Description

The present invention relates to a process for the reduction of the content of (removal of) resid ual monomeric isocyanate in a polyurethane prepolymer containing said residual monomeric isocyanate comprising the step of contacting the polyurethane prepolymer with a porous mate rial having pores formed by a framework containing isocyanate reactive functional groups under conditions allowing chemical reaction of the reactive functional groups with the residual mono meric isocyanate in at least a fraction of the pores in order to covalently bind the reacted isocya nate. The invention also relates to a prepolymer composition comprising said porous material and the use of said porous material for removal residual monomeric isocyanate in the prepoly mer.

Polyurethane prepolymers based on the reaction of polyisocyanates and polyols typically pos sess a given amount of monomeric isocyanates. These prepolymers in general are used for manifold applications e.g. foamed and compact elastomers, sealants, coatings and adhesives in 1 -component and 2-component formulations.

The hazardous nature of monomeric isocyanates leads to a severe increase of regulatory re strictions from governmental institutions in 2018 the ECHA suggested to tighten the restrictions of use for diisocyanates significantly. E.g. for industrial use, the handling of products with resid ual monomeric isocyanates will require extensive safety trainings and additional technical measures to keep isocyanate levels in air low. Further, any private use of isocyanate based products in do-it-yourself applications like sealants or can foams is already to date restricted and further limitations are expected. To minimize the hazardous potential of these products, a limit of 0.1 wt -% of monomeric isocyanate was defined (“monomer free”). Products with con tents below 0.1 wt -% of aromatic or aliphatic isocyanate enable easy and safe handling of the monomer-free products both for industrial and private users.

One approach to obtain low monomeric isocyanate content is known in the art by designing an appropriate chemical protocol for the synthesis of the polyurethane prepolymer.

EP 2 155 797 B1 describes a process for the production of isocyanate prepolymers based on toluene diisocyanate having a content of free monomeric toluene diisocyanate content of not more than 0.1 wt -% using polyether polyols, wherein a certain index based on the hydroxyl number of the polyether is not exceeded.

EP 951 493 B1 describes a low-monomer polyurethane prepolymer containing free isocyanate groups obtained by reacting one or more polyhydric alcohols and two or more diisocyanates, wherein a ratio of a total number of first and second isocyanate groups of non-symmetrical diisocyanate to a number of isocyanate groups of a second diisocyanate is greater than 6:1.

EP 150444 B1 describes a process for the production of isocyanate-terminated polyurethane prepolymers based on diisocyanates of different reactivity, wherein in a first reaction step car ried out in the absence of other diisocyanates, 2,4-tolylene diisocyanate is reacted and in a sec ond reaction step, a symmetrical, dicyclic diisocyanate which is more reactive by comparison with the less reactive isocyanate groups of the 2,4-tolylene diisocyanate used in the first reac tion step is added.

However this approach has the drawbacks that it contains many steps causing high costs and a very high level of reaction control is required.

A further approach to reduce monomeric isocyanate content is the distillation of the prepolymer.

WO 03/046 040 A1 describes a process for the preparation of prepolymers comprising isocya nate and urethane groups, comprising the step of removing monomeric diisocyanates by distil ling the reaction product from step a) by means of a short-path evaporator.

EP 1 241 197 A1 describes a method for forming an isocyanate-functional prepolymer having a low residual isocyanate content by passing the reaction mixture comprising prepolymer and un reacted isocyanate through a short-path evaporator to remove unreacted isocyanate to a level of less than 0.15% by weight.

DE 199 39 840 A1 describes a process for producing prepolymers which contain isocyanate ter minal groups, wherein the reaction mixture is subsequently subjected to distillation, optionally with the addition of an entraining agent.

However, this approach has the drawback that an expensive distillation setup is required and that it can only be used for prepolymers that are stable under the distillation conditions and show low viscosities.

A further approach uses adsorbent material in order to remove residual monomeric isocyanate.

