unsaturated and/or alicyclic carboxylic acids. Preferably, the aliphatic carboxylic acid is a monocarboxylic acid, i.e. the aliphatic carboxylic acid is characterized in that a single carboxyl group is present. Said carboxyl group is placed at the end of the carbon skeleton.

In one embodiment of the present invention, the aliphatic linear or branched carboxylic acid and/or salt thereof is selected from saturated unbranched carboxylic acids, preferably selected from the group of carboxylic acids consisting of pentanoic acid, hexanoic acid, heptanoic acid, octanoic acid, nonanoic acid, decanoic acid, undecanoic acid, lauric acid, tridecanoic acid, myristic acid, pentadecanoic acid, palmitic acid, heptadecanoic acid, stearic acid, nonadecanoic acid, arachidic acid, heneicosylic acid, behenic acid, tricosylic acid, lignoceric acid, their salts, their anhydrides and mixtures thereof.

In another embodiment of the present invention, the aliphatic linear or branched carboxylic acid and/or salt thereof is selected from the group consisting of octanoic acid, decanoic acid, lauric acid, myristic acid, palmitic acid, stearic acid, arachidic acid and mixtures thereof. Preferably, the aliphatic carboxylic acid is selected from the group consisting of myristic acid, palmitic acid, stearic acid, their salts, their anhydrides and mixtures thereof. Preferably, the aliphatic carboxylic acid and/or a salt or anhydride thereof is stearic acid and/or a stearic acid salt or stearic anhydride.

Alternatively, the unsaturated aliphatic linear or branched carboxylic acid is preferably selected from the group consisting of myristoleic acid, palmitoleic acid, sapienic acid, oleic acid, elaidic acid, vaccenic acid, linoleic acid, a-linolenic acid, eicosapentaenoic acid, docosahexaenoic acid and mixtures thereof. More preferably, the unsaturated aliphatic linear or branched carboxylic acid selected from the group consisting of myristoleic acid, palmitoleic acid, sapienic acid, oleic acid, elaidic acid, vaccenic acid, linoleic acid, a-linolenic acid and mixtures thereof. Most preferably, the unsaturated aliphatic linear or branched carboxylic acid is oleic acid and/or linoleic acid, preferably oleic acid or linoleic acid, most preferably linoleic acid.

Additionally or alternatively, the surface treatment agent is a salt of an unsaturated aliphatic linear or branched carboxylic acid.

The term “salt of an unsaturated aliphatic linear or branched carboxylic acid” refers to an unsaturated fatty acid, wherein the active acid group is partially or completely neutralized. The term “partially neutralized” unsaturated aliphatic linear or branched carboxylic acid refers to a degree of neutralization of the active acid groups in the range from 40 and 95 mole-% preferably from 50 to 95 mole-%, more preferably from 60 to 95 mole-% and most preferably from 70 to 95 mole-%. The term “completely neutralized” unsaturated aliphatic linear or branched carboxylic acid refers to a degree of neutralization of the active acid groups of > 95 mole-%, preferably of > 99 mole-%, more preferably of > 99.8 mole-% and most preferably of 100 mole-%. Preferably, the active acid groups are partially or completely neutralized.

The salt of unsaturated aliphatic linear or branched carboxylic acid is preferably a compound selected from the group consisting of sodium, potassium, calcium, magnesium, lithium, strontium, primary amine, secondary amine, tertiary amine and/or ammonium salts thereof, whereby the amine salts are linear or cyclic. For example, the unsaturated aliphatic linear or branched carboxylic acid is a salt of oleic acid and/or linoleic acid, preferably oleic acid or linoleic acid, most preferably linoleic acid.

According to another embodiment of the present invention, the surface-treatment agent is at least one mono-substituted succinic anhydride consisting of succinic anhydride mono-substituted with a group selected from a linear, branched, aliphatic and cyclic group having a total amount of carbon atoms from at least C2 to C30 in the substituent and/or salts thereof and/or reaction products thereof. Preferably, the surface-treatment agent is at least one mono-substituted succinic anhydride consisting of succinic anhydride mono-substituted with a group being a linear aliphatic group having a total amount of carbon atoms from at least C2 to C30 in the substituent and/or salts thereof and/or reaction products thereof. Additionally or alternatively, the surface-treatment agent is at least one monosubstituted succinic anhydride consisting of succinic anhydride mono-substituted with a group being a branched aliphatic group having a total amount of carbon atoms from at least C3 to C30 in the substituent and/or salts thereof and/or reaction products thereof. Additionally or alternatively, the surface-treatment agent is at least one mono-substituted succinic anhydride consisting of succinic anhydride mono-substituted with a group being a cyclic aliphatic group having a total amount of carbon atoms from at least C5 to C30 in the substituent and/or salts thereof and/or reaction products thereof. Accordingly, it should be noted that the at least one mono-substituted succinic anhydride may be one kind of mono-substituted succinic anhydride. Alternatively, the at least one mono-substituted succinic anhydride may be a mixture of two or more kinds of mono-substituted succinic anhydride. For example, the at least one mono-substituted succinic anhydride may be a mixture of two or three kinds of mono-substituted succinic anhydride, like two kinds of mono-substituted succinic anhydride.

In one embodiment of the present invention, the at least one mono-substituted succinic anhydride is one kind of mono-substituted succinic anhydride.

It is appreciated that the at least one mono-substituted succinic anhydride represents a surface treatment agent and consists of succinic anhydride mono-substituted with a group selected from any linear, branched, aliphatic, and cyclic group having a total amount of carbon atoms from C2 to C30 in the substituent.

In one embodiment of the present invention, the at least one mono-substituted succinic anhydride consists of succinic anhydride mono-substituted with a group selected from a linear, branched, aliphatic, and cyclic group having a total amount of carbon atoms from C3 to C20 in the substituent. For example, the at least one mono-substituted succinic anhydride consists of succinic anhydride mono-substituted with a group selected from a linear, branched, aliphatic, and cyclic group having a total amount of carbon atoms from C4 to C18 in the substituent. Preferably, the surfacetreatment agent is at least one mono-substituted succinic anhydride consisting of succinic anhydride mono-substituted with a group being a linear aliphatic group having a total amount of carbon atoms from C3 to C20, more preferably from C4 to C18, in the substituent and/or salts thereof and/or reaction products thereof. Additionally or alternatively, the surface-treatment agent is at least one mono-substituted succinic anhydride consisting of succinic anhydride mono-substituted with a group being a branched aliphatic group having a total amount of carbon atoms from C3 to C20, more preferably from C4 to C18, in the substituent and/or salts thereof and/or reaction products thereof. Additionally or alternatively, the surface-treatment agent is at least one mono-substituted succinic anhydride consisting of succinic anhydride mono-substituted with a group being a cyclic aliphatic group having a total amount of carbon atoms from C5 to C20, more preferably from C5 to C18 in the substituent and/or salts thereof and/or reaction products thereof.

In one embodiment of the present invention, the at least one mono-substituted succinic anhydride consists of succinic anhydride mono-substituted with one group being a linear and aliphatic group having a total amount of carbon atoms from C2 to C30, preferably from C3 to C20 and most preferably from C4 to C18 in the substituent. Additionally or alternatively, the at least one monosubstituted succinic anhydride consists of succinic anhydride mono-substituted with one group being a branched and aliphatic group having a total amount of carbon atoms from C3 to C30, preferably from C3 to C20 and most preferably from C4 to C18 in the substituent.

Thus, it is preferred that the at least one mono-substituted succinic anhydride consists of succinic anhydride mono-substituted with one group being a linear alkyl group having a total amount of carbon atoms from C2 to C30, preferably from C3 to C20 and most preferably from C4 to C18 in the substituent. Additionally or alternatively, it is preferred that the at least one mono-substituted succinic anhydride consists of succinic anhydride mono-substituted with one group being a branched alkyl group having a total amount of carbon atoms from C3 to C30, preferably from C3 to C20 and most preferably from C4 to C18 in the substituent.

For example, the at least one mono-substituted succinic anhydride consists of succinic anhydride mono-substituted with one group being a linear alkyl group having a total amount of carbon atoms from C2 to C30, preferably from C3 to C20 and most preferably from C4 to C18 in the substituent. Additionally or alternatively, the at least one mono-substituted succinic anhydride consists of succinic anhydride mono-substituted with one group being a branched alkyl group having a total amount of carbon atoms from C3 to C30, preferably from C3 to C20 and most preferably from C4 to C18 in the substituent.

In one embodiment of the present invention, the at least one mono-substituted succinic anhydride is at least one linear or branched alkyl mono-substituted succinic anhydride. For example, the at least one alkyl mono-substituted succinic anhydride is selected from the group comprising ethylsuccinic anhydride, propylsuccinic anhydride, butylsuccinic anhydride, triisobutyl succinic anhydride, pentylsuccinic anhydride, hexylsuccinic anhydride, heptylsuccinic anhydride, octylsuccinic anhydride, nonylsuccinic anhydride, decyl succinic anhydride, dodecyl succinic anhydride, hexadecanyl succinic anhydride, octadecanyl succinic anhydride, and mixtures thereof.

Accordingly, it is appreciated that, e.g., the term “butylsuccinic anhydride” comprises linear and branched butylsuccinic anhydride(s). One specific example of linear butylsuccinic anhydride(s) is n-butylsuccinic anhydride. Specific examples of branched butylsuccinic anhydride(s) are isobutylsuccinic anhydride, sec-butylsuccinic anhydride and/or tert-butylsuccinic anhydride.

Furthermore, it is appreciated that, e.g., the term “hexadecanyl succinic anhydride” comprises linear and branched hexadecanyl succinic anhydride(s). One specific example of linear hexadecanyl succinic anhydride(s) is n-hexadecanyl succinic anhydride. Specific examples of branched hexadecanyl succinic anhydride(s) are 14-methylpentadecanyl succinic anhydride, 13-methylpentadecanyl succinic anhydride, 12-methylpentadecanyl succinic anhydride,

11-methylpentadecanyl succinic anhydride, 10-methylpentadecanyl succinic anhydride, 9-methylpentadecanyl succinic anhydride, 8-methylpentadecanyl succinic anhydride, 7-methylpentadecanyl succinic anhydride, 6-methylpentadecanyl succinic anhydride, 5-methylpentadecanyl succinic anhydride, 4-methylpentadecanyl succinic anhydride, 3-methylpentadecanyl succinic anhydride, 2-methylpentadecanyl succinic anhydride,

1-methylpentadecanyl succinic anhydride, 13-ethylbutadecanyl succinic anhydride,

12-ethylbutadecanyl succinic anhydride, 11-ethylbutadecanyl succinic anhydride, 10-ethylbutadecanyl succinic anhydride, 9-ethylbutadecanyl succinic anhydride, 8-ethylbutadecanyl succinic anhydride, 7-ethylbutadecanyl succinic anhydride, 6-ethylbutadecanyl succinic anhydride, 5-ethylbutadecanyl succinic anhydride, 4-ethylbutadecanyl succinic anhydride, 3-ethylbutadecanyl succinic anhydride,

2-ethylbutadecanyl succinic anhydride, 1-ethylbutadecanyl succinic anhydride, 2-butyldodecanyl succinic anhydride, 1-hexyldecanyl succinic anhydride, 1-hexyl-2-decanyl succinic anhydride, 2-hexyldecanyl succinic anhydride, 6,12-dimethylbutadecanyl succinic anhydride, 2,2-diethyldodecanyl succinic anhydride, 4,8,12-trimethyltridecanyl succinic anhydride, 2,2,4,6,8-pentamethylundecanyl succinic anhydride, 2-ethyl-4-methyl-2-(2-methylpentyl)-heptyl succinic anhydride and/or 2-ethyl-4,6-dimethyl-2-propylnonyl succinic anhydride. Furthermore, it is appreciated that e.g. the term “octadecanyl succinic anhydride” comprises linear and branched octadecanyl succinic anhydride(s). One specific example of linear octadecanyl succinic anhydride(s) is n-octadecanyl succinic anhydride. Specific examples of branched hexadecanyl succinic anhydride(s) are 16-methylheptadecanyl succinic anhydride, 15-methylheptadecanyl succinic anhydride, 14-methylheptadecanyl succinic anhydride, 13-methylheptadecanyl succinic anhydride, 12-methylheptadecanyl succinic anhydride, 11-methylheptadecanyl succinic anhydride, 10-methylheptadecanyl succinic anhydride, 9-methylheptadecanyl succinic anhydride, 8-methylheptadecanyl succinic anhydride, 7-methylheptadecanyl succinic anhydride, 6-methylheptadecanyl succinic anhydride,

5-methylheptadecanyl succinic anhydride, 4-methylheptadecanyl succinic anhydride, 3-methylheptadecanyl succinic anhydride, 2-methylheptadecanyl succinic anhydride,

I-methylheptadecanyl succinic anhydride, 14-ethylhexadecanyl succinic anhydride, 13-ethylhexadecanyl succinic anhydride, 12-ethylhexadecanyl succinic anhydride,

I I-ethylhexadecanyl succinic anhydride, 10-ethylhexadecanyl succinic anhydride, 9-ethylhexadecanyl succinic anhydride, 8-ethylhexadecanyl succinic anhydride, 7-ethylhexadecanyl succinic anhydride,

6-ethylhexadecanyl succinic anhydride, 5-ethylhexadecanyl succinic anhydride, 4-ethylhexadecanyl succinic anhydride, 3-ethylhexadecanyl succinic anhydride, 2-ethylhexadecanyl succinic anhydride, 1-ethylhexadecanyl succinic anhydride, 2-hexyldodecanyl succinic anhydride, 2-heptylundecanyl succinic anhydride, iso-octadecanyl succinic anhydride and/or 1-octyl-2-decanyl succinic anhydride.

