Metal-organic framework extrudates with high packing density and tunable pore volume Description The present invention relates to extruded shaped bodies containing at least one metal-organic framework (MOF), methods for their preparation and their use.

Due to their large surface areas of up to 10 000 m ² /g, MOF materials are of interest for applications in gas storage or gas separation. For most applications, it is necessary to process the pul- verulent materials to compact shaped bodies. These can be handled more conveniently and especially in a safer manner, allow better exploitation of the apparatus or tank volumes and prevent large pressure drops. Prerequisites for the successful use of such shaped bodies are, however, the absorption capacity and selectivity thereof, adequate thermal and mechanical stability and high abrasion resistance. Even the recurrent thermal shocks resulting from the heat of adsorption released in the course of continuous adsorption/desorption cycles can be sufficient in the case of the related zeolite shaped bodies to cause fracture and splintering of the bodies (DE 1 905 019). Mechanical stability is therefore indispensible particularly for MOF shaped bodies which are used in vehicle tanks exposed constantly to agitation. It is therefore an object of the present invention to provide MOFs in forms allowing a broad use of these applications.

The general preparation of MOF pellets and extrudates is described in WO 2003/102000 and WO 2006/050898.

Kneading and/or pan milling and shaping can be carried out by any suitable method, for example as described in Ullmanns Enzyklopadie der Technischen Chemie, 4th edition, Volume 2, p. 313 ff. (1972). Binders for the shaping of zeolites are described, for example, in WO 94/29408, EP 0 592 050, WO 94/13584, JP 03-037156 and EP 0 102 544.

MOF-containing extrudates have been reported in Chem. Eng. J. 167 (201 1 ) 1 -12. The MOF mentioned therein is based on copper and the organic compound trimesate. It is available under the commercial name Basolite C300. A report within the project DE-FC26-07NT43092 of the US Department of Energy mentions a MOF based on nickel and the organic compound 2,5- dihydroxyterephthalic acid. However, no details have been given how these extrudates could be yielded. It was another aim to provide mechanically stable extrudates of metal-organic frameworks with high surface area, tunable pore volume and high packing density.

It was a further aim to apply the shaped bodies of the invention in gas storage/gas separation. Water steam is almost omnipresent as an impurity in gases. It is known to destabilize the structure of MOFs, especially at higher temperatures. This would lead to a reduced inner surface and gas storage capacity. Therefore, it was a further aim of the present invention to provide extru- dates of metal-organic frameworks with a high stability towards water, in particular to water steam.

The object is solved by providing a method for preparing a shaped body containing a metal- organic framework material (MOF) comprising the steps of (a) mixing a composition comprising the MOF and at least one additive; and

(b) extruding the composition into a shaped body. wherein the MOF is dried prior to step (a).

The term "shaped body" as used in the present invention thereby refers to shaped bodies obtained by extrusion processes. The term "shaped body" will be defined further below.

As described above MOFs and their preparation are described in, for example, WO 12/042410. The content of these publications and especially the MOFs disclosed therein, to which reference is made herein, is fully incorporated in the content of the present application.

MOFs are powder-like materials that exhibit high surface areas up to 10 000 m ² /g. This makes them ideal for storing or separating gases. Preferred applications are the storage and/or separa- tion of natural gas or shale gas, even more preferred is the storage of natural gas or shale gas in vehicle tanks. These examples, however, do not by any means limit the applicability of the present invention for different storage and separation purposes. The powders have to be compacted prior to using them in most of these applications. The resulting shaped bodies can be used in a more convenient and safer way, they allow for better use of the volume available in an apparatus or tank and prevent pressure loss.

Important prerequisites for the use of such shaped bodies are their gas uptake capacity and selectivity, appropriate thermal and mechanical stability as well as abrasion resistance. Moreover, they need to exhibit appropriate diffusion properties to allow fast storage of gas molecules in their interior and therefore result e.g. in short tank filling times. These diffusion properties are critically determined by the pore volume of the shaped bodies and the diameter of the pores. Both these properties are directly proportional to the extent of compaction the powder is exposed to. Therefore, the compaction process needs to be carefully adapted to obtain mechanically stable shaped bodies with an appropriate pore volume. According to this invention, in addi- tion to the compaction process, the morphology of the MOF powder and the drying technique applied to the MOF material were found to be critical for the resulting pore volume. The relatively small number of granted patents for MOF shaped bodies underlines that current knowledge in the field is rather basic. There is a lot of room to improve this basic manufacturing technology and adapt the properties of the shaped bodies to the requirements of applications such as the storage and separation of gas. Preferred applications are the storage and/or sepa- ration of natural gas or shale gas, even more preferred is the storage of natural gas or shale gas in vehicle tanks. These examples, however, do not by any means limit the applicability of the present invention for different storage and separation purposes. Moreover, the chemical and physical mechanisms underlying the compaction and binding of metal-organic frameworks are by far not as well understood as those of the related class of zeolites. The properties of shaped bodies resulting from the use of new additives and morphologies can hardly be predicted. An appropriate manufacturing process yields shaped bodies with high surface area, appropriate mechanical strength and adsorption capacity as well as kinetics with respect to the target application. One aspect of the present invention is a method for preparing a shaped body containing a metal-organic framework material (MOF) comprising the steps of

(a) mixing a composition comprising the MOF and at least one additive; and (b) extruding the composition into a shaped body. wherein the MOF is dried prior to step (a).

The shaped bodies obtained according to the invention can be prepared with any type of MOF material described in the state of the art. As the process involves humidity, moisture-stable MOFs are preferred even though water-sensitive MOFs can be subjected to the extrusion process by adapting the conditions or using an organic solvent. The shaped bodies according to the invention can exhibit any extrudate shape that is known to the expert in the field (e.g. rods, trilobes, stars). The surface of these extrudates can range from smooth to coarse. Established cutting techniques can be used to manufacture extrudates with identical lengths or narrow length distribution.