US 4,061 ,662 describes a method of reducing residual unreacted tolylene diisocyanate content in a prepolymer reaction product of toluene diisocyanate with a polyoxyalkylene polyol compris ing allowing said prepolymer to flow through a column packed with absorbent type X zeolite mo lecular sieves. However, the additional separation step results in an increased operating ex pense as described above for the distillation approach and the effectiveness is limited due to the high amount of zeolite that is needed. A further drawback of this and the distillation ap proach is that the amount of material is reduced due to the removal of the monomeric isocya nates. EP 2439220 A1 describes a carrier material which has functional groups on its surface which are reactive towards isocyanate groups, for reducing the proportion of isocyanate-containing monomers in compositions containing at least one isocyanate-containing polyurethane polymer and at least one isocyanate-containing monomer. This is accomplished by surface derivatization of amorphous silica by amino groups. However surface modification results in a limited active surface compared to the silica particles and is non-selective as not only residual monomeric iso cyanates can react with the amino functions on the surface but also other amino-reactive com ponents of the polymer, including terminal isocyanate functional groups of the polymer itself as well as other oligo- and polymeric isocyanates. The huge drawback of this approach is the tre mendous increase in viscosity after contacting theses functionalized silica with isocyanate con taining prepolymers.

International patent application with application N° PCT/EP2020/079866 describes the removal of residual monomeric aliphatic isocyanate from a reaction mixture comprising aliphatic polyiso cyanate using a scavenger comprising a zeolitic material.

Thus, an object of the present invention is to provide a method and polymer composition over coming the above disadvantages.

The object is achieved by a process for the reduction of the content of (removal of) residual monomeric isocyanate in a polyurethane prepolymer containing said residual monomeric isocy anate comprising the step of

(i) contacting the polyurethane prepolymer with a porous material having pores formed by a framework containing isocyanate reactive functional groups under conditions allowing chemical reaction of the reactive functional groups with the residual monomeric isocya nate in at least a fraction of the pores in order to covalently bind the reacted isocyanate, wherein the porous material is a porous metal-organic framework material comprising at least one metal ion and at least one at least bidentate organic compound, which is coordi- nately bound to said metal ion.

The object is also achieved by a polyurethane prepolymer composition, the composition com prising a polyurethane prepolymer comprising a porous material having pores formed by a framework containing isocyanate reactive functional groups, wherein the reactive functional groups are reacted with monomeric isocyanate in at least a fraction of the pores, wherein the porous material is a porous metal-organic framework material comprising at least one metal ion and at least one at least bidentate organic compound, which is coordinately bound to said metal ion.

The object is also achieved by the use of a porous material having pores formed by a frame work containing isocyanate reactive functional groups to remove residual monomeric isocyanate in a polyurethane prepolymer by chemical reaction of the reactive functional groups with the re sidual monomeric isocyanate in at least a fraction of the pores, wherein the porous material is a porous metal-organic framework material comprising at least one metal ion and at least one at least bidentate organic compound, which is coordinately bound to said metal ion.

Surprisingly, it was found that the use of a porous metal-organic framework (MOF) material hav ing pores formed by a framework containing isocyanate reactive functional groups under condi tions allowing chemical reaction of the reactive functional groups with the residual monomeric isocyanate in at least a fraction of the pores in order to covalently bind the reacted isocyanate, especially Basolite A 120 results in a substantially improved ability to capture the free monomer from TDI and MDI prepolymers. The functional group within the pores of the porous material al lows a selective reaction with monomeric isocyanate compared to oligomeric or polymeric isocy anate comprising substances. To remove the monomeric isocyanates, the prepolymer can -by way of example- be simply mixed with the porous material, annealed at 60 °C for 1-2 hours and kept at room temperature for 24 hours. The combination of the porous material that has an in trinsic size selectivity towards polymeric and monomeric components together with reactive groups inside the pores turned out to be the most efficient absorbent for monomer removal in isocyanate prepolymers. Further benefit is the moderate viscosity increase of the prepolymers containing the porous material, especially Basolite A 120, which is significantly lower than for the amino-functional fumed silicas.

Polyurethane prepolymers prepared from monomeric isocyanate are known in the art. In view of the selectivity of the porous material isocyanate groups containing polyurethane prepolymers are suitable.

The polyurethane prepolymers can be prepared by reaction of polyisocyanates with compounds having at least two isocyanate-reactive hydrogen atoms.