In one embodiment of the present invention, the at least one alkyl mono-substituted succinic anhydride is selected from the group comprising butylsuccinic anhydride, hexylsuccinic anhydride, heptylsuccinic anhydride, octylsuccinic anhydride, hexadecanyl succinic anhydride, octadecanyl succinic anhydride, and mixtures thereof.

In one embodiment of the present invention, the at least one mono-substituted succinic anhydride is one kind of alkyl mono-substituted succinic anhydride. For example, the one alkyl monosubstituted succinic anhydride is butylsuccinic anhydride. Alternatively, the one alkyl mono-substituted succinic anhydride is hexylsuccinic anhydride. Alternatively, the one alkyl mono-substituted succinic anhydride is heptylsuccinic anhydride or octylsuccinic anhydride. Alternatively, the one alkyl monosubstituted succinic anhydride is hexadecanyl succinic anhydride. For example, the one alkyl monosubstituted succinic anhydride is linear hexadecanyl succinic anhydride such as n-hexadecanyl succinic anhydride or branched hexadecanyl succinic anhydride such as 1-hexyl-2-decanyl succinic anhydride. Alternatively, the one alkyl mono-substituted succinic anhydride is octadecanyl succinic anhydride. For example, the one alkyl mono-substituted succinic anhydride is linear octadecanyl succinic anhydride such as n-octadecanyl succinic anhydride or branched octadecanyl succinic anhydride such as iso-octadecanyl succinic anhydride or 1-octyl-2-decanyl succinic anhydride.

In one embodiment of the present invention, the one alkyl mono-substituted succinic anhydride is butylsuccinic anhydride such as n-butylsuccinic anhydride.

In one embodiment of the present invention, the at least one mono-substituted succinic anhydride is a mixture of two or more kinds of alkyl mono-substituted succinic anhydrides. For example, the at least one mono-substituted succinic anhydride is a mixture of two or three kinds of alkyl mono-substituted succinic anhydrides. According to another embodiment of the present invention, the surface-treatment agent is at least one polydialkylsiloxane.

Preferred polydialkylsiloxanes are described e.g. in US 2004/0097616 A1. Most preferred are polydialkylsiloxanes selected from the group consisting of polydimethylsiloxane, preferably dimethicone, polydiethylsiloxane and polymethylphenylsiloxane and/or mixtures thereof.

For example, the at least one polydialkylsiloxane is preferably a polydimethylsiloxane (PDMS).

According to another embodiment of the present invention, the surface-treatment agent is at least one cross-linkable compound comprising at least two functional groups, wherein at least one functional group is suitable for cross-linking a polymer resin and wherein at least one functional group is suitable for reacting with the calcium carbonate-comprising material.

The term “at least one” cross-linkable compound comprising at least two functional groups in the meaning of the present invention means that the cross-linkable compound comprises, preferably consists of, one or more cross-linkable compound(s) comprising at least two functional groups.

In one embodiment of the present invention, the at least one cross-linkable compound comprising at least two functional groups comprises, preferably consists of, one cross-linkable compound. Alternatively, the at least one cross-linkable compound comprising at least two functional groups comprises, preferably consists of, two or more cross-linkable compounds. For example, the at least one cross-linkable compound comprising at least two functional groups comprises, preferably consists of, two or three cross-linkable compounds.

Preferably, the at least one cross-linkable compound comprising at least two functional groups comprises, more preferably consists of, one cross-linkable compound comprising at least two functional groups.

It is appreciated that the at least one cross-linkable compound comprising at least two functional groups comprises at least one functional group that is suitable for cross-linking a polymer resin.

For the purposes of the present invention, a “cross-linkable compound” is a compound, which comprises functional groups, e.g., carbon multiple bonds, halogen functional groups, sulfur functional groups, or hydrocarbon moieties, and which upon crosslinking is suitable for cross-linking a polymer resin. The inventors surprisingly found out that such a cross-linkable compound can react with the polymer resin, i.e. the polymer precursor, in a crosslinking step, e.g., a chemical crosslinking step. In this way, the polymer resin is (evenly) distributed all over the surface of the calcium carbonate- comprising material such that, even if used in small amounts only, the chemical compatibility in the polymer resin and the mechanical properties of the polymer product are improved.

Additionally, the at least one cross-linkable compound comprising at least two functional groups comprises at least one functional group that is suitable for reacting with the calcium carbonate- comprising material. For example, the at least one functional group that is suitable for reacting with the calcium carbonate-comprising material of the cross-linkable compound comprises one or more terminal triethoxysilyl, trimethoxysilyl and/or organic acid anhydride and/or salts thereof and/or carboxylic acid group(s) and/or salts thereof. Preferably, the at least one functional group that is suitable for reacting with the calcium carbonate-comprising material of the cross-linkable compound comprises one or more terminal triethoxysilyl, trimethoxysilyl or organic acid anhydride and/or salts thereof or carboxylic acid group(s) and/or salts thereof.

In a preferred embodiment, the at least one functional group that is suitable for reacting with the calcium carbonate-comprising material of the cross-linkable compound comprises one or more organic acid anhydride and/or salts thereof or carboxylic acid group(s) and/or salts thereof. Most preferably, the at least one functional group that is suitable for reacting with the calcium carbonate- comprising material of the cross-linkable compound comprises one or more organic acid anhydride group(s) and/or salts thereof. Alternatively, the at least one functional group that is suitable for reacting with the calcium carbonate-comprising material of the cross-linkable compound comprises one or more triethoxysilyl or trimethoxysilyl functional group(s) and/or salts thereof.

Preferably, the one or more organic acid anhydride group(s) is/are one or more succinic anhydride group(s) obtained by grafting maleic anhydride onto a homo- or copolymer.

In view of this, the at least one functional group that is suitable for reacting with the calcium carbonate-comprising material of the cross-linkable compound preferably comprises, more preferably consists of, one or more succinic anhydride group(s) obtained by grafting maleic anhydride onto a homo- or copolymer. For example, the at least one functional group that is suitable for reacting with the calcium carbonate-comprising material of the cross-linkable compound preferably comprises, more preferably consists of, one succinic anhydride group obtained by grafting maleic anhydride onto a homo- or copolymer. Alternatively, the at least one functional group that is suitable for reacting with the calcium carbonate-comprising material of the cross-linkable compound preferably comprises, more preferably consists of, two or more succinic anhydride groups obtained by grafting maleic anhydride onto a homo- or copolymer, e.g. from 2 to 12, particularly from 2 to 9 such as from 2 to 6, succinic anhydride groups. Alternatively, the at least one functional group that is suitable for reacting with the calcium carbonate-comprising material of the cross-linkable compound preferably comprises, more preferably consists of, one triethoxysilyl or trimethoxysilyl functional group. For example, the at least one functional group that is suitable for reacting with the calcium carbonate-comprising material of the cross-linkable compound preferably comprises, more preferably consists of, two or more triethoxysilyl or trimethoxysilyl functional groups, e.g. from 2 to 12, particularly from 2 to 9 such as from 2 to 6, triethoxysilyl or trimethoxysilyl functional groups.

It is appreciated that the at least one functional group that is suitable for reacting with the calcium carbonate-comprising material of the cross-linkable compound may be present as salt, preferably in the form of the sodium or potassium salt.

In view of the foregoing, the at least one cross-linkable compound comprising at least two functional groups may comprise two or more functional groups, e.g. one or more functional group(s) that is/are suitable for cross-linking a polymer resin and one or more functional group(s) that is/are suitable for reacting with the calcium carbonate-comprising material.

In a preferred embodiment, the at least one cross-linkable compound comprising at least two functional groups preferably comprises two functional groups, e.g. one functional group that is suitable for cross-linking a polymer resin and one functional group that is suitable for reacting with the calcium carbonate-comprising material. It is appreciated that the number of functional groups in the at least one cross-linkable compound refers to the number of different functional groups, i.e. functional groups not having the same chemical structure. That is to say, if the at least one cross-linkable compound comprises e.g. two functional groups, the two functional groups are of different chemical structures, whereas each of the two different functional groups may be present one or more times.

According to one embodiment, the at least one cross-linkable compound comprising at least two functional groups is at least one grafted polymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a homo- or copolymer comprising butadiene units and optionally styrene units.

The term “grafted” or “maleic anhydride grafted” means that a succinic anhydride is obtained after reaction of substituent(s) R ¹ and/or R ² comprising a carbon-carbon double bond with the double bond of maleic anhydride. Thus, the terms “grafted homopolymer” and “grafted copolymer” refer to a corresponding homopolymer and copolymer each bearing succinic anhydride moieties formed from the reaction of a carbon-carbon double bond with the double bond of maleic anhydride, respectively. It is appreciated the at least one grafted polymer or maleic anhydride grafted polymer may be also referred to as “polymer, e.g. polybutadiene, functionalized with maleic anhydride” or “polymer, e.g. polybutadiene, adducted maleic anhydride”.

That is to say, the at least one cross-linkable compound comprising at least two functional groups is preferably a grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer or a grafted polybutadiene-styrene copolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene-styrene copolymer. More preferably, the at least one cross-linkable compound comprising at least two functional groups is a grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer.

According to an alternative embodiment, the at least one cross-linkable compound comprising at least two functional groups is a sulfur-containing trialkoxysilane, preferably a compound comprising two trialkoxysilyl alkyl groups linked with a polysulfide.

If the at least one cross-linkable compound comprising at least two functional groups is a grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer, the grafted polybutadiene homopolymer preferably has i) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, and/or ii) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, and/or iii) an anhydride equivalent weight in the range from 400 to 2 200, preferably from 500 to 2 000, and more preferably from 550 to 1 800. In one embodiment, the grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer preferably has i) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, or ii) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, or iii) an anhydride equivalent weight in the range from 400 to 2200, preferably from 500 to 2 000, and more preferably from 550 to 1 800.

In a preferred embodiment, the grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer preferably has i) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, and ii) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, and iii) an anhydride equivalent weight in the range from 400 to 2 200, preferably from 500 to 2 000, and more preferably from 550 to 1 800.

Additionally or alternatively, the grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer has an acid number in the range from 10 to 300 meq KOH per g of grafted polybutadiene homopolymer, preferably 20 to 200 meq KOH / g, more preferably 30 to 150 meq KOH I g, measured according to ASTM D974-14.

In one embodiment, the grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer thus has i) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, and ii) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, and iii) an anhydride equivalent weight in the range from 400 to 2 200, preferably from 500 to 2 000, and more preferably from 550 to 1 800, and iv) an acid number in the range from 10 to 300 meq KOH per g of grafted polybutadiene homopolymer, preferably 20 to 200 meq KOH I g, more preferably 30 to 150 meq KOH I g, measured according to ASTM D974-14.

Additionally or alternatively, the grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer has a Brookfield viscosity at 25°C in the range from 3 000 to 70 000 cPs, preferably in the range from 5 000 to 50 000 cPs. Alternatively, the maleic anhydride grafted polybutadiene homopolymer has a Brookfield viscosity at 55°C in the range from 100 000 to 170 000 cPs, preferably in the range from 120 000 to 160 000 cPs.

In one embodiment, the grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer thus has i) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, and ii) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, and iii) an anhydride equivalent weight in the range from 400 to 2 200, preferably from 500 to 2 000, and more preferably from 550 to 1 800, and iv) an acid number in the range from 10 to 300 meq KOH per g of grafted polybutadiene homopolymer, preferably 20 to 200 meq KOH / g, more preferably 30 to 150 meq KOH I g, measured according to ASTM D974-14, and v) a Brookfield viscosity at 25°C in the range from 3 000 to 70 000 cPs, preferably in the range from 5 000 to 50 000 cPs.

For example, the grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer may have a number average molecular weight M _n measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, more preferably from 2 000 to 10 000 g/mol, an acid number in the range from 20 to 200 meq KOH per g of grafted polybutadiene homopolymer, preferably 30 to 150 meq KOH I g, measured according to ASTM D974-14. In another embodiment, the grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer may have a number average molecular weight M _n measured by gel permeation chromatography from 2000 to 5000 g/mol, an acid number in the range from 30 to 100 meq KOH / g, measured according to ASTM D974-14.