While the step of extrusion is mandatory, the following steps are optional according to the present invention:

(I) the extrusion may be preceded by a step of preparing a paste-like mass or a fluid containing the MOF material and, eventually, the binder, for example by adding solvents or other additional substances,

(II) the molding may be followed by a step of finishing, in particular a step of drying, activating or impregnating.

The mandatory step of extrusion may be achieved by any method known to the expert to achieve agglomeration of a powder, a suspension or a paste-like mass. Such methods are described, for example, in Ullmann's Enzyklopadie der Technischen Chemie, 4 ^th Edition, Vol. 2, p. 313 et seq., 1972, whose respective content is incorporated into the present application by reference.

The process is affected by extrusion in conventional extruders, for example such that result in extrudates having a diameter of, usually, from about 1 to about 10 mm, in particular from about 1 to about 5 mm. Such extrusion apparatuses are described, for example, in Ullmann's En- zyklopadie der Technischen Chemie, 4th Edition, Vol. 2, p. 295 et seq., 1972. In addition to the use of an extruder, an extrusion press is preferably also used for extrusion. The extrusion can be performed at elevated pressure (ranging from atmospheric pressure to several 100 bar), at elevated temperatures (ranging from room temperature to 300 °C) or in a protective atmosphere (noble gases, nitrogen or mixtures thereof). Any combinations of these conditions are possible as well. The step of extrusion is preferred performed in the presence of at least one binder and optional other additional substances that stabilize the materials to be agglomerated. As to the at least one binder, any material known to the expert to promote adhesion between the particles to be molded together can be employed. A binder, an organic viscosity-enhancing compound and/or a liquid for converting the material into a paste can be added to the MOF material, with the mix- ture being subsequently compacted in a mixing or kneading apparatus or an extruder. The resulting plastic material can then be molded, in particular using an extrusion press or an extruder, and the resulting moldings can then be subjected to the optional step (II) of finishing, for example drying, activating or impregnating. A number of compounds can be used as binders. For example, according to US-A 5,430,000, titanium dioxide or hydrated titanium dioxide is used as the binder. Examples of further prior art binders are:

hydrated alumina or other aluminum-containing binders (WO 94/29408);

mixtures of silicon and aluminum compounds (WO 94/13584);

silicon compounds (EP-A 0 592 050);

clay minerals (JP-A 03 037 156);

alkoxysilanes (EP-B 0 102 544);

amphiphilic substances. Other conceivable binders are in principle all compounds used to date for the purpose of achieving adhesion in powdery materials. Compounds, in particular oxygen-containing, of silicon, of aluminum, of boron, of phosphorus, of zirconium and/or of titanium are preferably used. Of particular interest as a binder are alumina, silica, where the S1O2 may be introduced into the shaping step as a silica sol or in the form of tetraalkoxysilanes, and silicones. Oxides of magne- sium and of beryllium and clays, for example montmorillonites, kaolins, bentonites, halloysites, dickites, nacrites and anauxites, may furthermore be used as binders. Specific examples of tetraalkoxysilanes are tetramethoxysilane, tetraethoxysilane, tetrapropoxysilane and tet- rabutoxysilane, the analogous tetraalkoxytitanium and tetraalkoxyzirconium compounds and trimethoxy-, triethoxy-, tripropoxy- and tributoxyaluminum, tetramethoxysilane and tetraethox- ysilane being particularly preferred.

It was surprisingly found that typical binders such as those applied for the extrusion of zeolites (e.g. aluminum oxide, clays such as e.g. kaolin, attapulgite, bentonite, silicium dioxide, compare DE 1 905 019, DE 2 1 17 479, US 1 332 847) interact well with the partially organic MOFs yielding mechanically stable shaped bodies with appropriate strength. The expert in the field would expect a change to an at least partially organic binder to be required, as materials with similar polarities are known to interact best with each other. Compare e.g. the basic observation that hydrophile water and hydrophobic oil do not mix. The hardness of the extrudates obtained according to the invention can reach surprisingly high values at least comparable to those of zeolites (e.g. EP 1 467 81 1 , DE 2 1 17 479), even though partially organic MOFs do not allow for calcination after the shaping stage. Zeolites in comparison require high calcination temperatures (a few hundred °C) to yield extrudates of sufficient hardness (e.g. EP 1 467 81 1 ). MOFs, how- ever, decompose at these high temperatures due to the organic units being burnt. Surprisingly, thermal treatment at considerably reduced temperatures (e.g. 200 °C) yields shaped bodies with appropriate hardness.

Even more surprisingly these conventional binders do not block the highly porous MOF struc- tures that do exhibit up to the 20-fold surface area compared to zeolites. This high surface area is the prerequisite for MOFs' superior performance in applications such as the storage of natural gas. Preserving the surface area as best as possible in the extrusion process is therefore mandatory. Due to the surprisingly high surface areas of the extrudates obtained according to the invention they do show high methane uptake.

In addition, organic viscosity-enhancing substances and/or hydrophilic polymers, e.g. cellulose or polyacrylates may be used. The organic viscosity-enhancing substance used may likewise be any substance suitable for this purpose. Those preferred are in particular hydrophilic polymers, e.g., cellulose, starch, polyacrylates, polymethacrylates, polyvinyl alcohol, polyvinylpyrrolidone, polyisobutene and polytetrahydrofuran. These substances primarily promote the formation of a plastic material during the kneading, molding and drying step by bridging the primary particles and moreover ensuring the mechanical stability of the molding during the molding and the optional drying process. There are no restrictions at all with regard to the optional liquid which may be used to create a paste-like substance, either for the optional step (I) of mixing or for the mandatory step of molding. In addition to water, alcohols may be used, provided that they are water-miscible. Accordingly, both monoalcohols of 1 to 4 carbon atoms and water-miscible polyhydric alcohols may be used. In particular, methanol, ethanol, propanol, n-butanol, isobutanol, tert-butanol and mixtures of two or more thereof are used. However toluene is also suitable.