Suitable polyisocyanates include, for example, aliphatic, cycloaliphatic, aromatic and particularly aromatic diisocyanates. The following are specifically named by way of example: aliphatic diiso cyanates, such as hexamethylene 1 ,6-diisocyanate, 2-methylpentamethylene 1 ,5-diisocyanate, 2-ethylbutylene 1 ,4-diisocyanate or mixtures of at least two of said C ₆ -alkylene diisocyanates, pentamethylene 1 ,5-diisocyanate and butylene 1 ,4-diisocyanate, cycloaliphatic diisocyanates, such as 1-isocyanato-3,3,5-trimethyl-5-isocyanatomethylcyclohexane (isophorone diisocya nate), 1 ,4-cyclohexane diisocyanate, 1 -methyl-2,4- and -2,6-cyclohexane diisocyanate, as well as the corresponding isomer mixtures, 4,4'-, 2,4'- and 2,2'-dicyclo-hexylmethane diisocyanate, as well as the corresponding isomer mixtures and preferably aromatic diisocyanates, such as 1 ,5-naphthylene diisocyanate (1 ,5-NDI), 2,4- and 2,6-tolylene diisocyanate (TDI) as well as their mixtures, 2,4'-, 2,2'-, and preferably 4,4'-diphenylmethane diisocyanate (MDI) as well as mix tures of at least two of these isomers, having two or more aromatic systems. Suitable isocya nate components can also include derivatives of said isocyanates, such as uretdione, urea, biu ret or isocyanurate and mixtures thereof.

According to the process of the present invention said polyisocyanates represent residual mon omeric isocyanate to be removed in the polyurethane prepolymer. The term “removal” means according to the present invention any reduction of the content of residual monomeric isocya nate resulting from the contacting with the porous material. Preferably, the content of residual isocyanate in the prepolymer according to the present invention is at most 0.1 wt -% (percent by weight) based on the total weight of the prepolymer. The content of residual monomeric isocya nate is preferably determined by using high performance liquid chromatography (HPLC) with UV detection of samples derivatized with 1-(2-Piridlyl)piperazine.

In general polyisocyanates used in the preparation of the polyurethane prepolymer may have a molecular weight of less than 500 g/mol, preferably less than 400 g/mol, even more preferably less than 300 g/mol. The prefix “poly” in the term polyisocyanate refers to the fact that the isocy anate has at least two isocyanate groups and does not refer to a polymeric nature in weight.

The polyisocyanates represent monomers and thus are not oligomers or polymers.

Accordingly, the residual monomeric isocyanate is preferably an aromatic or aliphatic isocya nate. Thus, in one embodiment of the present invention the residual monomeric isocyanate is an aromatic isocyanate. In another embodiment of the invention the residual monomer is an ali phatic isocyanate. In an additional embodiment of the invention the residual monomer is a mix ture of aliphatic and aromatic monomeric isocyanates.

A preferred residual monomeric isocyanate is MDI in isomeric pure form or as mixture of 2,2’- MDI, 4,4'-MDI and 2,4'-MDI. Another preferred residual monomeric isocyanate is TDI in isomeric pure form or as mixture of 2,4-TDI and 2,6-TDI

Suitable compounds having at least two isocyanate-reactive hydrogen atoms preferably have at least two hydroxyl and/or amino groups in the molecule. Particularly suitable compounds have a molecular weight Mn in the range from 60 to 10000 g/mol. The compounds having at least two isocyanate-reactive hydrogen atoms are particularly preferably selected from the group consist ing of polyfunctional alcohols, polyetheralcohols, polyesteralcohols, polyetherpolyamines, hy droxyl-containing polycarbonates, hydroxyl-containing polyacetals and any mixtures of at least two thereof. Polyfunctional alcohols and polyether-alcohols, as well as mixtures thereof, are par ticularly preferred.

Examples of suitable polyfunctional alcohols are alkanediols having from 2 to 10, preferably from 2 to 6 carbon atoms, as well as higher alcohols, such as glycerol, trimethylolpropane or pentaerythritol. Furthermore, natural polyols can be used, such as castor oil.

The polyetheralcohols are preferably from di- to octafunctional. Their preparation is usually car ried out by addition of alkylene oxides, in particular ethylene oxide and/or propylene oxide, to FI- functional starters. The alkylene oxides can be used individually, in sequence or as a mixture. Possible starters include, for example, water, diols, triols, alcohols of higher functionality, sugar alcohols, aliphatic or aromatic amines or aminoalcohols. Polyetheralcohols having an average molecular weight in the range from 500 to 10 000 g/mol and an average OH-functionality in the range from 2 to 6 are particularly suitable. Particularly preferred starters for the preparation of these polyetheralcohols are propylene glycol and glyc erol. Preferred alkylene oxides are ethylene oxide and propylene oxide.