In one embodiment, the grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer has a number average molecular weight Mn measured by gel permeation chromatography from 2 000 to 10 000 g/mol, preferably from 2 000 to 4 500 g/mol or from 4 500 to 7 000 g/mol, a number of functional groups per chain in the range from 2 to 6, preferably from 2 to 4 or from 4 to 6, an anhydride equivalent weight in the range from 550 to 1 800, preferably from 550 to 1 000 or from 1 000 to 1 800, and a Brookfield viscosity at 25°C in the range from 5 000 to 50 000 cPs, preferably from 5 000 to 10 000 cPs or from 35 000 to 50 000 cPs.

For example, the grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer has a number average molecular weight Mn measured by gel permeation chromatography from 2 000 to 4 500 g/mol, a number of functional groups per chain in the range from 2 to 4, an anhydride equivalent weight in the range from 1 000 to 1 800, and a Brookfield viscosity at 25°C in the range from 5 000 to 10 000 cPs. In an alternative embodiment, the grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer has a number average molecular weight Mn measured by gel permeation chromatography from 4 500 to 7 000 g/mol, a number of functional groups per chain in the range from 4 to 6, an anhydride equivalent weight in the range from 550 to 1 000, and a Brookfield viscosity at 25°C in the range from 35 000 to 50 000 cPs. In an alternative embodiment, the grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer has a number average molecular weight Mn measured by gel permeation chromatography from 2 500 to 4 500 g/mol, a number of functional groups per chain in the range from 2 to 4, an anhydride equivalent weight in the range from 550 to 1 000, and a Brookfield viscosity at 55°C in the range from 120 000 to 160 000 cPs.

Additionally or alternatively, the at least one cross-linkable compound comprising at least two functional groups is a grafted polybutadiene-styrene copolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene-styrene copolymer and having i) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, and/or ii) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, and/or iii) an anhydride equivalent weight in the range from 400 to 2 200, preferably from 500 to 2 000, and more preferably from 550 to 1 800, and/or iv) a 1 ,2 vinyl content from 20 to 80 mol.-%, preferably from 20 to 40 mol.-%, based on the total weight of the grafted polybutadiene-styrene copolymer.

In one embodiment, the grafted polybutadiene-styrene copolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene-styrene copolymer preferably has i) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, or ii) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, or iii) an anhydride equivalent weight in the range from 400 to 2 200, preferably from 500 to 2 000, and more preferably from 550 to 1 800, or iv) a 1 ,2 vinyl content from 20 to 80 mol.-%, preferably from 20 to 40 mol.-%, based on the total weight of the grafted polybutadiene-styrene copolymer.

In a preferred embodiment, the grafted polybutadiene-styrene copolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene-styrene copolymer preferably has i) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, and ii) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, and iii) an anhydride equivalent weight in the range from 400 to 2 200, preferably from 500 to 2 000, and more preferably from 550 to 1 800, and iv) a 1 ,2 vinyl content from 20 to 80 mol.-%, preferably from 20 to 40 mol.-%, based on the total weight of the grafted polybutadiene-styrene copolymer.

Additionally or alternatively, the grafted polybutadiene-styrene copolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene-styrene copolymer has a Brookfield viscosity at 45°C in the range from 100 000 to 200 000 cPs, preferably in the range from 150 000 to 200 000 cPs.

In one embodiment, the grafted polybutadiene-styrene copolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene-styrene copolymer has a number average molecular weight Mn measured by gel permeation chromatography from 2 000 to 10 000 g/mol, a number of functional groups per chain in the range from 2 to 6, an anhydride equivalent weight in the range from 550 to 1 800, and a Brookfield viscosity at 45°C in the range from 150 000 to 200 000 cPs.

According to yet another embodiment of the present invention, the at least one cross-linkable compound is a sulfur-containing trialkoxysilane.

In one embodiment, the sulfur-containing trialkoxysilane is preferably selected from the group comprising, preferably consisting of, mercaptopropyltrimethoxysilane (MPTS), mercaptopropyltriethoxysilane, bis(triethoxysilylpropyl) disulfide (TESPD), bis(triethoxysilylpropyl) tetrasulfide (TESPT), 3-aminopropyltrimethoxysilane (APTMS), 3-aminopropyltriethoxysilane, and mixtures thereof.

In one embodiment, the sulfur-containing trialkoxysilane is preferably a compound comprising two trialkoxysilyl alkyl groups linked with a polysulfide. For example, the compound comprising two trialkoxysilyl alkyl groups linked with a polysulfide is selected from bis(triethoxysilylpropyl) disulfide (TESPD), bis(triethoxysilylpropyl) tetrasulfide (TESPT) and mixtures thereof. Preferably, the compound comprising two trialkoxysilyl alkyl groups linked with a polysulfide is bis(triethoxysilylpropyl) tetrasulfide (TESPT).

According to another embodiment of the present invention, the surface-treatment agent is at least one grafted polymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a homo- or copolymer comprising butadiene units and optionally styrene units and/or salts thereof and/or reaction products thereof.

It is appreciated that the “at least one grafted polymer” comprises, preferably consists of, one or more grafted polymer(s). For example, the “at least one grafted polymer” comprises, preferably consists of, one grafted polymer. Alternatively, the “at least one grafted polymer” comprises, preferably consists of, two or more, preferably two, grafted polymers.

Preferably, the “at least one grafted polymer” comprises, preferably consists of, one grafted polymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a homo- or copolymer comprising butadiene units and optionally styrene units and/or salts thereof and/or reaction products thereof. It is appreciated that the at least one grafted polymer comprises at least one succinic anhydride group obtained by grafting maleic anhydride onto a homo- or copolymer comprising butadiene units and optionally styrene units and/or salts thereof and/or reaction products thereof. The term “at least one” succinic anhydride group obtained by grafting maleic anhydride onto a homo- or copolymer comprising butadiene units and optionally styrene units and/or salts thereof and/or reaction products thereof in the meaning of the present invention means that the grafted polymer comprises, preferably consists of, one or more succinic anhydride group(s) obtained by grafting maleic anhydride onto a homo- or copolymer comprising butadiene units and optionally styrene units and/or salts thereof and/or reaction products thereof.

In view of this, the at least one grafted polymer preferably comprises one or more succinic anhydride group(s) obtained by grafting maleic anhydride onto a homo- or copolymer. For example, the at least one grafted polymer comprises one succinic anhydride group obtained by grafting maleic anhydride onto a homo- or copolymer. Alternatively, the at least one grafted polymer comprises two or more succinic anhydride groups obtained by grafting maleic anhydride onto a homo- or copolymer, e.g. from 2 to 12, particularly from 2 to 9 such as from 2 to 6, succinic anhydride groups.

The term “grafted” or “maleic anhydride grafted” means that a succinic anhydride is obtained after reaction of substituent(s) R ¹ and/or R ² comprising a carbon-carbon double bond with the double bond of maleic anhydride. Thus, the terms “grafted homopolymer” and “grafted copolymer” refer to a corresponding homopolymer and copolymer each bearing succinic anhydride moieties formed from the reaction of a carbon-carbon double bond with the double bond of maleic anhydride, respectively. It is appreciated the at least one grafted polymer or maleic anhydride grafted polymer may be also referred to as “polymer, e.g. polybutadiene, functionalized with maleic anhydride” or “polymer, e.g. polybutadiene, adducted maleic anhydride”.

It is appreciated that the at least one succinic anhydride group may be present as salt, preferably in the form of the sodium or potassium salt.

Preferably, the one or more succinic anhydride group(s) of the at least one grafted polymer is/are suitable for reacting with the calcium carbonate-comprising material.

According to one embodiment, the at least one grafted polymer comprises at least one unsubstituted succinic anhydride group obtained by grafting maleic anhydride onto a homo- or copolymer comprising butadiene units and/or salts thereof and/or reaction products thereof and optionally styrene units. The term “unsubstituted” succinic anhydride group obtained by grafting maleic anhydride onto a homo- or copolymer comprising butadiene units and/or salts thereof and/or reaction products thereof and optionally styrene units means that the succinic anhydride group comprises only substituents which are linked to the homo- or copolymer backbone. In other words, the succinic anhydride group is free of substituents which are not linked to the homo- or copolymer backbone.

That is to say, the at least one grafted polymer is preferably a grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer or a grafted polybutadiene-styrene copolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene-styrene copolymer. For example, the at least one grafted polymer is preferably a grafted polybutadiene homopolymer comprising at least one unsubstituted succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer or a grafted polybutadiene-styrene copolymer comprising at least one unsubstituted succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene-styrene copolymer. More preferably, the at least one grafted polymer is a grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer. For example, the at least one grafted polymer is preferably a grafted polybutadiene homopolymer comprising at least one unsubstituted succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer.

If the at least one grafted polymer is a grafted polybutadiene homopolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer, the grafted polybutadiene homopolymer preferably has i) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, and/or ii) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, and/or iii) an anhydride equivalent weight in the range from 400 to 2 200, preferably from 500 to 2 000, and more preferably from 550 to 1 800.

In one embodiment, the grafted polybutadiene homopolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer preferably has iv) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, or v) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, or vi) an anhydride equivalent weight in the range from 400 to 2 200, preferably from 500 to 2 000, and more preferably from 550 to 1 800.

In a preferred embodiment, the grafted polybutadiene homopolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer preferably has iv) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, and v) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, and vi) an anhydride equivalent weight in the range from 400 to 2 200, preferably from 500 to 2 000, and more preferably from 550 to 1 800.

Additionally or alternatively, the grafted polybutadiene homopolymer comprising at least one succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer has an acid number in the range from 10 to 300 meq KOH per g of grafted polybutadiene homopolymer, preferably 20 to 200 meq KOH / g, more preferably 30 to 150 meq KOH / g, measured according to ASTM D974-14.

In one embodiment, the grafted polybutadiene homopolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer thus has i) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, and ii) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, and iii) an anhydride equivalent weight in the range from 400 to 2 200, preferably from 500 to 2 000, and more preferably from 550 to 1 800, and iv) an acid number in the range from 10 to 300 meq KOH per g of grafted polybutadiene homopolymer, preferably 20 to 200 meq KOH / g, more preferably 30 to 150 meq KOH I g, measured according to ASTM D974-14.

Additionally or alternatively, the grafted polybutadiene homopolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer has a Brookfield viscosity at 25°C in the range from 3 000 to 70 000 cPs, preferably in the range from 5 000 to 50 000 cPs. Alternatively, the grafted polybutadiene homopolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer has a Brookfield viscosity at 55°C in the range from 100 000 to 170 000 cPs, preferably in the range from 120 000 to 160 000 cPs.

In one embodiment, the grafted polybutadiene homopolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer thus has i) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, and ii) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, and iii) an anhydride equivalent weight in the range from 400 to 2 200, preferably from 500 to 2 000, and more preferably from 550 to 1 800, and iv) an acid number in the range from 10 to 300 meq KOH per g of grafted polybutadiene homopolymer, preferably 20 to 200 meq KOH / g, more preferably 30 to 150 meq KOH I g, measured according to ASTM D974-14, and v) a Brookfield viscosity at 25°C in the range from 3 000 to 70 000 cPs, preferably in the range from 5 000 to 50 000 cPs.

The term “grafted” means that a succinic anhydride group is obtained obtained after reaction of substituent(s) R ¹ and/or R ² comprising a carbon-carbon double bond with the double bond of maleic anhydride. For example, the grafted polybutadiene homopolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer may have a number average molecular weight M _n measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, more preferably from 2 000 to 10 000 g/mol, an acid number in the range from 20 to 200 meq KOH per g of grafted polybutadiene homopolymer, preferably 30 to 150 meq KOH / g, measured according to ASTM D974- 14. In another embodiment, the grafted polybutadiene homopolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer may have a number average molecular weight M _n measured by gel permeation chromatography from 2000 to 5000 g/mol, an acid number in the range from 30 to 100 meq KOH / g, measured according to ASTM D974-14.

In one embodiment, the grafted polybutadiene homopolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer has a number average molecular weight Mn measured by gel permeation chromatography from 2 000 to 10 000 g/mol, preferably from 2 000 to 4 500 g/mol or from 4 500 to 7 000 g/mol, a number of functional groups per chain in the range from 2 to 6, preferably from 2 to 4 or from 4 to 6, an anhydride equivalent weight in the range from 550 to 1 800, preferably from 550 to

1 000 or from 1 000 to 1 800, and a Brookfield viscosity at 25°C in the range from 5 000 to 50 000 cPs, preferably from 5 000 to 10 000 cPs or from 35 000 to 50 000 cPs.