Amines or amine-like compounds, for example ammonium, tetraalkylammonium compounds or aminoalcohols, and carbonate-containing substances, such as calcium carbonate, may be used as further additives. Such further additives are described in EP-A 0 389 041 , EP-A 0 200 260 and WO 95/19222, which are incorporated fully by reference in the context of the present application. Most, if not all, of the additive substances mentioned above may be removed from the shaped bodies by drying or heating, optionally in a protective atmosphere or under vacuum. In order to keep the MOF material intact, the shaped bodies are preferably not exposed to temperatures exceeding 300 °C. However, studies show that heating and/or drying under the aforementioned mild conditions, in particular drying in vacuo, preferably well below 300 °C is sufficient to at least remove organic compounds and water out of the pores of the MOF material. Generally, the conditions are adapted and chosen depending upon the additive substances used.

In general it is possible either to add first the binder, then, for example, the MOF material and, if required, the additive and finally the mixture containing at least one alcohol and/or water or to interchange the order with respect to any of the aforementioned components.

As far as the step of mixing is concerned, for example, of the material containing a MOF material and preferred a binder and optionally further process materials (= additional materials), all methods known to the expert in the fields of materials processing and unit operations can be used. If the mixing occurs in the liquid phase, stirring is preferred, if the mass to be mixed is paste-like, kneading and/or extruding are preferred and if the components to be mixed are all in a solid, powdery state, mixing is preferred. The use of atomizers, sprayers, diffusers or nebulizers is conceivable as well if the state of the components to be used allows the use thereof. For paste-like and powder-like materials the use of static mixers, planetary mixers, mixers with rotat- ing containers, pan mixers, pug mills, shearing-disk mixers, centrifugal mixers, sand mills, trough kneaders, internal mixers, and continuous kneaders are preferred. It is explicitly included that a process of mixing may be sufficient to achieve the molding, i.e., that the steps of mixing and molding coincide. It was found that extrudates with the best set of mechanical and sorption properties are obtained by using spray dried MOF or MOF that has been mixed with a binder suspension prior to spray-drying, resulting in powder particles that contain a MOF/binder-ratio that is appropriate for extrusion. Moreover the humidity content of the MOF powder can be adjusted via spray-drying over a wide range (e.g. 3 to 60 wt% residual water). Thereby MOF powder can be produced that contains right-away the right amount of binder and water for the extrusion, i.e. it can be directly placed into an extruder without the need to add any other agent. Spray-drying furthermore allows to tune the particle size of the MOF material resulting in spheres with diameters from 2 to 500 μηη, preferred from 10 to 200 μηη. This is a great advantage as the particle size directly translates into pore volume. Higher pore volume can be generated in the extrudates by applying bigger MOF particles.

In a preferred embodiment, the composition of step (a) is dried prior to step (b). It is even more preferred that the drying of the composition of step (a) prior to step (b) comprises spray-drying. The MOF can be applied as in pulverulent form, as powder or in the form of spheres.

In a preferred embodiment, the at least one additive comprises at least one binder that is selected from the group consisting of oxidic binders and partially organic binder, preferred alumi- num oxide, silicon oxide, clay, cement, and silicon-organic compounds.

Suitable binders are described below. Preferably, the at least one binder is an oxygen containing binder. More preferably, the at least one binder is selected from the group consisting of an oxygen-containing aluminum compound, a silicium oxide and a silicium organic compound, like tetraethyl orthosilicate.

Such compounds are typically commercially available under trade names like Pural® SB (aluminum oxide), Ludox® AS 40 (colloidal silica), or Silres® MSE100 (methyl and methoxy groups containing polysiloxane).

The amount of the at least one binder additive based on the total weight of the shaped body can range from 0.1 to 90 wt.%. Preferred the amount is from 1 to 80 wt.-%.

In another preferred embodiment, the metal of the MOF is selected from the group consisting of Mg, Zn, Al or mixtures thereof. Preferred it is Al.

Preferred MOFs according to the inventive method comprise aluminum and one or more of the organic compounds selected from fumarate, trimesate, 2-aminoterephthalic acid and 4, 4', 4"- benzene-1 ,3,5-triyl- tribenzoate.

More preferred MOFs according to the inventive method consist essentially of aluminum and one or more of the organic compounds selected from fumarate, trimesate, 2-aminoterephthalic acid and 4, 4', 4"-benzene-1 ,3,5-triyl- tribenzoate. Even more preferred MOFs according to the inventive method consist of aluminum and one or more of the organic compounds selected from fumarate, trimesate, 2-aminoterephthalic acid and 4, 4', 4"-benzene-1 ,3,5-triyl- tribenzoate.

Most preferred MOFs according to the inventive method are aluminum fumarate, aluminum tri- mesate, aluminum 2-aminoterephthalic acid, aluminum 4,4',4"-benzene-1 ,3,5-triyl-tribenzoate or mixtures thereof.