Polyesteralcohols having average molecular weights in the range from 1 000 to 10 000 g/mol and an average OH-functionality in the range from 2 to 3 are also preferred. Polyesteralcohols- based on adipic acid are particularly preferred. The preparation of the prepolymers is carried out, as explained, by reaction of the polyisocyanates with the compounds having at least two isocyanate-reactive hydrogen atoms.

Suitable catalysts, which in particular speed the reaction between the isocyanate groups of the polyisocyanates and the hydroxyl groups of the polyalcohols, include the known and conven tional strongly basic amines and also organic nnetal compounds such as titanic esters, iron com pounds such as iron(lll) acetylacetonate, tin compounds, e.g. tin(ll) salts of organic carboxylic acids, or the dialkyltin(IV) salts of organic carboxylic acids or mixtures of at least two of the named catalysts, bismuth salts of organic carboxylic acids as well as synergistic combinations of strongly basic amines and organic metal compounds. The catalysts can be used in the usual quantities, for example from 0.002 to 5% by weight, based on the polyalcohols.

The reaction can be carried out continuously or batchwise in the usual reactors, for example the known tubular or stirred-tank reactors, preferably in the presence of the usual catalysts, which speed the reaction of the OH-functional compounds with isocyanate groups, with or without inert solvents, i.e. compounds that do not react with the isocyanates and OH-functional compounds.

For instance, a polyurethane prepolymer was prepared by reacting toluene diisocyanate (TDI) with a ratio of 2,4-TDI:2,6-TDI=80:20 with poly(tetramethylene ether glycol) with an OH value of 112 mg KOH/g in the presence of diglycol-bis-chloroformiat (DIBIS). The prepolymer has an NCO content of 6.09%, free monomer content was 0.4% 2,4-TDI and 2.1% 2,6-TDI and a vis cosity of 11.4 Pas at 25 °C.

Another exemplary polyurethane prepolymer w ^r as prepared by reacting methylene diphenyl diisocyanate (MDI) with a ratio of 4,4’-MDI:2,4’-MDI: 2,2’-MDI=1 :1:0.05 with polypropylene gly col) with an OH value of 104 mg KOH/g in the presence of Diglycol-bis-chloroformiat (DIBIS). The prepolymer has an NCO content of 5.27%, free monomer content of 2.1% 4,4’-MDI, 4.7% 2,4’-MDI and 0.4% 2,2’-MDI and a viscosity of 2,8 Pas at 60 °C.

The prepolymers are customarily used in the preparation of polyurethanes. To this end, the pre polymers are reacted with compounds that can react with isocyanate groups. The compounds that can react with isocyanate groups include, for example, water, alcohols, amines or com pounds having mercapto groups. The polyurethanes can be used as foams, coatings, adhe sives, in particular melt-applied adhesives, paints, as well as compact or cellular elastomers. The polyurethane prepolymer is contacted with a porous MOF material. Said porous MOF mate rial has pores formed by a framework. Within the pores the framework contains isocyanate reac tive functional groups capable of allowing chemical reaction of the reactive functional groups with the residual monomeric isocyanate in at least a fraction of the pores in order to covalently bind the reacted isocyanate. The covalently binding results in reduction of residual monomeric isocyanate content.

The porous MOF material has pores, wherein the mean pore size of the porous material before contacting, i.e. before reaction with residual monomeric isocyanate, is preferably in the range from 0.3 to 9.0 nm. More preferably, the range is from 0.5 to 5.0 nm, even more preferably from 1.0 to 2.5 nm, even more from 1.5 to 2.2 nm, according to DIN ISO 9277:2014-01 (Determina tion of the specific surface area of solids by gas adsorption - BET method).

Preferably, the porous MOF material has before the contacting a total pore volume in the range from 0.04 to 4.0 cm ³ /g. More preferably, the range is from 0.4 to 2.0, even more preferably 1.0 to 1.8 cm ³ /g, according to DIN ISO 9277:2014-01 (Determination of the specific surface area of solids by gas adsorption - BET method).

Preferably, the porous MOF material has before the contacting a specific surface area BET from 10 to 5700 m ² /g, more preferably from 150 to 5700 m ² /g. More preferably, the range is from 300 to 4500 m ² /g, even more preferably, from 400 to 4500 m ² /g, even more preferably from 1000 to 3300 m ² /g according to DIN ISO 9277:2014-01 (Determination of the specific surface area of solids by gas adsorption - BET method).