For example, the grafted polybutadiene homopolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer has a number average molecular weight Mn measured by gel permeation chromatography from 2 000 to 4 500 g/mol, a number of functional groups per chain in the range from

2 to 4, an anhydride equivalent weight in the range from 1 000 to 1 800, and a Brookfield viscosity at 25°C in the range from 5 000 to 10 000 cPs. In an alternative embodiment, the grafted polybutadiene homopolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer has a number average molecular weight Mn measured by gel permeation chromatography from 4 500 to 7 000 g/mol, a number of functional groups per chain in the range from 4 to 6, an anhydride equivalent weight in the range from 550 to

1 000, and a Brookfield viscosity at 25°C in the range from 35 000 to 50 000 cPs. In an alternative embodiment, the grafted polybutadiene homopolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene homopolymer has a number average molecular weight Mn measured by gel permeation chromatography from 2 500 to 4 500 g/mol, a number of functional groups per chain in the range from

2 to 4, an anhydride equivalent weight in the range from 550 to 1 000, and a Brookfield viscosity at 55°C in the range from 120 000 to 160 000 cPs.

Additionally or alternatively, the at least one grafted polymer is a grafted polybutadienestyrene copolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene-styrene copolymer and having i) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, and/or ii) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, and/or iii) an anhydride equivalent weight in the range from 400 to 2 200, preferably from 500 to 2 000, and more preferably from 550 to 1 800, and/or iv) a 1 ,2 vinyl content from 20 to 80 mol.-%, preferably from 20 to 40 mol.-%, based on the total weight of the grafted polybutadiene-styrene copolymer.

In one embodiment, the grafted polybutadiene-styrene copolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene-styrene copolymer preferably has i) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, or ii) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, or iii) an anhydride equivalent weight in the range from 400 to 2 200, preferably from 500 to 2 000, and more preferably from 550 to 1 800, or iv) a 1 ,2 vinyl content from 20 to 80 mol.-%, preferably from 20 to 40 mol.-%, based on the total weight of the grafted polybutadiene-styrene copolymer.

In a preferred embodiment, the grafted polybutadiene-styrene copolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene-styrene copolymer preferably has i) a number average molecular weight Mn measured by gel permeation chromatography from 1 000 to 20 000 g/mol, preferably from 1 400 to 15 000 g/mol, and more preferably from 2 000 to 10 000 g/mol measured according to EN ISO 16014-1 :2019, and ii) a number of functional groups per chain in the range from 2 to 12, preferably from 2 to 9, and more preferably from 2 to 6, and iii) an anhydride equivalent weight in the range from 400 to 2 200, preferably from 500 to 2 000, and more preferably from 550 to 1 800, and iv) a 1 ,2 vinyl content from 20 to 80 mol.-%, preferably from 20 to 40 mol.-%, based on the total weight of the grafted polybutadiene-styrene copolymer.

Additionally or alternatively, the (grafted polybutadiene-styrene copolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene-styrene copolymer has a Brookfield viscosity at 45°C in the range from 100 000 to 200 000 cPs, preferably in the range from 150 000 to 200 000 cPs.

In one embodiment, the grafted polybutadiene-styrene copolymer comprising at least one (preferably unsubstituted) succinic anhydride group obtained by grafting maleic anhydride onto a polybutadiene-styrene copolymer has a number average molecular weight Mn measured by gel permeation chromatography from 2 000 to 10 000 g/mol, a number of functional groups per chain in the range from 2 to 6, an anhydride equivalent weight in the range from 550 to 1 800, and a Brookfield viscosity at 45°C in the range from 150 000 to 200 000 cPs.

In a preferred embodiment, the treatment layer comprises a surface-treatment agent selected from at least one mono-substituted succinic anhydride consisting of succinic anhydride monosubstituted with a group selected from a linear, branched, aliphatic and cyclic group having a total amount of carbon atoms from at least C2 to C30 in the substituent and/or reaction products thereof.

The treated calcium carbonate-comprising material is preferably formed in that the calcium carbonate-comprising material is contacted with the surface-treatment agent such that a treatment layer comprising the surface-treatment agent and/or salts thereof and/or reaction products thereof is/are formed on the surface of the calcium carbonate-comprising material.

The term "reaction products" of the surface-treatment agent refers to products obtained by contacting the calcium carbonate-comprising material with the surface-treatment agent. Said reaction products are formed between at least a part of the applied surface-treatment agent and reactive molecules located at the surface of the calcium carbonate-comprising material. Thus, the reaction products include salts of the surface-treatment agent and/or other reaction products such as hydrolysis products and/or their salts.

The treated calcium carbonate-comprising material preferably comprises the treatment layer in an amount ranging from 0.1 to 3 wt.-%, preferably from 0.1 to 1 .2 wt.-% based on the total weight of the treated calcium carbonate-comprising material, and/or in an amount ranging from 0.2 to 5.0 mg/m ² of the BET specific surface area of the calcium carbonate-comprising material and preferably from 0.5 to 3.0 mg/m ² of the BET specific surface area of the calcium carbonate-comprising material

It is to be noted that the treated calcium carbonate-comprising material typically has a residual total moisture content that is below the residual total moisture content of the (untreated) calcium carbonate-comprising material.

Thus, the treated calcium carbonate-comprising material preferably has a residual total moisture content of < 0.7 wt.-%, preferably of < 0.5 wt.-%, more preferably < 0.3 wt.-% and most preferably of < 0.2 wt.-%, based on the total dry weight of the treated calcium carbonate-comprising material.

Additionally or alternatively, the treated calcium carbonate-comprising material preferably has a moisture pick-up susceptibility of < 6 mg/g, preferably < 3 mg/g, more preferably < 2 mg/g, and most preferably < 1 .5 mg/g, based on the total dry weight of the treated calcium carbonate-comprising material.

In one embodiment, the treated calcium carbonate-comprising material preferably has

- a residual total moisture content of < 0.7 wt.-%, preferably of < 0.5 wt.-%, more preferably < 0.3 wt.-% and most preferably of < 0.2 wt.-%, based on the total dry weight of the treated calcium carbonate-comprising material, or

- a moisture pick-up susceptibility of < 6 mg/g, preferably < 3 mg/g, more preferably < 2 mg/g, and most preferably < 1 .5 mg/g, based on the total dry weight of the treated calcium carbonate- comprising material.

Alternatively, the treated calcium carbonate-comprising material preferably has - a residual total moisture content of < 0.7 wt.-%, preferably of < 0.5 wt.-%, more preferably

< 0.3 wt.-% and most preferably of < 0.2 wt.-%, based on the total dry weight of the treated calcium carbonate-comprising material, and

- a moisture pick-up susceptibility of < 6 mg/g, preferably < 3 mg/g, more preferably < 2 mg/g, and most preferably < 1 .5 mg/g, based on the total dry weight of the treated calcium carbonate- comprising material.

Thus, the treated calcium carbonate-comprising material has

- a weight median particle size cko of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably < 2 pm, and

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm, and

- a residual total moisture content of < 0.7 wt.-%, preferably of < 0.5 wt.-%, more preferably

< 0.3 wt.-% and most preferably of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate- comprising material, and

- a content of bio-based carbon determined according to DIN EN 16640:2017 of at least

50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material.

In one embodiment, the treated calcium carbonate-comprising material has

- a weight median particle size dso of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably < 2 pm, and

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm, and

- a residual total moisture content of < 0.7 wt.-%, preferably of < 0.5 wt.-%, more preferably

< 0.3 wt.-% and most preferably of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate- comprising material, and

- a content of bio-based carbon determined according to DIN EN 16640:2017 of at least

50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a moisture pick-up susceptibility of < 6 mg/g, preferably < 3 mg/g, more preferably < 2 mg/g, and most preferably < 1 .5 mg/gbased on the total dry weight of the treated calcium carbonate- comprising material.

In another embodiment, the treated calcium carbonate-comprising material has

- a weight median particle size dso of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably < 2 pm, and

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm, and

- a residual total moisture content of < 0.7 wt.-%, preferably of < 0.5 wt.-%, more preferably

< 0.3 wt.-% and most preferably of < 0.2 wt.-%, based on the total dry weight of the calcium carbonate- comprising material, and - a content of bio-based carbon determined according to DIN EN 16640:2017 of at least

50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, and

- a moisture pick-up susceptibility of < 6 mg/g, preferably < 3 mg/g, more preferably < 2 mg/g, and most preferably < 1 .5 mg/g, based on the total dry weight of the treated calcium carbonate- comprising material, and

- a specific surface area (BET) in the range from 1 to 50 m ² /g, preferably 2.5 to 15 m ² /g, and most preferably from 3 to 9 m ² /g, as measured using nitrogen and the BET method according to ISO 9277.

Process for the preparation of the calcium carbonate-comprising material

According to one aspect of the present invention, the calcium carbonate-comprising material of the present invention is obtainable by a process comprising the steps of: a) providing a calcium carbonate-comprising material having a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the material, and b) grinding the calcium carbonate-comprising material of step a) to

- a weight median particle size cko of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably of < 2 pm,

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm.

It is preferred that the calcium carbonate-comprising material is based on eggshells, seashells and/or oystershells.

According to one embodiment, the calcium carbonate-comprising material provided in step a) has a weight median particle size dso ranging from 100 pm to 10.0 mm, preferably from 300 pm to 6.0 mm, more preferably from 400 pm to 5.5 mm and most preferably from 500 pm to 5.0 mm.

Additionally or alternatively, the calcium carbonate-comprising material provided in step a) has an amount of acid insolubles of < 5 wt.-%, preferably < 3 wt.-% and most preferably < 2 wt.-%, based on the total weight of the calcium carbonate-comprising material.

It is appreciated that grinding step b) can be carried out by any grinding means known in the art. In general, the grinding step can be carried out with any conventional grinding device, for example, under conditions such that refinement predominantly results from impacts with a secondary body, i.e. in one or more of: a ball mill, a rod mill, a vibrating mill, a roll crusher, a centrifugal impact mill, a vertical bead mill, an attrition mill, a pin mill, a hammer mill, a pulveriser, a shredder, a de-clumper, a knife cutter, or other such equipment known to the skilled man. Furthermore, grinding step b) can be carried out by dry grinding or wet grinding.

It is preferred that grinding step b) is carried out by wet grinding. Thus, the calcium carbonate- comprising material of step a) is preferably provided in form of an aqueous suspension.

The aqueous suspension subjected to step b) may have any solids content that is suitable to be subjected to a wet grinding. However, in order to obtain the inventive calcium carbonate-comprising material it is specifically advantageous that the aqueous suspension subjected to step b) has a relatively low solids content. Thus, it is preferred that the aqueous suspension subjected to step b) has a solids content in the range from 1 to 40 wt.-%, preferably from 2 to 35 wt.-%, based on the total weight of the aqueous suspension.

The term “wet grinding” in the meaning of the process according to the present invention refers to the comminution (e.g., in a ball mill, semi-autogenous mill, or autogenous mill) of solid material (e.g., of mineral origin) in the presence of water meaning that said material is in form of an aqueous slurry or suspension.

For the purposes of the present invention, any suitable mill known in the art may be used. However, said wet grinding step is preferably carried out in a ball mill. It has to be noted that step b) is carried out in at least one wet grinding step, i.e. it is also possible to use a series of grinding units which may, for example, be selected from ball mills, semi-autogenous mills, or autogenous mills. Preferably, step b) is carried out in one wet grinding step.

It is appreciated that wet grinding step b) can be carried out at room temperature or elevated temperatures. It is for example possible that the temperature of the aqueous suspension when starting step b) is of about room temperature, whereas the temperature may rise until the end of wet grinding step b). That is to say, it is preferred that the temperature during wet grinding step b) is not adjusted to a specific temperature.

Alternatively, the temperature during wet grinding step b) is held at a specific temperature by cooling the aqueous suspension.

For the purposes of the process according to the present invention, wet grinding step b) is preferably carried out at a temperature ranging from 2 to 90°C. According to another embodiment, the temperature in wet grinding step b) ranges from 2 to 80°C, preferably from 2 to 70°C, and most preferably from 2 to 60°C.

It is of further advantageous for obtaining a residual total moisture content of < 1 .0 wt.-%, if the grinding step b) is carried out in the absence of dispersant(s). For obtaining a residual total moisture content of < 1 .0 wt.-%, it is especially preferred if the grinding step b) is carried out by wet grinding in the absence of dis persa nt(s). More preferably, the grinding step b) is carried out by wet grinding at solids content in the range from 1 to 40 wt.-%, preferably from 2 to 35 wt.-%, based on the total weight of the aqueous suspension, in the absence of dispersant(s). It may be also advantageous to subject the calcium carbonate-comprising material obtained after grinding step b) to a dewatering step in order to further reduce the moisture content. Thus, the process for the preparation of the calcium carbonate- comprising material preferably comprises a step d) of drying the calcium carbonate-comprising material after grinding step b).

For the sake of completeness, it is preferred that the whole process for preparing the calcium carbonate-comprising material is carried out in the absence of dispersant(s). Thus, the calcium carbonate-comprising material is free of dispersant(s).

It is appreciated that the calcium carbonate-comprising material obtained after grinding step b) has a

- a weight median particle size cfeo of < 60 pm,

- a top cut particle size dgs of < 500 pm, and - a residual total moisture content of < 1 .0 wt.-%, based on the total dry weight of the calcium carbonate-comprising material.

With regard to the definition of the calcium carbonate-comprising material and preferred embodiments thereof, reference is made to the statements provided above when discussing the technical details of the calcium carbonate-comprising material of the present invention.