Another aspect of the present invention is an extruded shaped body comprising a metal-organic framework material (MOF), wherein the metal of the MOF is selected from the group consisting of Mg, Zn, Al or mixtures thereof, preferred Al. In a preferred embodiment, the MOF comprises aluminum and one or more of the organic compounds selected from fumarate, trimesate, 2-aminoterephthalic acid and 4,4',4"-benzene-1 ,3,5- triyl-tribenzoate. Aluminum-MOFs are stable in water. Therefore, they can be directly produced in aqueous solutions. These can, e.g. be spray-dried without prior removal of organic compounds. This renders them particularly advantageous on an industrial scale. Most other synthesis routes of MOFs require the use of organic compounds. Many of them are toxic, irritating, explosive, combustible and/or hazardous for the environment. Their handling renders protection measures unavoida- ble. This includes the e.g. use of non-corrosive material, safety controls, pressure controls and the like. The use of water as exclusive solvent or main component of the solvent would help to minimize these protection measures and the costs related thereto.

In a more preferred embodiment, the MOF consists essentially of aluminum and one or more of the organic compounds selected from fumarate, trimesate, 2-aminoterephthalic acid and 4,4',4"- benzene-1 ,3,5-triyl- tribenzoate.

In an even more preferred embodiment, the MOF consists of aluminum and one or more of the organic compounds selected from fumarate, trimesate, 2-aminoterephthalic acid and 4, 4', 4"- benzene-1 ,3,5-triyl- tribenzoate.

In a most preferred embodiment, the MOF is aluminum fumarate, aluminum trimesate, aluminum 2-aminoterephthalic acid, aluminum 4, 4',4"-benzene-1 ,3,5-triyl- tribenzoate or mixtures thereof.

In a preferred embodiment, the extruded shaped body further comprises at least one additive.

A further aspect of the present invention is the use of the shaped bodies comprising a metal- organic framework for the uptake of at least one substance for the purposes of its storage, sep- aration, controlled release, chemical reaction or as support.

In one embodiment, the shaped bodies are those comprising a metal-organic framework material (MOF), wherein the metal of the MOF is selected from the group consisting of Mg, Zn, Al or mixtures thereof, preferred Al.

In a second embodiment, the shaped bodies are those yielded by the inventive method as de- scribed above.

Preferred, the at least one substance is a gas or gas mixture, preferred natural gas or shale gas. Processes for storage by means of shaped bodies according to the present invention can be used as known for shaped bodies of metal-organic frameworks. In general these are described in WO-A 2005/003622, WO-A 2003/064030, WO-A 2005/049484, WO-A 2006/089908 and DE- A 10 2005 012 087. Preferred gases for storage are methane, methane containing gas mixtures, like natural gas, shale gas or town gas, and hydrogen.

Processes for separation or purification by means of shaped bodies according to the present invention can be used as known for shaped bodies of metal-organic frameworks. In general these are described in EP-A 1 674 555, DE-A 10 2005 000938 and DE-A 10 2005 022 844. A gas which is preferably separated off is carbon dioxide, in particular from a gas mixture which further comprises carbon monoxide. Other gases or volatile components which are preferably separated off are sulfur-based impurities in natural gas or shale gas like hydrogen sulfide or carbonyl sulfide.

If the shaped bodies of the invention are used for storage, this is preferably carried out in a temperature range from -200°C to +80°C. A temperature range from -80°C to +80°C is more preferred. A preferred pressure range is from 1 bar to 300 bar (absolute), in particular from 2 bar to 250 bar.

For the purposes of the present invention, the terms "gas" and "liquid" are used in the interests of simplicity, but gas mixtures and liquid mixtures or liquid solutions are likewise encompassed by the term "gas" or "liquid".

Preferred gases are hydrogen, natural gas, town gas, hydrocarbons, in particular methane, ethane, ethene, acetylene, propane, propene, n-butane and i-butane, 1 -butene, 2-butene, carbon monoxide, carbon dioxide, nitrogen oxides, oxygen, sulfur oxides, halogens, halogenated hydrocarbons, NF3, SFe, ammonia, hydrogen sulfide, ammonia, formaldehyde, noble gases, in particular helium, neon, argon, krypton and xenon.

Particular preference is given to the use of the framework of the invention for the storage of a gas at a minimum pressure of 1 bar (absolute). The minimum pressure is more preferably 3 bar (absolute), in particular 10 bar (absolute). The gas is in this case particularly preferably hydro- gen, methane or a methane containing gas, like natural gas, shale gas or town gas.

Particular preference is given to the use in vehicles. The term 'vehicle' includes -but shall not be limited to- cars, trucks, ships, airplanes, motorcycles and the like. In a particular embodiment, the MOF is used in tanks in the vehicles.

A vehicle can comprise one or more tanks equipped with MOF.

When two or more tanks are used in one vehicle the tanks can be used to store the same gas or gas mixture. They can also be used to store different gases or gas mixtures. For example, one MOF-based tank can be used to store methane and a second MOF-based tank to store hydrogen. The gas is particularly preferably carbon dioxide which is separated off from a gas mixture comprising carbon dioxide. The gas mixture preferably comprises carbon dioxide together with at least hydrogen, methane or carbon monoxide. In particular, the gas mixture comprises carbon monoxide in addition to carbon dioxide. Very particular preference is given to mixtures which comprise at least 10 and not more than 45% by volume of carbon dioxide and at least 30 and not more than 90% by volume of carbon monoxide.

A preferred embodiment is pressure swing adsorption using a plurality of parallel adsorber reactors, with the adsorbent bed being made up completely or partly of the material according to the invention. The adsorption phase for the CO2/CO separation preferably takes place at CO2 partial pressure of from 0.6 to 3 bar and a temperature of at least 20°C, but not more than 70°C. To desorb the adsorbed carbon dioxide, the total pressure in the adsorber reactor concerned is usually reduced to values in the range from 100 mbar to 1 bar. A preferred embodiment of the invention is the use an extruded shaped body comprising a metal-organic framework material (MOF) to store water, preferred water steam.