The isocyanate reactive functional groups are preferably amino, hydroxyl, thiol, epoxy or a mix ture of two or more of these groups, preferably amino groups, more preferably primary amino groups.

Examples for the at least bidentate organic compound functionalized with one or more amino groups are for example aspartic acid, glutamic acid, arginine, histidine, proline, tryptophane, amino-fumaric acid, amino-maleic acid, amino-tartaric acid, amino-muconic acid, amino-hy- droxy-1 ,4-benzenedicarboxylic acid, amino-dihydroxy-1 ,4-benzenedicarboxylic acid, amino-im idazole, amino-pyrazole, amino-1 ,4-butanedicarboxylic acid, amino-1 ,4-butenedicarboxylic acid, amino-1 ,6-hexanedicarboxylic acid, amino-decanedicarboxylic acid, amino-1 ,8-heptadecanedi- carboxylic acid, amino-1 ,9-heptadecanedicarboxylic acid, amino-heptadecanedicarboxylic acid, amino-1 ,2-benzenedicarboxylic acid, amino-1 ,3-benzenedicarboxylic acid, amino-2, 3-pyridinedi- carboxylic acid, amino-pyridine-2, 3-dicarboxylic acid, amino-1 ,3-butadiene-1 ,4-dicarboxylic acid, amino-1 ,4-benzenedicarboxylic acid, amino-p-benzenedicarboxylic acid, amino-imidazole-2, 4- dicarboxylic acid, 4,4'-diaminophenylmethane-3,3'-dicarboxylic acid, amino-pyridine-2, 6-dicar- boxylic acid, amino-thiophene-3, 4-dicarboxylic acid, amino-perylene-3,9-dicarboxylic acid, amino-perylenedicarboxylic acid, amino-3, 6-dioxaoctanedicarboxylic acid, amino-3, 5-cyclohexa- diene-1 ,2-dicarboxylic acid, amino-octadicarboxylic acid, amino-pentane-3, 3-carboxylic acid, amino-1 , 1'-dinaphthyldicarboxylic acid, amino-phenylindanedicarboxylic acid, amino-1 ,4-cyclo- hexanedicarboxylic acid, amino-naphthalene-1 ,8-dicarboxylic acid, amino-2, -benzoylbenzene- 1 ,3-dicarboxylic acid, amino-1 ,4-naphthalenedicarboxylic acid, amino-2, 6-naphthalenedicarbox- ylic acid, amino-1 ,3-adamantanedicarboxylic acid, amino-1 ,8-naphthalenedicarboxylic acid, amino-2, 3-naphthalenedicarboxylic acid, amino-8-methoxy-2,3-naphthalenedicarboxylic acid, amino-8-nitro-2,3-naphthalenecarboxylic acid, amino-8-sulfo-2, 3-naphthalenedicarboxylic acid, amino-anthracene-2, 3-dicarboxylic acid, amino-imidazole-4, 5-dicarboxylic acid, amino-4-cyclo- hexene-1 ,2-dicarboxylic acid, amino-tetradecanedicarboxylic acid, amino-1 ,7-heptadicarboxylic acid, amino-5-hydroxy-1 ,3-benzenedicarboxylic acid, amino-2, 5-dihydroxy-1 ,4-dicarboxylic acid, amino-pyrazine-2, 3-dicarboxylic acid, amino-furan-2, 5-dicarboxylic acid, amino-2, 5-pyridinedi- carboxylic acid, amino-cyclohexene-2, 3-dicarboxylic acid, amino-1 ,3-benzenedicarboxylic acid, amino- 2,6-pyridinedicarboxylic acid, amino-anthraquinone-1 , 5-dicarboxylic acid, amino-3, 5-py- razoledicarboxylic acid, amino-2-nitrobenzene-1 ,4-dicarboxylic acid, amino-heptane-1 ,7-dicar- boxylic acid, amino-cyclobutane-1 , 1-dicarboxylic acid, amino-1 , 14-tetradecanedicarboxylic acid, amino-5, -6-dehydronorbornane-2, 3-dicarboxylic acid, amino-5-ethyl-2,3-pyridinedicarboxylic acid or amino-camphordicarboxylic acid.