As already mentioned above, the calcium carbonate-comprising material can be a treated calcium carbonate-comprising material.

In this embodiment, the process further comprises step c) in which the calcium carbonate- comprising material is contacted under mixing, in one or more steps, with a surface-treatment agent such that a treatment layer comprising the surface-treatment agent and/or salts thereof and/or reaction products thereof is formed on the surface of the calcium carbonate-comprising material.

It is appreciated that the treatment layer on the surface of the calcium carbonate-comprising material is formed by contacting the calcium or magnesium carbonate-comprising material with the further surface-treatment agent. The calcium carbonate-comprising material is contacted with the surface-treatment agent in an amount from 0.1 to 10 mg/m ² of the calcium carbonate-comprising material surface, preferably 0.1 to 8 mg/m ² , more preferably 0.11 to 3 mg/m ² and most preferably 0.2 to 3 mg/m ² . That is to say, a chemical reaction may take place between the calcium carbonate- comprising material and the surface treatment agent. In other words, the treatment layer may comprise the surface treatment agent and/or salts thereof and/or reaction products thereof.

Methods for the surface treatment of fillers such as calcium carbonate-comprising materials are known to the skilled person, and are described, for example, in EP3192837 A1 , EP2770017 A1 , and WO2016023937.

It is appreciated that the calcium carbonate-comprising material in step c) is preferably provided in dry form. Additionally or alternatively, the surface-treatment agent in step c) is preferably provided in dry form. Preferably, the calcium carbonate-comprising material in step c) is provided in dry form and the surface-treatment agent in step c) is provided in dry form. In a preferred embodiment, the treated calcium carbonate-comprising material is thus prepared in a dry process step. With respect to the process, it is to be noted that the wording “dry form” means that the calcium carbonate- comprising material in step c) and/or the surface-treatment agent in step c) is/are provided without the use of solvent(s) such as water.

However, it is also possible that the treated calcium carbonate-comprising material is prepared in a wet process step, which is well known to the skilled person.

It is appreciated that the temperature in optional step c) is adjusted such that the surfacetreatment agent is in a liquid or molten state but without thermally decomposing the surface-treatment agent. In general, step c) is carried out at a temperature that is at least 2°C, preferably 5°C above the melting point of the surface-treatment agent.

Additionally or alternatively, step c) is carried out at a temperature ranging from 50 to 130°C, preferably from 60 to 120°C, e.g. from 80 to 120°C.

In one embodiment, step c) is carried out at a temperature that is at least 2°C, preferably 5°C above the melting point of the surface-treatment agent, and at a temperature ranging from 50 to 130°C, preferably from 60 to 120°C, e.g. from 80 to 120°C. Step c) is carried out under mixing. It is appreciated that the mixing can be carried out by any method or in any vessel known to the skilled person resulting in a homogeneous composition. For example, step c) is carried out in a high speed mixer or pin mill.

Thus, the treated calcium carbonate-comprising material of the present invention is obtainable by a process comprising the steps of: a) providing a calcium carbonate-comprising material having a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the material, and b) grinding the calcium carbonate-comprising material of step a) to

- a weight median particle size cko of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably of < 2 pm,

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm, and c) contacting the calcium carbonate-comprising material obtained in step b) under mixing, in one or more steps, with a surface-treatment agent such that a treatment layer comprising the surface-treatment agent and/or salts thereof and/or reaction products thereof is formed on the surface of the calcium carbonate-comprising material.

With regard to the definition of the treated calcium carbonate-comprising material and preferred embodiments thereof, reference is made to the statements provided above when discussing the technical details of the calcium carbonate-comprising material of the present invention.

It is appreciated that the process for the preparation of the calcium carbonate-comprising material may comprise further steps. For example, the process for the preparation of the calcium carbonate-comprising material further comprises a step d) of drying the calcium carbonate-comprising material before and/or after grinding step b) and optionally before surface-treating step c).

In one embodiment, the process for the preparation of the calcium carbonate-comprising material further comprises a step d) of drying the calcium carbonate-comprising material before and/or after grinding step b), preferably before or after grinding step b). If the present process comprises step c) of surface-treating the calcium carbonate-comprising material, drying step d) is preferably carried out before surface-treating step c), i.e. after grinding step b). Such a drying step d), which is carried out before surface-treating step c) is specifically advantageous as step c) is preferably carried out in the absence of solvents. Thus, it is preferred that a dried calcium carbonate-comprising material is subjected to surface-treating step c).

In another embodiment, the process for the preparation of the calcium carbonate-comprising material further comprises a step d) of drying the calcium carbonate-comprising material before and after grinding step b).

For example, the drying in step d) is achieved by up-concentration or dewatering to achieve a higher solids content than that of step b) and the solids content achieved in step d) is at least 98, wt.-%, preferably at least 99 wt.-% and most preferably at least 99.5 wt.-%, based on the total weight of the aqueous suspension. The drying in step d) is carried out by means known to the skilled person such as by mechanical- and/or thermal up-concentration or dewatering and/or combinations thereof.

Mechanical up-concentration or dewatering can be carried out by centrifugation or by filter pressing. Thermal up-concentration or dewatering can be carried out by methods such as solvent evaporation by heat or by flash-cooling.

Preferably, the drying in step d) is carried out by thermal up-concentration. In one embodiment, the thermal up-concentration is carried out in combination with vacuum.

In one embodiment, the drying in step d) is carried out such as to achieve a higher solids content than that of step b) and the solids content achieved in step d) is at least 99.7 wt.-%, preferably of at least 99.8 wt.-% and most preferably at least 99.9 wt.-%, based on the total weight of the calcium carbonate-comprising material. Preferably, the calcium carbonate-comprising material is thus a dry calcium carbonate-comprising material.

It is appreciated that the drying in step d) is carried out without a decrease in particle size of the calcium carbonate-comprising material.

Additionally or alternatively, the process for the preparation of the calcium carbonate- comprising material further comprises a step e) of grinding, cleaning, washing and/or bleaching the calcium carbonate-comprising material before and/or after grinding step b).

For example, the process for the preparation of the calcium carbonate-comprising material further comprises a step e) of grinding such as dry-grinding and/or wet-grinding the calcium carbonate-comprising material before grinding step b). Preferably, the process for the preparation of the calcium carbonate-comprising material further comprises a step e) of grinding such as dry-grinding or wet-grinding the calcium carbonate-comprising material before grinding step b).

In one embodiment, the process for the preparation of the calcium carbonate-comprising material further comprises a step e) of dry-grinding the calcium carbonate-comprising material before grinding step b).

In another embodiment, the process for the preparation of the calcium carbonate-comprising material further comprises a step e) of wet-grinding the calcium carbonate-comprising material before grinding step b), preferably at solids content ranging from 20 to 60 wt.-%, based on the total weight of the aqueous suspension.

Thus, the process for the preparation of the calcium carbonate-comprising material preferably further comprises a step e) of grinding the calcium carbonate-comprising material before grinding step b).

If the process for the preparation of the calcium carbonate-comprising material comprises grinding step e), it is appreciated that the product resulting from grinding step e) is used as a feed for subsequent grinding step b). In this embodiment, it is especially preferred that the product resulting from grinding step e) is used as a feed for the subsequent grinding step b) which is carried out by wetgrinding.

It is appreciated that the process for the preparation of the calcium carbonate-comprising material may further comprise one or more steps e) of washing, e.g. by using NaOH or H2O2, and/or bleaching, e.g. by using NaOCI or H2O2. Preferably, such washing and/or bleaching steps can be carried out before grinding step b). More preferably, such washing and/or bleaching steps e) can be carried out after grinding step e) and the product resulting from such washing and/or bleaching steps is used as a feed for subsequent grinding step b).

Alternatively, the process for the preparation of the calcium carbonate-comprising material may further comprise a cleaning step e). Preferably, such cleaning step e), e.g. by using membrane removal methods can be carried out before grinding step b). More preferably, such cleaning step e) by e.g. membrane removal methods can be carried out after grinding step e) and the product resulting from such cleaning step is used as a feed for subsequent grinding step b).

Such cleaning, washing and/or bleaching steps are well known in the art and do not need to be described in more detail herein.

Thus, the calcium carbonate-comprising material of the present invention is obtainable by a process comprising the steps of: a) providing a calcium carbonate-comprising material having a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the material, and b) grinding the calcium carbonate-comprising material of step a) to

- a weight median particle size cko of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably of < 2 pm,

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm, and d) optionally drying the calcium carbonate-comprising material before and/or after grinding step b) and optionally before surface-treating step c), and/or e) optionally grinding, cleaning, washing and/or bleaching the calcium carbonate- comprising material before and/or after grinding step b).

In a preferred embodiment, the calcium carbonate-comprising material of the present invention is obtainable by a process comprising the steps of: a) providing a calcium carbonate-comprising material having a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the material, e) grinding the calcium carbonate-comprising material of step a) by wet- or dry-grinding, preferably in the absence of dispersants, and b) grinding the calcium carbonate-comprising material obtained in step e) to

- a weight median particle size dso of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably of < 2 pm,

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm, and e) optionally cleaning, washing and/or bleaching the calcium carbonate-comprising material before and/or after grinding step b).

For example, the calcium carbonate-comprising material of the present invention is obtainable by a process comprising the steps of: a) providing a calcium carbonate-comprising material having a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the material, e) grinding the calcium carbonate-comprising material of step a) by dry-grinding, and b) grinding the calcium carbonate-comprising material obtained in step e) to

- a weight median particle size cko of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably of < 2 pm,

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm, and e) optionally cleaning, washing and/or bleaching the calcium carbonate-comprising material before and/or after grinding step b).

In one embodiment, the treated calcium carbonate-comprising material of the present invention is obtainable by a process comprising the steps of: a) providing a calcium carbonate-comprising material having a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the material, e) grinding the calcium carbonate-comprising material of step a) by wet- or dry-grinding, preferably in the absence of dispersants, and b) grinding the calcium carbonate-comprising material obtained in step e) to

- a weight median particle size dso of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably of < 2 pm,

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm, and c) contacting the calcium carbonate-comprising material obtained in step b) under mixing, in one or more steps, with a surface-treatment agent such that a treatment layer comprising the surface-treatment agent and/or salts thereof and/or reaction products thereof is formed on the surface of the calcium carbonate-comprising material.

For example, the treated calcium carbonate-comprising material of the present invention is obtainable by a process comprising the steps of: a) providing a calcium carbonate-comprising material having a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the material, e) grinding the calcium carbonate-comprising material of step a) by dry-grinding, and b) grinding the calcium carbonate-comprising material obtained in step e) to

- a weight median particle size dso of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably of < 2 pm,

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm, and c) contacting the calcium carbonate-comprising material obtained in step b) under mixing, in one or more steps, with a surface-treatment agent such that a treatment layer comprising the surface-treatment agent and/or salts thereof and/or reaction products thereof is formed on the surface of the calcium carbonate-comprising material, and e) optionally cleaning, washing and/or bleaching the calcium carbonate-comprising material before and/or after grinding step b).

In one embodiment, the process further comprises a step d) of drying the calcium carbonate- comprising material before and/or after grinding step b), preferably after grinding step b). In this embodiment, the treated calcium carbonate-comprising material of the present invention is thus obtainable by a process comprising the steps of: a) providing a calcium carbonate-comprising material having a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the material, e) grinding the calcium carbonate-comprising material of step a) by wet- or dry-grinding, preferably in the absence of dispersants, and b) grinding the calcium carbonate-comprising material obtained in step e) to

- a weight median particle size cko of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably of < 2 pm,

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm, and c) contacting the calcium carbonate-comprising material obtained in step b) under mixing, in one or more steps, with a surface-treatment agent such that a treatment layer comprising the surface-treatment agent and/or salts thereof and/or reaction products thereof is formed on the surface of the calcium carbonate-comprising material, and d) drying the calcium carbonate-comprising material before and/or after grinding step b).

For example, the treated calcium carbonate-comprising material of the present invention is obtainable by a process comprising the steps of: a) providing a calcium carbonate-comprising material having a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the material, e) grinding the calcium carbonate-comprising material of step a) by dry-grinding, and b) grinding the calcium carbonate-comprising material obtained in step e) to

- a weight median particle size dso of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably of < 2 pm,

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm, c) contacting the calcium carbonate-comprising material obtained in step b) under mixing, in one or more steps, with a surface-treatment agent such that a treatment layer comprising the surface-treatment agent and/or salts thereof and/or reaction products thereof is formed on the surface of the calcium carbonate-comprising material, and d) drying the calcium carbonate-comprising material after grinding step b) and before surface-treating step c).