In a preferred embodiment, the adsorption enthalpy is used for heating the environment. In a further preferred embodiment, the desorption enthalpy is used for cooling the environment.

Thereore, another embodiment of the invention is the use of an extruded shaped body comprising a metal-organic framework material (MOF) for heating and/or cooling devices. Another embodiment are heating and/or cooling devices comprising at least one extruded shaped body comprising a metal-organic framework material (MOF).

However, the at least one substance can also be a liquid. Examples of such a liquid are disinfectants, inorganic or organic solvents, fuels, in particular gasoline or diesel, hydraulic fluid, ra- diator fluid, brake fluid or an oil, in particular machine oil. The liquid can also be halogenated aliphatic or aromatic, cyclic or acyclic hydrocarbons or mixtures thereof. In particular, the liquid can be acetone, acetonitrile, aniline, anisol, benzene, benzonitrile, bromobenzene, butanol, tert- butanol, quinoline, chlorobenzene, chloroform, cyclohexane, diethylene glycol, diethyl ether, dimethylacetamide, dimethylformamide, dimethyl sulfoxide, dioxane, glacial acetic acid, acetic anhydride, ethyl acetate, ethanol, ethylene carbonate, ethylene dichloride, ethylene glycol, ethylene glycol dimethyl ether, formamide, hexane, isopropanol, methanol, methoxypropanol, 3-methyl-1 -butanol, methylene chloride, methyl ethyl ketone, N-methylformamide, N-methylpyrrolidone, nitrobenzene, nitromethane, piperidine, propanol, propylene carbonate, pyridine, carbon disulfide, sulfolane, tetrachloroethene, carbon tetrachloride, tetrahydrofuran, toluene, 1 ,1 ,1 -trichloroethane, trichloroethylene, triethylamine, triethylene glycol, triglyme, water or mixtures thereof.

Furthermore, the at least one substance can be an odorous substance. The odorous substance is preferably a volatile organic or inorganic compound which comprises at least one of the elements nitrogen, phosphorus, oxygen, sulfur, fluorine, chlorine, bromine or iodine or is an unsaturated or aromatic hydrocarbon or a saturated or unsaturated aldehyde or a ketone. More preferred elements are nitrogen, oxygen, phosphorus, sulfur, chlorine, bromine; and particular preference is given to nitrogen, oxygen, phosphorus and sulfur.

In particular, the odorous substance is ammonia, hydrogen sulfide, sulfur oxides, nitrogen oxides, ozone, cyclic or acyclic amines, thiols, thioethers and aldehydes, ketones, esters, ethers, acids or alcohols. Particular preference is given to ammonia, hydrogen sulfide, organic acids (preferably acetic acid, propionic acid, butyric acid, isobutyric acid, valeric acid, isovaleric acid, caproic acid, heptanoic acid, lauric acid, pelargonic acid) and cyclic or acyclic hydrocarbons comprising nitrogen or sulfur and saturated or unsaturated aldehydes such as hexanal, heptanal, octanal, nonanal, decanal, octenal or nonenal and in particular volatile aldehydes such as butyraldehyde, propionaldehyde, acetaldehyde and formaldehyde and also fuels such as gasoline, diesel (constituents).

The odorous substances can also be fragrances which are used, for example, for producing perfumes. Examples of fragrances or oils which can release such fragrances are: essential oils, basil oil, geranium oil, mint oil, cananga oil, cardamom oil, lavender oil, peppermint oil, nutmeg oil, camomile oil, eucalyptus oil, Rosemary oil, lemon oil, lime oil, orange oil, bergamot oil, muscatel sage oil, coriander oil, cypress oil, 1 ,1 -dimethoxy-2-phenylethane, 2,4-dimethyl-4- phenyltetrahydrofuran, dimethyltetrahydrobenzaldehyde, 2,6-dimethyl-7-octen-2-ol, 1 ,2- diethoxy-3,7-dimethyl-2,6-octadiene, phenylacetaldehyde, rose oxide, ethyl 2- methylpentanoate, 1 -(2,6,6-trimethyl-1 ,3-cyclohexadien-1 -yl)-2-buten-1 -one, ethyl vanillin, 2,6- dimethyl-2-octenol, 3,7-dimethyl-2-octenol, tert-butylcyclohexyl acetate, anisyl acetate, allyl cy- clohexyloxyacetate, ethyllinalool, eugenol, coumarin, ethyl acetoacetate, 4-phenyl-2,4,6- trimethyl-1 ,3-dioxane, 4-methylene-3,5,6,6-tetramethyl-2-heptanone, ethyl tetrahydrosafranate, geranyl nitrile, cis-3-hexen-1 -ol, cis-3-hexenyl acetate, cis-3-hexenyl methyl carbonate, 2,6- dimethyl-5-hepten-1 -al, 4-(tricyclo[5.2.1 .0]decylidene)-8-butanal, 5-(2,2,3-trimethyl-3- cyclopentenyl)-3-methylpentan-2-ol, p-tert-butyl-alpha-methylhydrocinnamaldehyde, ethyl[5.2.1 .0]tricyclodecanecarboxylate, geraniol, citronellol, citral, linalool, linalyl acetate, io- none, phenylethanol and mixtures thereof.

For the purposes of the present invention, a volatile odorous substance preferably has a boiling point or boiling point range below 300°C. The odorous substance is more preferably a readily volatile compound or mixture. In particular, the odorous substance has a boiling point or boiling range below 250°C, more preferably below 230°C, particularly preferably below 200°C.