For example, the at least bidentate organic compound can be derived from a tricarboxylic acid that already has at least one isocyanate reactive functional group or that can serve as starting material for the preparation of a tricarboxylic acid by derivatization. Examples of tricarboxylic ac ids are amino-2-hydroxy-1 ,2,3-propanetricarboxylic acid, amino-1 ,2,3-, amino-1 ,2, 4-benzenetricarbox- ylic acid, amino-1 ,2, 4-butanetricarboxylic acid, amino-1 , 3, 5-benzenetricarboxylic acid, amino- 1 -hydroxy-1 , 2, 3-propanetricarboxylic acid, amino-benzene-trisbenzoic acid.

Examples of an at least bidentate organic compound derived from a tetracarboxylic acid that can serve as starting material for the preparation of a tetracarboxylic acid by derivatization, are amino-1 ,2,4,5-benzenetetracarboxylic acid, amino-1 ,2,5,6-hexanetetracarboxylic acid, amino- 1 , 2,7, 8-octanetetracarboxylic acid, amino-1 ,4,5,8-naphthalenetetracarboxylic acid, amino- 1 ,2,9, 10-decanetetracarboxylic acid, amino-benzophenonetetracarboxylic acid, amino- 3, 3', 4, 4'-benzophenonetetracarboxylic acid.

In a preferred embodiment the polyurethane prepolymer is liquid under the conditions allowing the chemical reaction. As mentioned above the viscosity of a prepolymer can be influenced by the polyisocyanate as starting material and residual monomeric isocyanate. Further viscosity in fluencing factors are known by the practitioner in the art. Within the meaning of the present in vention the term “liquid” is preferably used in case the viscosity is in the range from 0.1 to 10 ⁷ mPas The viscosity can be determined with a Haake-Mars rheometer with plate-plate geometry in rotation and 1 mm gap width at a shear rate of 10 and 40 S ¹ at the given temperature. Preferably, the ratio (w/w) polyurethane prepolymer to porous material is in the range of from 100:0.1 to 100:50, more preferably from 100:0.1 to 100:20, even more preferably from 100:0.1 to 100:10, even more preferably from 100:0.1 to 100:5.

Preferably, the residual monomer isocyanate content of the polyurethane prepolymer is reduced by at least 50 %, more preferably by at least 90%, even more preferably by at least 95%, even more preferably by at least 99 % in step (i).

The isocyanate reactive functional groups contained in the pores of the porous material can be introduced by using a porous material without said groups and subsequently derivatization of the porous material in order to introduce the functional groups. Additionally, the reactive func tional groups may be present as a part of one or more framework forming component. The latter is preferred.

It is preferred that the porous metal-organic framework material comprising the at least one metal ion and the at least one at least bidentate organic compound, which is coordinately bound to said metal ion is prepared by contacting the at least one metal ion with the at least one at least bidentate organic compound, wherein the at least one at least bidentate organic com pound already contains the isocyanate reactive functional groups.

Thus, metal-organic framework material is preferably used, wherein the at least one at least bi dentate organic compound already comprises isocyanate reactive functional groups or wherein the at least one at least bidentate organic compound, already known as starting material for the preparation of metal-organic framework material, can be derivatized in order to introduce isocy anate one or more reactive functional groups. By way of example dicarboxylic acids are known to form metal-organic frameworks with metal ion. Such a dicarboxylic acid can be derivatized by introducing an amino group in order to provide an at least bidentate organic compound in order to form a framework with pores having amino groups therein.

Such metal-organic frameworks (MOFs) are known in the prior art and are described, for exam ple, in US 5,648,508, EP-A-0 790253, M. O'Keeffe et al„ J. Sol. State Chem., 152 (2000), pages 3 to 20, H. Li et al., Nature 402, (1999), page 276, M. Eddaoudi et al., Topics in Catalysis 9, (1999), pages 105 to 111, B. Chen et al., Science 291, (2001), pages 1021 to 1023,

DE-A 101 11 230, DE-A 102005053430, WO-A 2007/054581 , WO-A 2005/049892 and WO-A 2007/023134.