In one embodiment, the process further comprises a step e) of cleaning, washing and/or bleaching the calcium carbonate-comprising material before and/or after grinding step b). In this embodiment, the treated calcium carbonate-comprising material of the present invention is thus obtainable by a process comprising the steps of: a) providing a calcium carbonate-comprising material having a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the material, e) grinding the calcium carbonate-comprising material of step a) by wet- or dry-grinding, preferably in the absence of dispersants, and b) grinding the calcium carbonate-comprising material obtained in step e) to

- a weight median particle size cko of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably of < 2 pm,

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm, and c) contacting the calcium carbonate-comprising material obtained in step b) under mixing, in one or more steps, with a surface-treatment agent such that a treatment layer comprising the surface-treatment agent and/or salts thereof and/or reaction products thereof is formed on the surface of the calcium carbonate-comprising material, and d) drying the calcium carbonate-comprising material before and/or after grinding step b), and e) cleaning, washing and/or bleaching the calcium carbonate-comprising material before and/or after grinding step b).

For example, the treated calcium carbonate-comprising material of the present invention is obtainable by a process comprising the steps of: a) providing a calcium carbonate-comprising material having a content of bio-based carbon determined according to DIN EN 16640:2017 of at least 50 wt.-%, preferably at least 60 wt.-%, more preferably at least 70 wt.-%, and most preferably at least 80 wt.-%, based on the total weight of carbon in the material, e) grinding the calcium carbonate-comprising material of step a) by dry-grinding, and b) grinding the calcium carbonate-comprising material obtained in step e) to

- a weight median particle size dso of < 60 pm, preferably < 20 pm, more preferably < 6 pm, even more preferably < 3 pm, and most preferably of < 2 pm,

- a top cut particle size dgs of < 500 pm, preferably < 200 pm, more preferably < 20 pm, even more preferably < 10 pm, and most preferably < 8 pm, c) contacting the calcium carbonate-comprising material obtained in step b) under mixing, in one or more steps, with a surface-treatment agent such that a treatment layer comprising the surface-treatment agent and/or salts thereof and/or reaction products thereof is formed on the surface of the calcium carbonate-comprising material, and d) drying the calcium carbonate-comprising material after grinding step b) and before surface-treating step c), and e) cleaning, washing and/or bleaching the calcium carbonate-comprising material before and/or after grinding step b).

Articles, their preparation and uses

Another aspect of the present invention refers to a polymer formulation comprising a polymer resin and the calcium carbonate-comprising material as defined herein, wherein the calcium carbonate-comprising material according is dispersed in the polymer resin.

With regard to the definition of the calcium carbonate-comprising material and preferred embodiments thereof, reference is made to the statements provided above when discussing the technical details of the calcium carbonate-comprising material of the present invention.

The polymer formulation preferably comprises the calcium carbonate-comprising material in an amount ranging from 3 to 85 wt.-%, preferably from 3 to 82 wt.-%, based on the total weight of the formulation.

It should be noted that the polymer resin may be one kind of polymer resin. Alternatively, the polymer resin may be a mixture of two or more kinds of polymer resins. For example, the polymer resin may be a mixture of two or three kinds of polymer resins, like two kinds of polymer resins.

In one embodiment of the present invention, the polymer resin comprises, preferably consists of, one kind of polymer resin.

The polymer resin is preferably selected from the group comprising polyester, polyolefin, polyamide and mixtures thereof.

For example, the polymer resin is selected from the group comprising, e.g. consisting of, polyethylene, polypropylene, polylactic acid, polylactic acid-based polymer, polyhydroxyalkanoates (PHA), e.g. polyhydroxybutyrate (PHB), poly-3- hydroxy butyrate (P3HB), poly3-hydroxybutyrate-co-3- hydroxyhexanoate (PHBH), polyhydroxyvalerate, polyhydroxybutyrate-polyhydroxyvalerate copolymer, poly(3- hydroxybutyrate-co-3-hydroxyvalerate) (PHBV); polybutyrate-adipate-terephthalate (PBAT), polyglyconate, polyethylene terephthalate (PET), polycarbonate (PC), poly(dioxanone), polybutylene succinate (PBS), polycaprolactone (PCL), polycaprolactone-poly(ethylene glycol) copolymer, polycaprolactone-polylactic acid copolymer, polyvinylalcohol (PVA), polyethylene succinate) (PES), polypropylene succinate) (PPS), and mixtures thereof,

Preferably, the polymer resin is a polyester, more preferably the polymer resin is selected from the group comprising, e.g. consisting of, polylactic acid, polylactic acid-based polymer, poly(3- hydroxybutyrate-co-3-hydroxyvalerate) (PHBV), polyhydroxyalkanoates (PHA), polyethylene terephthalate (PET), polybutylene succinate (PBS), polycaprolactone (PCL), polybutyrate-adipate- terephthalate (PBAT) and mixtures thereof.

More preferably, the polymer resin is selected from the group comprising, e.g. consisting of, polylactic acid, polylactic acid-based polymer, poly(3- hydroxybutyrate-co-3-hydroxyvalerate) (PHBV), polyhydroxyalkanoates (PHA) polyethylene terephthalate (PET), and mixtures thereof.

Alternatively, the polymer resin is an elastomer resin. Preferably, the polymer resin is an elastomer resin selected from natural or synthetic rubber, more preferably from the group consisting of acrylic rubber, butadiene rubber, acrylonitrile-butadiene rubber, epichlorhydrin rubber, isoprene rubber, ethylene-propylene rubber, ethylene-propylene-diene monomer rubber, nitrile-butadiene rubber, butyl rubber, styrene-butadiene rubber, polyisoprene, hydrogenated nitrile-butadiene rubber, carboxylated nitrile-butadiene rubber, chloroprene rubber, isoprene isobutylene rubber, chloro-isobutene-isoprene rubber, brominated isobutene-isoprene rubber, silicone rubber, fluorocarbon rubber, polyurethane rubber, polysulfide rubber, thermoplastic rubber, thermoplastic starch (TPS), and mixtures thereof.

Such polymer resins are well known and do not need to be described in more detail herein.

In order to increase the content of bio-based carbon, it is preferred that the polymer resin is a bio-based polymer resin, such as a partially or fully bio-based polymer resin in which the monomers are derived from renewable biomass sources. It is appreciated that a biobased polymer is a polymer having a biobased carbon content of more than 20 wt.-%, based on the total weight of the polymer resin. Preferably, the biobased polymer is a polymer having a biobased carbon content of more than 40 wt.-%, more preferably more than 50 wt.-%, and most preferably more than 80 wt.-%, based on the total weight of the polymer resin.

For example, the polymer resin is a bio-based polyolefin, thermoplastic starch or polyester resin. Thus, the polymer resin is preferably a biobased polyester resin that is selected from the group comprising, e.g. consisting of, polylactic acid, polylactic acid-based polymer, polyhydroxyalkanoates (PHA), polyethylene terephthalate (PET), polybutylene succinate (PBS), polycaprolactone (PCL), polybutyrate-adipate-terephthalate (PBAT) and mixtures thereof, a biobased thermoplastic starch (TPS) or a biobased polyethylene (PE), polypropylene (PP) and mixtures thereof. More preferably, the polymer resin is a bio-based polyester resin or a mixture of biobased polyester resins.

In one embodiment, the bio-based polyester resin is selected from the group comprising, e.g. consisting of, polylactic acid, polylactic acid-based polymer and mixtures thereof. Preferably, the biobased polyester resin of the present invention is polylactic acid.

Polylactic acid may be prepared in a well-known manner and is commercially available from different manufacturers such as Cereplast Inc, Mitsui Chemicals Inc, Gehr GmbH or NatureWorks and many more.

There is no specific limitation on the molecular weight of the bio-based polymer resin used in this invention. However, the number average molecular weight Mn measured by gel permeation chromatography from 5 000 to 200 000 g/mol, preferably from 10 000 to 100 000 g/mol, and more preferably from 15000 to 80000 g/mol. If the number average molecular weight is smaller than the aforementioned range, the mechanical strength (tensile strength, impact strength) of the polymer formulation is too low. On the other hand, if the number average molecular weight is larger than the aforementioned range, the melt viscosity may be too high for carrying out the processing.

Examples of polylactic acid-based resins suitable for the instant polymer formulation include copolymers of lactic acid and blends of polylactic acids.

If the polylactic acid-based resin is a copolymer, the polylactic acid-based resin may comprise further copolymer components in addition to lactic acid. Examples of the further copolymer component include hydroxy butyric acid, 3-hydroxybutyric acid, hydroxyvaleric acid, 3-hydroxyvaleric acid and citric acid.

The polymer formulation may further comprise additives, such as colouring pigments, fibers, e.g. cellulose, glass or wood fibers, dyes, waxes, lubricants, oxidative- and/or UV-stabilizers, antioxidants and other fillers, such as carbon black, TiC>2, mica, clay, precipitated silica, talc or calcined kaolin.

According to one embodiment, the polymer formulation can comprise a filler differing from the calcium carbonate-comprising material of the present invention, preferably the other filler is selected from the group comprising carbon black, silica, ground natural calcium carbonate, calcium carbonate- comprising material, nanofillers, graphite, clay, talc, diatomaceous earth, barium sulfate, titanium dioxide, wollastonite, and mixtures thereof. Preferably, the polymer formulation comprises another filler, such as carbon black, TiC>2, mica, clay, precipitated silica, talc or calcined kaolin.

If the polymer formulation comprises a filler differing from the calcium carbonate-comprising material of the present invention, it is appreciated that the calcium carbonate-comprising material of the present invention is the main filler. That is to say, the amount of the calcium carbonate-comprising material exceeds the amount of the filler differing from the calcium carbonate-comprising material. It is appreciated that the present invention further relates to an article formed from the polymer formulation as defined herein.

With regard to the definition of the polymer formulation and preferred embodiments thereof, reference is made to the statements provided above when discussing the technical details of the polymer formulation of the present invention.

The article is preferably selected from the group comprising hygiene products, medical and healthcare products, filter products, geotextile products, agriculture and horticulture products, clothing, footwear and baggage products, household and industrial products, packaging products, construction products, automotive parts, bottles, cups, bags, straws, flooring products, and the like.

The article may be prepared by any method known to the skilled person. A suitable process for preparing the article comprises the steps of: a) providing a polymer resin, b) providing a calcium carbonate-comprising material as defined herein as filler, c) optionally providing further additives such as colouring pigments, fibers, e.g. cellulose, glass or wood fibers, dyes, waxes, lubricants, oxidative- and/or UV-stabilizers, antioxidants and other fillers, such as carbon black, TiC>2, mica, clay, precipitated silica, talc or calcined kaolin, d) contacting the components of step a), step b), and optionally step c) in any order to form a polymer formulation, and e) forming the polymer formulation of step d) such that an article is obtained.

In one embodiment, the article further comprises additive(s). The process thus comprises the steps of a) providing a polymer resin, b) providing a calcium carbonate-comprising material as defined herein as filler, c) providing further additives such as colouring pigments, fibers, e.g. cellulose, glass or wood fibers, dyes, waxes, lubricants, oxidative- and/or UV-stabilizers, antioxidants and other fillers, such as carbon black, TiC>2, mica, clay, precipitated silica, talc or calcined kaolin, d) contacting the components of step a), step b), and step c) in any order to form a polymer formulation, and e) forming the polymer formulation of step d) such that an article is obtained.

According to step d) of the inventive process, the components of step a) and step b) are contacted in any order. Preferably, the contacting is carried out by mixing the components to form a polymer formulation. During contacting step d), optionally one or more additives and other fillers may be added to the polymer formulation.

Preferably, in contacting step d) the calcium carbonate-comprising material of step b) is contacted under mixing, in one or more steps, with the polymer resin of step a) first, and if present with the additives and other fillers in a following step.

Thus, if present, the further additives of step c) are contacted under mixing, in one or more steps, with the calcium carbonate-comprising material before or after, preferably after, the calcium carbonate-comprising material is contacted under mixing, in one or more steps, with the polymer resin of step a).

It is appreciated that the further additives of optional step c) can be contacted in one or more steps with the components of step a) and step b). For example, the further additives of optional step c) can be contacted in several steps with the components of step a) and step b).

Contacting step d) may be performed by any means known to the skilled person, including, but not limited to, blending, extruding, kneading, and high-speed mixing.

Preferably, contacting step d) is performed in an internal mixer and/or external mixer, wherein the external mixer preferably is a cylinder mixer. It is appreciated that step d) is preferably carried out at a temperature of at least 2°C, preferably at least 5°C and most preferably at least 10°C above the melting point of the polyester resin. For example, step d) is carried out at a temperature of 2°C to 30°C, preferably of 5°C to 25°C, and most preferably 10°C to 20°C, above the melting point of the polyester resin.

The mixture obtained in step d) is formed to article in step e). The forming may be performed by any method known to the skilled person resulting in a polymeric article. These methods include, without being limited to, extrusion processes, co-extrusion process, extrusion coating processes, lamination processes, injection molding processes, compression molding processe, melt-blown processes, spunbonding-processes, staple fiber production processes, blow molding processes and thermoforming processes.

Preferably, contacting step d) is carried out during forming step e).

It is appreciated that the process may comprise further steps such as processing the article in any desired shape. Such steps of processing are well known to the skilled person and can be e.g. carried out by shaping the article for example by stretching of a film.