Preference is likewise given to odorous substances which have a high volatility. The vapor pressure can be employed as a measure of the volatility. For the purposes of the present inven- tion, a volatile odorous substance preferably has a vapor pressure of more than 0.001 kPa (20°C). The odorous substance is more preferably a readily volatile compound or mixture. The odorous substance particularly preferably has a vapor pressure of more than 0.01 kPa (20°C), more preferably a vapor pressure of more than 0.05 kPa (20°C). Particular preference is given to the odorous substances having a vapor pressure of more than 0.1 kPa (20°C).

In addition, the shaped bodies of the invention can be used as support, in particular as support of a catalyst.

Preferably, the shaped body of the present invention has a cutting hardness of 0.5 N to 100 N. This is especially preferred for a shaped body that has a diameter of at least 1 mm and not more than 10 mm and a length of at least 1 mm and not more than 30 mm. Preferably, the cut- ting hardness is from 1 .5 N to 50 N. This is especially preferred for a shaped body that has a diameter of at least 1 mm and not more than 5 mm and a length of at least 1 mm and not more than 25 mm, more preferred a diameter of at least 1 mm and not more than 4 mm and a length of at least 1 mm and not more than 20 mm, most preferred a diameter of at least 1 mm and not more than 3 mm and a length of at least 1 mm and not more than 15 mm.

The determination/measurement of the cutting hardness was carried out as described in the earlier German patent application no. 103261 137.0 of June 6, 2003 (BASF AG): The cutting hardnesses were measured on an apparatus from Zwick (model: BZ2.5/TS1 S; initial loading: 0.5 N, preliminary advance rate: 10 mm/min; test speed: 1 .6 mm/min) and are the means of in each case 10 measured catalyst extrudates. In detail, the cutting hardness was determined as follows: Extrudates were loaded with increasing force by means of a cutter having a thickness of 0.3 mm until the extrudate had been cut through. The force required for this is the cutting hardness in N (Newton). The determination was carried out on a testing apparatus from Zwick, Ulm, having a rotating plate in a fixed position and a freely movable, vertical punch with built-in cutter having a thickness of 0.3 mm. The movable punch with the cutter was connected to a load cell to record the force and during the measurement moved towards the rotating plate on which the extrudate to be measured was located. The test apparatus was controlled via a computer which recorded and evaluated the measurement results. 10 straight, preferably crack-free extrudates were taken from a well-mixed sample and their cutting hardnesses were determined and sub- sequently averaged.

In a preferred embodiment, the specific surface area of the shaped body of the present invention, as calculated according to the Langmuir model (DI N 66131 , 66134) is above 50 m ² /g, further preferred above 100 m ² /g, more preferably above 150 m ² /g, particularly preferred above 500 m ² /g and may increase into the region above 3000 m ² /g.

The surface area per volume of the shaped bodies according to the present invention preferably amounts to 100 m ² /ml_ or more and even more preferably to 200 m ² /ml_ or more and even more preferably to 300 m ² /ml_ or more. The values obtained for the surface area were obtained ac- cording to the Langmuir model.

The pore volume was determined via mercury porosimetry using an Autopore IV instrument and the Rootare-Prenzlow equation for data evaluation. The pore volume has a preferred value of from 0.05 to 2.0 mL/g, more preferred 0.1 to 1.5 mL/g, even more preferred 0.2 to 1 .2 mL/g, most preferred 0.3 to 1.1 mL/g.

Bulk densities of extrudate packings were determined using a jolting volumeter type STAV II from J. Engelsmann AG. The machine has been tested according to DIN ISO 787 by the manufacturer. A weighed amount of the respective sample was put into a 1000 or 100 ml. scaled cylinder. After tapping the cylinder 3000 times, the resulting volume of the packing was determined and the density calculated by dividing sample weight by sample volume.

The bulk density has a preferred value of from 0.1 to 1 .0 g/mL, more preferred of from 0.3 to 0.9 g/mL, even more preferred of from 0.4 to 0.8 g/mL.

In the context of the present invention, the term "extrusion" refers to any process known to the expert in the field by which a substance that does not fulfill the above-mentioned requirement of a shaped body, i.e. any powder, powdery substance, array of crystallites etc., can be formed into a shaped body that is stable under the conditions of its intended use by means of an extruder.

The present invention is illustrated by means of the examples below. The following examples describe the extrusion of MOFs according to this invention. The material that was applied was prepared as described in WO 12/042410. Its surface area ranged from 1200-1300 m ² /g.

The determination/measurement of the cutting hardness was carried out as described in the earlier German patent application no. 103261 137.0 of June 6, 2003 (BASF AG): The cutting hardnesses were measured on an apparatus from Zwick (model: BZ2.5/TS1 S; initial loading: 0.5 N, preliminary advance rate: 10 mm/min; test speed: 1 .6 mm/min) and are the means of in each case 10 measured catalyst extrudates. In detail, the cutting hardness was determined as follows: Extrudates were loaded with increasing force by means of a cutter having a thickness of 0.3 mm until the extrudate had been cut through. The force required for this is the cutting hardness in N (Newton). The determination was carried out on a testing apparatus from Zwick, Ulm, having a rotating plate in a fixed position and a freely movable, vertical punch with built-in cutter having a thickness of 0.3 mm. The movable punch with the cutter was connected to a load cell to record the force and during the measurement moved towards the rotating plate on which the extrudate to be measured was located. The test apparatus was controlled via a computer which recorded and evaluated the measurement results. 10 straight, preferably crack-free extrudates were taken from a well-mixed sample and their cutting hardnesses were determined and subsequently averaged. The obtained shaped bodies exhibited a relatively broad length distribution due to manual breaking of the strands instead of machine cutting after the extrusion. The smallest and largest lengths ranged from 0.3 to 2.0 cm. After being broken to shorter pieces, the strands were dried (12 h, 100°C) and calcined (5 h, 200°C). The pore volume was determined via mercury porosimetry using an Autopore IV instrument and the Rootare-Prenzlow equation for data evaluation.