The metal-organic frameworks comprise pores, in particular micropores and/or mesopores. Mi cropores are defined as pores having a diameter of 2 nm or less and mesopores are defined by a diameter in the range from 2 to 50 nm, in each case in accordance with the definition given in Pure & Applied Chem. 57 (1985), 603 - 619, in particular on page 606. The presence of mi cropores and/or mesopores can be checked by means of sorption measurements, with these measurements determining the uptake capacity of the MOF for nitrogen at 77 Kelvin in accord ance with DIN ISO 9277:2014-01. The specific surface area, calculated according to the Langmuir model of an MOF in powder form is preferably more than 100 m ² /g, more preferably above 300 m ² /g, more preferably more than 700 m ² /g, even more preferably more than 800 m ² /g, even more preferably more than 1000 m ² /g and particularly preferably more than 1200 m ² /g.

Shaped bodies comprising metal-organic frameworks can have a lower active surface area; but preferably more than 150 m ² /g, more preferably more than 300 m ² /g, even more preferably more than 700 m ² /g.

The metal component in the framework according to the present invention is preferably selected from groups la, lla, Ilia, IVa to Villa and lb to Vlb. Particular preference is given to Mg, Ca, Sr, Ba, Sc, Y, Ln, Ti, Zr, Hf, V, Nb, Ta, Cr, Mo, W, Mn, Re, Fe, Ro, Os, Co, Rh, Ir, Ni, Pd, Pt, Cu,

Ag, Au, Zn, Cd, Fig, Al, Ga, In, TI, Si, Ge, Sn, Pb, As, Sb and Bi, where Ln represents the lan thanides.

Lanthanides are La, Ce, Pr, Nd, Pm, Sm, En, Gd, Tb, Dy, Ho, Er, Tm, Yb.

With regard to the ions of these elements, particular mention may be made of Mg ²⁺ , Ca ²⁺ , Sr ²⁺ , Ba ²⁺ , Sc ³⁺ , Y ³⁺ , Ln ³⁺ , Ti ⁴⁺ , Zr ⁴⁺ , Hf ⁴⁺ , V ⁴⁺ , V ³⁺ , V ²⁺ , Nb ³⁺ , Ta ³⁺ , Cr ³⁺ , Mo ³⁺ , W ³⁺ , Mn ³⁺ , Mn ²⁺ , Re ³⁺ , Re ²⁺ , Fe ³⁺ , Fe ²⁺ , Ru ³⁺ , Ru ²⁺ , Os ³⁺ , Os ²⁺ , Co ³⁺ , Co ²⁺ , Rh ²⁺ , Rh ⁺ , lr ²⁺ , lr ⁺ , Ni ²⁺ , Ni ⁺ , Pd ²⁺ , Pd ⁺ , Pt ²⁺ , Pt ⁺ , Cu ²⁺ , Cu ⁺ , Ag ⁺ , Au ⁺ , Zn ²⁺ , Cd ²⁺ , Hg ²⁺ , Al ³⁺ , Ga ³⁺ , ln ³⁺ , Tl ³⁺ , Si ⁴⁺ , Si ²⁺ , Ge ⁴⁺ , Ge ²⁺ , Sn ⁴⁺ , Sn ²⁺ , Pb ⁴⁺ , Pb ²⁺ , As ⁵⁺ , As ³⁺ , As ⁺ , Sb ⁵⁺ , Sb ³⁺ , Sb ⁺ , Bi ⁵⁺ , Bi ³⁺ and Bi ⁺ .

Preferred metals are Mg, Ca, Sr, Ba, Sc, Y, Ln, Ti, Zr, Hf, V, Nb, Ta, Cr, Mo, W, Mn, Re, Fe, Ro, Os, Co, Rh, Ir, Ni, Pd, Pt, Cu, Ag, Au, Zn, Cd, Hg, Al, Ga, In, TI, Si, Ge, Sn, Pb, As, Sb, Bi, and mixtures thereof ND wherein Ln represents a lanthanide, preferably Mg, Al, Y, Sc, Zr, Ti, V, Cr, Mo, Fe, Co, Cu, Ni, Zn, Ln, even more preferably Al, Mg, Fe, Cu and Zn, even more preferably Mg and Al, even more preferably Al.

The term "at least bidentate organic compound" refers to an organic compound which com prises at least one functional group which is able to form at least two coordinate bonds to a given metal ion and/or a coordinate bond to each of two or more, preferably two, metal atoms.