In another aspect, the present invention relates to the use of the calcium carbonate- comprising material as defined herein in a polymer formulation comprising a polymer resin, preferably the polymer resin is selected from the group comprising polyester, polyolefin, polyamide and mixtures thereof, more preferably polyethylene, polypropylene, polylactic acid, polylactic acid-based polymer, polyhydroxyalkanoates (PHA), e.g. polyhydroxybutyrate (PHB), poly-3- hydroxy butyrate (P3HB), poly3-hydroxybutyrate-co-3-hydroxyhexanoate (PHBH), polyhydroxyvalerate, polyhydroxybutyratepolyhydroxyvalerate copolymer, poly(3- hydroxybutyrate-co-3-hydroxyvalerate) (PHBV); polybutyrate- adipate-terephthalate (PBAT), polyglyconate, polyethylene terephthalate (PET), polycarbonate (PC), poly(dioxanone), polybutylene succinate (PBS), polycaprolactone (PCL), polycaprolactone- poly(ethylene glycol) copolymer, polycaprolactone-polylactic acid copolymer, polyvinylalcohol (PVA), polyethylene succinate) (PES), polypropylene succinate) (PPS), and mixtures thereof, most preferably polylactic acid, polylactic acid-based polymer, poly(3- hydroxy butyrate-co-3- hydroxyvalerate) (PHBV), polyhydroxyalkanoates (PHA) polyethylene terephthalate (PET), and mixtures thereof or the polymer resin is an elastomer resin, preferably an elastomer resin selected from natural or synthetic rubber, more preferably from the group consisting of acrylic rubber, butadiene rubber, acrylonitrile-butadiene rubber, epichlorhydrin rubber, isoprene rubber, ethylene-propylene rubber, ethylene-propylene-diene monomer rubber, nitrile-butadiene rubber, butyl rubber, styrenebutadiene rubber, polyisoprene, hydrogenated nitrile-butadiene rubber, carboxylated nitrile-butadiene rubber, chloroprene rubber, isoprene isobutylene rubber, chloro-isobutene-isoprene rubber, brominated isobutene-isoprene rubber, silicone rubber, fluorocarbon rubber, polyurethane rubber, polysulfide rubber, thermoplastic rubber, thermoplastic starch (TPS), and mixtures thereof.

With regard to the definition of the calcium carbonate-comprising material, polymer formulation and preferred embodiments thereof, reference is made to the statements provided above when discussing the technical details of the calcium carbonate-comprising material and polymer formulation of the present invention.

The scope and interest of the invention will be better understood based on the following examples which are intended to illustrate certain embodiments of the present invention and are non- limitative.

Examples

I. Analytical methods

BET specific surface area of a material

Throughout the present document, the specific surface area (in m ² /g) of the mineral filler was determined using the BET method (using nitrogen as adsorbing gas), which is well known to the skilled man (ISO 9277:2010). The total surface area (in m ² ) of the mineral filler was then obtained by multiplication of the specific surface area and the mass (in g) of the mineral filler prior to treatment.

Particle size distribution (mass % particles with a diameter < X) and weight median diameter (cfco) of a particulate material

As used herein and as generally defined in the art, the “cfeo” value was determined based on measurements made by using a Sedigraph™ 5120 of Micromeritics Instrument Corporation and is defined as the size at which 50 % (the median point) of the particle mass is accounted for by particles having a diameter equal to the specified value.

The method and the instrument are known to the skilled person and are commonly used to determine grain size of fillers and pigments. The measurement was carried out in an aqueous solution of 0.1 wt.-% N34P2O7. The samples are dispersed using a high speed stirrer and supersonics.

Moisture pick up susceptibility

The moisture pick up susceptibility of a material as referred to herein was determined in mg moisture/g after exposure to an atmosphere of 10 and 85 % relative humidity, respectively, for 2.5 hours at a temperature of +23°C (± 2°C). The measurements were made in a GraviTest 6300 device from Gintronic. For this purpose, the sample was first kept at an atmosphere of 10 % relative humidity for 2.5 hours, then the atmosphere was changed to 85 % relative humidity at which the sample is kept for another 2.5 hours. The weight increase between 10 and 85 % relative humidity was then used to calculate the moisture pick-up in mg moisture/g of sample.

Amount of surface-treatment layer

The amount of the at least one hydrophobizing agent on the calcium carbonate-containing material was calculated theoretically from the values of the BET of the untreated calcium carbonate- containing filler material and the amount of at least one hydrophobizing agent that were used for the surface-treatment.

The amount of the at least one hydrophobizing agent in the surface-treated calcium carbonate-containing material was determined by thermogravimetric analysis (TGA). TGA was performed using a Mettler Toledo TGA/DSC3+ based on a sample of 250 ± 50 mg in a 900 pL crucible and scanning temperatures from 25 to 400 °C at a rate of 20°C/minute under an air flow of 80 ml/min. The total volatiles associated with calcium carbonate-containing material and evolved over a temperature range of 25 to 280 °C or 25 to 400 °C was characterized according to % mass loss of the sample over a temperature range as read on a thermogravimetric (TGA) curve. The total weight of the at least one hydrophobizing agent on the accessible surface area of the calcium carbonate-containing material was determined by thermogravimetric analysis by mass loss between 105 °C to 400 °C, whereby the obtained value of mass loss between 105°C to 400°C was substracted with the mass loss (105 to 400°C) of the not-surface-treated calcium carbonate-containing material for correction.

Total residual moisture content

The residual total moisture content was determined by thermogravimetric analysis (TGA). The equipment used to measure the TGA was the Mettler-Toledo TGA/DSC1 (TGA 1 STARe System) and the crucibles used were aluminium oxide 900 pl. The method consists of several heating steps under air (80 mL/min). The first step was a heating from 25 to 105°C at a heating rate of 20°C/minute (step 1), then the temperature was maintained for 10 minutes at 105 °C (step 2), then heating was continued at a heating rate of 20°C/minute from 105 to 400 °C (step 3). The temperature was then maintained at 400 °C for 10 minutes (step 4), and finally, heating was continued at a heating rate of 20°C/minute from 400 to 600 °C (step 5). The residual total moisture content is the cumulated weight loss after steps 1 and 2. Alternatively, the residual total moisture content was determined by Karl-Fischer coulometry. The equipment used to measure the total residual moisture content by Karl-Fischer coulometry was a Karl-Fischer Coulometer (C 30 oven: Mettler Toledo Stromboli, Mettler Toledo, Switzerland) at 220 °C under nitrogen (flow 80 ml/min, heating time 10 min). The accuracy of the result is checked with a HYDRANAL-Water Standard KF-Oven (Sigma-Adrich, Germany), measured at 220 °C).

X-ray diffraction (XRD)

XRD experiments are performed on the samples using rotatable PMMA holder rings. Samples are analysed with a Bruker D8 Advance powder diffractometer obeying Bragg’s law. This diffractometer consists of a 2.2 kW X-ray tube, a sample holder, a 3-3-goniometer, and a VANTEC-1 detector. Nickel-filtered Cu Ka radiation is employed in all experiments. The profiles are chart recorded automatically using a scan speed of 0.7° per min in 23. The resulting powder diffraction pattern can easily be classified by mineral content using the DIFFRACsuite software packages EVA and SEARCH, based on reference patterns of the ICDD PDF 2 database. Quantitative analysis of diffraction data refers to the determination of amounts of different phases in a multi-phase sample and has been performed using the DIFFRACsuite software package TOPAS. In detail, quantitative analysis allows to determine structural characteristics and phase proportions with quantifiable numerical precision from the experimental data itself. This involves modelling the full diffraction pattern (Rietveld approach) such that the calculated pattern(s) duplicates the experimental one. The Rietveld method requires knowledge of the approximate crystal structure of all phases of interest in the pattern. However, the use of the whole pattern rather than a few select lines produces accuracy and precision much better than any single-peak-intensity based method.

Pigment whiteness R457 and brightness Ry

Pigment whiteness R457 and brightness Ry were measured on a tablet (prepared on an Omyapress 2000, pressure = 4 bar, 15 s) using a Datacolor ELREPHO (Datacolor AG, Switzerland) according to ISO 2469:1994 (DIN 53145-1 :2000 and DIN 53146:2000).

CIELAB coordinates

The CIELAB L*, a*, b* coordinates were measured using a Datacolor ELREPHO (Datacolor AG, Switzerland) according to EN ISO 11664-4 and barium sulphate as standard.

Yellow Index

The CIE coordinates were measured using a Datacolor ELREPHO (Datacolor AG, Switzerland). The yellow index (= Yl) is calculated by the following formula:

Yl —100*(Rx-Rz)/Ry).

Melt Flow Rate

The melt flow index was measured according to ISO 1133-1 :2011 on a CEAST Instrument equipped with the software Ceast View 6.15 4C. The length of the die was 8 mm and its diameter was 2.095 mm. Measurements were performed at 210 °C with 300 s of preheating without load, then a nominal load of 2.16 kg is used and the melt flow was measured along 20 mm. Tensile properties

The tensile properties were measured according to ISO 527-1 :2012 Type BA(1 :2) on a Allround Z020 traction device from Zwick Roell. Measurements were performed with an initial load of 0.1 MPa. For the measurement of the E-modulus a speed of 1 mm/min is used, then it was increased to 100 mm/min. The tensile strain at break was obtained under standard conditions. All measurements were performed on samples that have been stored under similar conditions after preparation.

Impact properties

The impact properties were measured according to ISO 179-1 eA:2010-11 on a HIT5.5P device from Zwick Roell. Measurements were performed on notched samples with a hammer of 0.5 J. All measurements were performed on samples that have been stored under similar conditions after preparation.

II. Materials a. Treatment agents

Surface-treatment agent 1

Surface treatment agent 1 was a mono-substituted alkenyl succinic anhydride (2,5- Furandione, dihydro-, mono-Cis-20-alkenyl derivs., CAS No. 68784-12-3), which was a blend of mainly branched octadecenyl succinic anhydrides (CAS #28777-98-2) and mainly branched hexadecenyl succinic anhydrides (CAS #32072-96-1). More than 80% of the blend was branched octadecenyl succinic anhydrides. The purity of the blend was > 95 wt%. The residual olefin content was below 3 wt%.

Surface-treatment agent 2

Surface treatment agent 2 was a 1 :1 mixture of stearic acid and palmitic acid. b. Mineral powders

Comparative examples:

Calcium carbonate CC1

The calcium carbonate CC1 was a wet ground and spray dried calcium carbonate from Italy (dso = 1 .9 |j.m, dgs = 5.8 |j.m, BET = 3.5 m ² /g).

Treated calcium carbonate CC2

The treated calcium carbonate CC2 was a wet ground and spray dried calcium carbonate from Italy, treated with surface treatment agent 2 (dso = 1 .9 |j.m, dgs = 5.8 |j.m, BET = 3.5 m ² /g).

Treated calcium carbonate CC3

The treated calcium carbonate CC3 was a wet ground and spray dried calcium carbonate from Italy treated with surface treatment agent 1 (dso = 1 .9 |j.m, dgs = 5.8 |j.m, BET = 3.5 m ² /g). Calcium carbonate-comprising material - “Pre-ground” material

Calcium carbonate CC4

The calcium carbonate CC4 has been prepared from brown eggshells. After mechanical separation of the inner membrane, the calcium carbonate sample (containing ca 14% humidity and traces of residual membrane) was first ground in a sand mill with diluted NaOH (no dispersant, 42% solids) to reach a dso of 4 microns. The material was then dewatered and bleached with diluted NaOCI. The mixture was dewatered and washed several times with fresh water.

Calcium carbonate-comprising material - with dispersant

Calcium carbonate-comprising material CC5

The calcium carbonate-comprising material CC5 has been prepared by wet grinding of CC4 at high solids content of 70 % solids with dispersant, and subsequent filtration and drying (dso = 1 .5 |j.m, dgs = 6.8 |j.m (Sedigraph 5120), BET = 9.1 m ² /g).

Calcium carbonate-comprising material CC6

The calcium carbonate-comprising material CC6 has been prepared by wet grinding of CC4 at high solids content of 42.5 % solids with dispersant, and subsequent filtration and drying (dso = 0.7 |j.m, dgs = 4.1 |j.m (Sedigraph 5120), BET = 16.0 m ² /g).

Treated calcium carbonate-comprising material CC7

The calcium carbonate-comprising material CC7 has been prepared by surface treatment of powder CC5 with surface treatment agent 1 . For this, 700 g of powder CC5 were placed in a 15 L mixer vessel (Somakon MP-LB Mixer, Somakon Verfahrenstechnik, Germany), and conditioned by stirring for 5 minutes (600 rpm, 120 °C). After that time, 1 .5 parts by weight relative to 100 parts by weight CaCOs of surface treatment agent 1 (10.5 g) were added dropwise to the mixture. Stirring and heating were then continued for another 10 minutes (120 °C, 600 rpm). After that time, the mixture was allowed to cool and the free-flowing hydrophobic powder was collected (powder CC7).