Bulk densities of extrudate packings were determined using a jolting volumeter type STAV II from J. Engelsmann AG. The machine has been tested according to DIN ISO 787 by the manufacturer. A weighed amount of the respective sample was put into a 1000 or 100 ml. scaled cylinder. After tapping the cylinder 3000 times, the resulting volume of the packing was determined and the density calculated by dividing sample weight by sample volume.

The density of extrudates was determined by weighing a selected extrudate, measuring its diameter and length with a sliding calliper and then dividing weight by volume (the latter being calculated via the diameter and length). Example 1 : Extrusion of spray-dried aluminum-fumarate powder (residual water content 4 wt%) without any additive

Aluminum-fumarate MOF (1 10 g) was densified with water (158 g) in a kneading machine (5 min). The obtained plastic mixture was formed to strands (0 2.0 mm) using a strand press. Bulk density of extrudate packing: 0.59 g/ml

Average density of extrudates: 1 .04-1 .36 g/ml

Langmuir surface area: 1050 m ² /g

Pore volume: 0.24 mL/g (determined via Hg-Porosimetry)

Cutting hardness: 23.6 N

Methane uptake: 60 g/L, 6.0 wt% (at 298 K, 50 bar)

Example 2: Extrusion of spray-dried aluminum-fumarate powder (residual water content 4 wt%) with 20 wt% Pural SB

Aluminum-fumarate MOF (1 10 g) was mixed with Pural SB (27.5 g). The mixture was densified in a first step with diluted formic acid (1 .1 g in 10 g water) and in a second step with water (145 g) in a kneading machine (overall 20 min). The obtained plastic mixture was formed to strands

(0 2.0 mm) using a strand press.

Bulk density of extrudate packing: 0.58 g/mL

Average density of extrudates: 0.95-1 .18 g/ml

Langmuir surface area: 979 m ² /g

Pore volume: 0.23 mL/g (determined via Hg-Porosimetry)

Cutting hardness: 22.0 N

Methane uptake: 58 g/L, 5.5 wt% (at 298 K, 50 bar)

Example 3: Extrusion of spray-dried aluminum-fumarate powder (residual water content 4 wt%) with 20 wt% Pural SB

Aluminum-fumarate MOF (3000 g) was mixed with Pural SB (750 g). The mixture was densified in a first step with diluted formic acid (22.55 g in 100 g water) and in a second step with water (3100 g) in a mix muller (overall 15 min). The obtained plastic mixture was formed to strands (0 2.5 mm) using a strand press.

Bulk density: 0.72 g/mL

Average density of extrudates 1 .03-1 .35 g/ml

Langmuir surface area: 672 m ² /g

Pore volume: 0.1 1 mL/g (determined via Hg-Porosimetry)

Cutting hardness: 82.7 N

Methane uptake: 56 g/L (at 298 K, 50 bar)

Methane uptake: 1 .28 wt% (at 298 K, 918 mmHg)

Example 4: Extrusion of spray-dried aluminum-fumarate powder (residual water content 4 wt%) with 30 wt% Pural SB

Aluminum-fumarate MOF (3000 g) was mixed with Pural SB (1286 g). The mixture was densified in a first step with diluted formic acid (38.6 g in 100 g water) and in a second step with wa- ter (4950 g) in a mix muller (overall 15 min). The obtained plastic mixture was formed to strands (0 2.5 mm) using a strand press.

Bulk density: 0.74 g/mL

Average density of extrudates: 1 .13-1 .25 g/ml

Langmuir surface area: 809 m ² /g

Pore volume: 0.16 mL/g (determined via Hg-Porosimetry)

Cutting hardness: 45.9 N

Methane uptake: 56 g/L (at 298 K, 50 bar)

Methane uptake: 1 .16 wt% (at 298 K, 921 mmHg) Example 5: Extrusion of spray-dried aluminum-fumarate powder (residual water content 57 wt%) with 20 wt% Pural SB

Aluminum-fumarate MOF (6170.0 g) was mixed with Pural SB (767.5 g). The mixture was densified in a first step with diluted formic acid (23.0 g in 100 g water) and in a second step with water (1050 g) in a mix muller (overall 4 min). The obtained plastic mixture was formed to strands (0 3.5 mm) using a strand press.

Bulk density: 0.56 g/mL

Average density of extrudates: 1 .00-1 .19 g/ml

Langmuir surface area: 938 m ² /g

Pore volume: 0.26 mL/g (determined via Hg-Porosimetry)

Cutting hardness: 38.1 N

Methane uptake: 56 g/L, 5.0 wt% (at 298 K, 50 bar)

Methane uptake: 1 .33 wt% (at 298 K, 918 mmHg)

Example 6: Extrusion of aluminum-fumarate MOF/Pural SB spheres (residual water content 60 wt%, 20 wt% Pural SB introduced during spray-drying)

Aluminum-fumarate MOF/Pural SB spheres (2857 g) were densified with diluted formic acid (6.2 g in 100 g water) in a mix muller (overall 4 min). The obtained plastic mixture was formed to strands (0 3.5 mm) using a strand press.

Bulk density: 0.46 g/mL Average density of extrudates 0.65-0.81 g/ml

Langmuir surface area: 1012 m ² /g

Pore volume: 0.45 mL/g (determined via Hg-Porosimetry)

Cutting hardness: 14.2 N

Methane uptake: 54 g/L, 5.0 wt% (at 298 K, 50 bar)

Methane uptake: 1 .39 wt% (at 298 K, 918 mmHg)

Example 7: Extrusion of aluminum-fumarate MOF filter cake (residual water content 70 wt%) without any additive

Aluminum-fumarate MOF filter cake (215.0 g) was mixed with aluminum-fumarate MOF powder (4 wt% residual water, 61 .6 g). The mixture was densified in a kneading machine (5 min). The obtained plastic mixture was formed to strands (0 2.0 mm) using a strand press.