Treated calcium carbonate-comprising material CC8

The treated calcium carbonate-comprising material CC8 has been prepared by surface treatment of powder CC6 with surface treatment agent 1 . For this, 700 g of powder CC6 were placed in a 15 L mixer vessel (Somakon MP-LB Mixer, Somakon Verfahrenstechnik, Germany), and conditioned by stirring for 5 minutes (600 rpm, 120 °C). After that time, 3.0 parts by weight relative to 100 parts by weight CaCOs of surface treatment agent 1 (21 g) were added dropwise to the mixture. Stirring and heating were then continued for another 10 minutes (120 °C, 600 rpm). After that time, the mixture was allowed to cool and the free-flowing hydrophobic powder was collected (powder CC8). Calcium carbonate-comprising material - dispersant free

Calcium carbonate-comprisinq material CC9

The calcium carbonate-comprising material CC9 has been prepared by wet grinding of CC4 at low solids without additives, and subsequent filtration and drying as follows The CC9 material was made through a low solids grinding process, which was performed in a proprietary design 3 liter sandmill, equipped with an 2-level agitator that rotates at 970 rpm. In a batch process, 275 g of eggshell (dry CC4) were mixed with 584 g of water in the mill, giving a slurry with 32% solids content. A quantity of 4575 g of grinding media were added. The grinding media size was 1 .5 mm. The eggshell slurry was then milled for 2 min and 12 seconds. The slurry was separated from the grinding media and then was dried, (dso = 1 .5 |j.m, dgs = 7.8 |j.m (Sedigraph 5120), BET = 6.6 m ² /g).

Calcium carbonate-comprisinq material CC10

The calcium carbonate-comprising material CC10 has been prepared by wet grinding of CC4 at low solids without dispersant, and subsequent filtration and drying as follows: The CC10 material was ground at pilot scale with two proprietary design sandmills arranged in series. The first sandmill used a rotational speed of 250 rpm and the second sandmill used 260 rpm. The grinding media size was 1 .5 mm in both mills. In a continuous process, 775 kg/h of (dry) CC115 material was fed to the first sandmill. A quantity of 1650 l/h was also fed to this first sandmill, to give a slurry with 32% solids content. The resulting material from the first sandmill was fed to the second sandmill. A quantity of water of 350 l/h was also fed to the second sandmill, giving a slurry with 28% solids content. The product from the second sandmill was then passed through a 45 micron screen and was then dried, (dso = 0.8 |j.m, dgs = 5.1 |j.m (Sedigraph 5120), BET = 9.7 m ² /g).

Treated calcium carbonate-comprisinq material CC11

The treated calcium carbonate-comprising material CC11 has been prepared by surface treatment of powder CC9 with surface treatment agent 1 . For this, 500 g of powder CC9 were placed in a 2.5 L mixer vessel (Somakon MP-LB Mixer, Somakon Verfahrenstechnik, Germany), and conditioned by stirring for 5 minutes (600 rpm, 120 °C). After that time, 1 .3 parts by weight relative to 100 parts by weight CaCOs of surface treatment agent 1 (6.5 g) were added dropwise to the mixture. Stirring and heating were then continued for another 10 minutes (120 °C, 600 rpm). After that time, the mixture was allowed to cool and the free-flowing hydrophobic powder was collected (powder CC11).

Treated calcium carbonate-comprisinq material CC12

The treated calcium carbonate-comprising material CC12 has been prepared by surface treatment of powder CC10 with surface treatment agent 1 . For this, 500 g of powder CC10 were placed in a 2.5 L mixer vessel (Somakon MP-LB Mixer, Somakon Verfahrenstechnik, Germany), and conditioned by stirring for 5 minutes (600 rpm, 120 °C). After that time, 1 .8 parts by weight relative to 100 parts by weight CaCOs of surface treatment agent 1 (9 g) were added dropwise to the mixture. Stirring and heating were then continued for another 10 minutes (120 °C, 600 rpm). After that time, the mixture was allowed to cool and the free-flowing hydrophobic powder was collected (powder CC12). Calcium carbonate-comprisinq material CC13

The calcium carbonate-comprising material CC13 has been prepared by dry grinding 2.5-5.0 mm seashell material on a ZPS classifier mill (Hosokawa Alpine Multiprocess unit). A dark grey powder was obtained (CaCOs: 95%, acid insoluble residue: 4%, dso = 2.3 pm, dgs = 7.4 pm (Malvern 3000 wet), BET = 5.8 m ² /g).

Treated calcium carbonate-comprisinq material CC14

The treated calcium carbonate-comprising material CC14 has been prepared by surface treatment of powder CC13 with surface treatment agent 1 . For this, 300 g of powder CC13 were placed in a 2.5 L mixer vessel (Somakon MP-LB Mixer, Somakon Verfahrenstechnik, Germany), and conditioned by stirring for 5 minutes (600 rpm, 120 °C). After that time, 1.15 parts by weight relative to 100 parts by weight CaCOs of surface treatment agent 1 were added dropwise to the mixture. Stirring and heating were then continued for another 10 minutes (120 °C, 600 rpm). After that time, the mixture was allowed to cool and the free-flowing hydrophobic powder was collected (powder CC14).

Calcium carbonate-comprisinq material CC15

The calcium carbonate-comprising material CC15 has been prepared by low solids wet grinding oystershell material on a Dynomill ECM-AP05 (WAB) without dispersants. A dark grey powder was obtained (CaCOs (calcite): 97%, acid insoluble residue: 3%, dso = 1.5 pm, dgs = 7.0 pm (Malvern 3000 wet), BET = 9.4 m ² /g).

Treated calcium carbonate-comprisinq material CC16

The treated calcium carbonate-comprising material CC16 has been prepared by surface treatment of powder CC15 with surface treatment agent 1 . For this, 350 g of powder CC15 were placed in a 1.2 L mixer vessel (Somakon MP-LB Mixer, Somakon Verfahrenstechnik, Germany), and conditioned by stirring for 5 minutes (800 rpm, 120 °C). After that time, 2.1 parts by weight relative to 100 parts by weight CaCOs of surface treatment agent 1 were added dropwise to the mixture. Stirring and heating were then continued for another 15 minutes (120 °C, 800 rpm). After that time, the mixture was allowed to cool and the free-flowing hydrophobic powder was collected (powder CC16). c. Powder properties

The content of bio-based carbon of the calcium carbonate-comprising materials as determined according to DIN EN 16640:2017 in wt.-%, based on the total weight of carbon in the calcium carbonate-comprising material, is set out in the following table 1 . Table 1

“% modern carbon” (pMC) is the percentage of C14 measured in the sample relative to a modern reference standard (NIST 4990C). The % Biobased Carbon content is calculated from pMC by applying a small adjustment factor for C14 in carbon dioxide in air today. It is important to note that all internationally recognized standards using C14 assume that the plant or biomass feedstocks were obtained from natural environments. In case of a treated material, the bio-based carbon content is determined on the treated material, i.e. after surface-treatment.

The BET specific surface area measured using nitrogen and the BET method according to ISO 9277 as well as the residual total moisture content and moisture pick-up susceptibility of the calcium carbonate-comprising materials determined by Karl Fischer coulometry, based on the total dry weight of the calcium carbonate-comprising material, are set out in the following table 2.

Table 2

The powders optical characteristics such as brightness Ry, yellow index Yl and L*/a*/b* of the calcium carbonate-comprising materials are set out in the following table 3. Table 3

The TGA results of the calcium carbonate-comprising materials are set out in the following table 4. Table 4 c. Application examples

1. High solids ground eggshells in PLA

Compounding and injection Compounding in PLA (Ingeo 2003D from Natureworks) was performed on a lab twin screw extruder. PLA was first crushed to <1 mm particles with a Retsch SR300 rotor beater mill, and dried 2 h at 80 °C prior to compounding.

Extrusion conditions'. Twin-screw extruder 25:1 from Three Tec (Extruder Type ZE12, die: 0.5 mm)

T1 = 170°C

T2 = 190°C

T3 = 190°C

T4 = 180°C

The samples compounded are summarized in the following table 5.

Table 5 pbw: throughout the present invention, “pbw” refers to “parts by weight”.

For mechanical properties testing, sample pieces were produced by injection molding using a Xplore IM12 injection moulder from Xplore Instruments B.V with the settings indicated in the following Table 6:

Table 6

The ash content of the PLA samples in [%] of the compounds was determined by incineration of a sample in an incineration crucible which is put into an incineration furnace at 580°C for 2 hours.

The ash content was measured as the total amount of remaining inorganic residues. The results are set out in the following Table 7:

Table 7

The melt flow index of the PLA samples was measured and the results are set out in the following Table 8. Table 8

*: not measurable - value too high

The tensile properties were measured and the results are presented in the following table 9.

Table 9

The impact properties (Charpy, V-notched) were measured and the results are presented in the following table 10.

Table 10

The color of the PLA samples was measured on polymer plates (40x40x5 mm) with a Spectro- guide 45/0 gloss device from BYK-Gardner GmbH. Results (average over 3 measurements) are presented in the following table 11 . Table 11

2. Low solids ground eggshells in PLA

Compounding and injection

Compounding in PLA (Ingeo 2003D from Natureworks) was performed on a lab twin screw extruder. PLA was first crushed to <1 mm particles with a Retsch SR300 rotor beater mill, and dried 2 h at 80 °C prior to compounding.

Extrusion conditions'.

Twin-screw extruder 25:1 from Three Tec (Extruder Type ZE12, die: 0.5 mm)

T1 = 170°C

T2 = 190°C

T3 = 190°C

T4 = 180°C

The samples compounded are summarized in the following table 12.

Table 12

For mechanical properties testing, sample specimens were produced by injection molding using a Xplore I M 12 injection moulder from Xplore Instruments B.V with the settings indicated in the following table 13: Table 13

The ash content in [%] of the compounds was determined by incineration of a sample in an incineration crucible which is put into an incineration furnace at 580°C for 2 hours. The ash content was measured as the total amount of remaining inorganic residues. The results are set out in the following table 14

Table 14 The melt flow index of the PLA samples was measured and the results are set out in the following table 15.

Table 15 The tensile properties were measured and the results are presented in the following table 16.

Table 16

The impact properties (Charpy, V-notched) were measured and the results are presented in the following table 17.

Table 17

The color was measured on polymer plates (40x40x5 mm) with a Spectro-guide 45/0 gloss device from BYK-Gardner GmbH. Results (average over 3 measurements) are presented in the following table 18.

Table 18

3. Examples with seashells

Compounding and injection

Compounding in PLA (Ingeo 2003D from Natureworks) was performed on a lab twin screw extruder. PLA was first crushed to <1 mm particles with a Retsch SR300 rotor beater mill, and dried 2 h at 80 °C prior to compounding.

Extrusion conditions'.

Twin-screw extruder 25:1 from Three Tec (Extruder Type ZE12, die: 0.5 mm)

T1 = 170°C

T2 = 190°C

T3 = 190°C

T4 = 180°C The samples compounded are summarized in the following table 19.

Table 19

For mechanical properties testing, sample specimens were produced by injection molding using a Xplore IM12 injection moulder from Xplore Instruments B.V with the settings indicated in the following table 20:

Table 20

The ash content in [%] of the compounds was determined by incineration of a sample in an incineration crucible which was put into an incineration furnace at 580°C for 2 hours. The ash content was measured as the total amount of remaining inorganic residues. The results are set out in the following table 21 .

Table 21

The melt flow index of the PLA samples was measured and the results are set out in the following table 22.

Table 22

The tensile properties were measured and the results are presented in the following table 23.

Table 23

The impact properties (Charpy, V-notched) were measured and the results are presented in the following table 24.

Table 24

4. Lab trials in PHBV

Compounding in poly(3-hydroxybutyrate-co-3-hydroxyvalerate) (PHBV; Enmat Y1000P from PHAradox) was performed on a lab twin screw extruder.

Extrusion conditions'.

Twin-screw extruder 25:1 from Three Tec (Extruder Type ZE12, die: 0.5 mm)

T1 = 165°C

T2 = 170°C

T3 = 173°C

T4 = 175°C

The samples compounded are summarized in the following table 25. Table 25

For mechanical properties testing, sample specimens were produced by injection molding using a Xplore IM12 injection moulder from Xplore Instruments B.V with the settings indicated in the following table 26:

Table 26

The ash content in [%] of the compounds was determined by incineration of a sample in an incineration crucible which was put into an incineration furnace at 580°C for 2 hours. The ash content was measured as the total amount of remaining inorganic residues. The results are set out in the following table 27. Table 27

The melt flow index of the PHBV samples was measured and the results are set out in the following table 28.

Table 28

The tensile properties were measured and the results are presented in the following table 29. Table 29

The impact properties (Charpy, V-notched) were measured according to ISO 179-1 eA:2010-

11 on a HIT5.5P device from Zwick Roell. Measurements were performed on V-notched samples with a hammer of 2 J. All measurements were performed on samples that have been stored under similar conditions after preparation. The results from impact tests are presented in the following table 30.

Table 30