Bulk density: 0.46 g/mL

Average density of extrudates: 0.48-0.97 g/ml

Langmuir surface area: 1043 m ² /g

Pore volume: 0.24 mL/g (determined via Hg-Porosimetry)

Cutting hardness: 26.5 N

Methane uptake: 57 g/L, 6.0 wt% (at 298 K, 50 bar)

Methane uptake: 1 .60 wt% (at 298 K, 918 mmHg)

Comparative Example 8: Pelletizing of aluminum-fumarate MOF powder with graphite

Aluminum-fumarate MOF (16154 g) was mixed with graphite (246 g). The mixture was compacted to pellets (3x3 mm) in a Kilian compaction machine.

Bulk density: 0.35 g/mL

Langmuir surface area: 1 150 m ² /g

Pore volume: 1 .13 mL/g (determined via Hg-Porosimetry)

Cutting hardness: 15.0 N

Methane uptake: 60 g/L, 6.0 wt% (at 298 K, 50 bar)

Table 1 : Comparison of extrudate properties from Examples 1 to 7 with respect to Comparative example 8. The increase/decrease of selected properties of Examples 1 to 7 with respect to Comparative example 8 is given in %.

The relative increase of bulk density and especially cutting hardness outweighs the loss of methane uptake capacity.

Example 9: Extrusion of aluminum-trimesate MOF (oven-dried) with Pural SB

Aluminum-trimesate MOF (120.0 g) was mixed with Pural SB (30.0 g). The mixture was densi- fied in a first step with diluted formic acid (1 .0 g in 10 g water) and in a second step with water

(228 g) in a mix muller (overall 21 min). The obtained plastic mixture was formed to strands (0

3.5 mm) using a strand press.

Bulk density: 0.32 g/ml_

Langmuir surface area: 435 m ² /g

Pore volume: 1 .01 mL/g (determined via Hg-Porosimetry)

Cutting hardness: 9.5 N

Methane uptake: 45 g/L (at 298 K, 50 bar)

Methane uptake: 0.65 wt% (at 298 K, 921 mmHg)

Comparative Example 10: Pelletizing of aluminum-trimesate MOF powder with graphite

Aluminum-trimesate MOF (46.0 g) was mixed with graphite (1.4 g). The mixture was compacted to pellets (3x3 mm) in a Kilian compaction machine.

Bulk density: 0.46 g/ml_ Langmuir surface area: 743 m ² /g

Pore volume: 0.39 mL/g (determined via Hg-Porosimetry)

Cutting hardness: 45.0 N Example 1 1 : Catalyst preparation from extrudates of Example 9

The extrudates resulting from Example 9 (aluminum-trimesate MOF) were mechanically sized into smaller pieces and sieved to separate a split fraction with size of 0.5 to 0.6 mm. This size fraction was used for testing in the reactor. The resultant catalyst is referred to as the fresh state meaning that is has not been subjected to any hydrothermal aging.

The Langmuir surface area was found to be not altered by the procedure (435 m ² /g).

Comparative Example 12: Catalyst preparation from pellets of Comparative Example 10

The pellets resulting from comparative Example 10 (aluminum-trimesate MOF) were mechanically sized into smaller pieces and sieved to separate a split fraction with size of 0.5 to 0.6 mm. This size fraction was used for testing in the reactor. The resultant catalyst is referred to as the fresh state meaning that is has not been subjected to any hydrothermal aging.

The Langmuir surface area was found to be 632 m ² /g.

Example 13: Aging

4.00 g of catalyst from Example 1 1 were placed in a U-type reactor (49.5 cm length, 0.6 cm diameter). The reactor was fixed in an adjustable furnace and the furnace was heated up to 200 °C. A stream of nitrogen (6 l/h) was fed with water vapor (200 °C) via a HPLC-pump with a pump rate of 8.021 g IPA per hour. To avoid the condensation of water, all lines from the satura- tor to the cryostat were heated above 120 °C. The gaseous reaction mixture was fed into the reactor at a weight hourly space velocity of 2.0 g/(g ^* h). The temperature of the furnace was kept at 200 °C for 2h with constant water feed. The feed stream then was set on halt and the furnace was allowed to cool to room temperature. To evaluate the cycling stability the described aging tests were repeated up to 5 times. The Langmuir surface area and the surface retention are depicted in Table 1 .

Comparative Example 14: Aging

4.00 g of catalyst from Comparative Example 12 were placed in an U-type reactor (49.5 cm length, 0.6 cm diameter). The reactor was fixed in an adjustable furnace and the furnace was heated up to 200 °C. A stream of nitrogen (6 l/h) was fed with water vapor (200 °C) via a HPLC- pump with a pump rate of 8.021 g IPA per hour. To avoid the condensation of water, all lines from the saturator to the cryostat were heated above 120 °C. The gas reaction mixture fed the reactor at a weight hourly space velocity of 2.0 g/(g ^* h). The temperature of the furnace was kept at 200 °C for 2h with constant water feed. The feed stream then was set on halt and the furnace was allowed to cool down to down room temperature. To evaluate the cycling stability the de- scribed aging tests were repeated up to 3 times. The Langmuir surface area and the surface retention are depicted in Table 2.

Table 2 Langmuir surface area and the surface retention Comparative Example 14

Number of cycles Langmuir Surface area Surface Retention

[m ² /g] [%]

3 391 62