As functional groups via which the coordinate bonds mentioned can be formed, particular men tion may be made of, for example, the following functional groups -CO ₂ H, -CS ₂ H, -NO ₂ ,

-B(OH) ₂ , -SO ₃ H, -Si(OH) ₃ , -Ge(OH) ₃ , -Sn(OH) ₃ , -Si(SH) ₄ , -Ge(SH) ₄ , -Sn(SH) ₃ , -P0 ₃ H, -As0 ₃ H, -AS0 ₄ H, -P(SH) ₃ , -AS(SH) ₃ , -CH(RSH) ₂ , -C(RSH) ₃ , -CH(RNH ₂ ) , -C(RNH ₂ ) ₃ , -CH(R0H) ₂ , -CH(RCN) ₂ , -C(RCH) ₃ , where R is, for example, preferably an alkylene group having 1 , 2, 3, 4 or 5 carbon atoms, for example a methylene, ethylene, n-propylene, i-propylene, n-butylene, i-butylene, tert-butylene or n-pentylene group, or an aryl group comprising 1 or 2 aromatic rings, for example 2 Ob rings, which may, if appropriate, be fused and may be independently substi- tuted by at least one substituent in each case and/or may comprise, independently of one an other, at least one heteroatom such as N, O arid/or S In likewise preferred embodiments, func tional groups in which the abovementioned radical R is not present are possible. Such groups are, inter alia, CH(SH) ₂ , -C(SH) ₃ , -CH(NH ₂ ) ₂ , -C(NH ₂ ) ₃ , -CH(OH) ₂ , -C(OH) ₃ , -CH(CN) ₂ or C(CN) ₃ .

However, the functional groups can also be heteroatoms of a heterocycle. Particular mention may here be made of nitrogen atoms.

The at least two functional groups can in principle be any suitable organic compound, as long as it is ensured that the organic compound in which these functional groups are present is capa ble of forming the coordinate bond and of producing the framework.

The organic compounds which comprise the at least two functional groups are preferably de rived from a saturated or unsaturated aliphatic compound or an aromatic compound or a both aliphatic and aromatic compound.

The aliphatic compound or the aliphatic part of the both aliphatic and aromatic compound can be linear and/or branched and/or cyclic, with a plurality of rings per compound also being possi ble. More preferably, the aliphatic compound or the aliphatic part of the both aliphatic and aro matic compound comprises from 1 to 15, more preferably from 1 to 14, more preferably from 1 to 13, more preferably from 1 to 12, more preferably from 1 to 11 and particularly preferably from 1 to 10, carbon atoms, for example 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10 carbon atoms. Particular preference is here given to, inter alia, methane, adamantane, acetylene, ethylene or butadiene.

The aromatic compound or the aromatic part of the both aromatic and aliphatic compound can have one or more rings, for example two, three, four or five rings, with the rings being able to be separate from one another and/or at least two rings being able to be present in fused form. The aromatic compound or the aromatic part of the both aliphatic and aromatic compound particu larly preferably has one, two or three rings, with one or two rings being particularly preferred. Furthermore, each ring of the specified compound can independently comprise at least one het eroatom such as N, O, S, B, P, Si, Al, preferably N, O and/or S. The aromatic compound or the aromatic part of the both aromatic and aliphatic compound more preferably comprises one or two C ₆ rings which are present either separately or in fused form. Particular mention may be made of benzene, naphthalene and/or biphenyl and/or bipyridyl and/or pyridyl as aromatic com pounds.

The at least bidentate organic compound is more preferably an aliphatic or aromatic, acyclic or cyclic hydrocarbon which has from 1 to 18, preferably from 1 to 10 and in particular 6, carbon atoms and additionally has exclusively 2, 3 or 4 carboxyl groups as functional groups.

For example, the at least bidentate organic compound is derived from a dicarboxylic acid that already has at least one isocyanate reactive functional group or that can serve as starting mate rial for the preparation of a dicarboxylic acid by derivatization. Examples of dicarboxylic acids are oxalic acid, succinic acid, tartaric acid, 1 ,4-butanedicarboxylic acid, 1 ,4-butenedicarboxylic acid, 4-oxopyran-2,6-dicarboxylic acid, 1 ,6-hexanedicarboxylic acid, decanedicarboxylic acid,

1.8-heptadecanedicarboxylic acid, 1 ,9-heptadecanedicarboxylic acid, heptadecanedicarboxylic acid, acetylenedicarboxylic acid, 1 ,2-benzenedicarboxylic acid, 1 ,3-benzenedicarboxylic acid,

2.3-pyridinedicarboxylic acid, pyridine-2, 3-dicarboxylic acid, 1 ,3-butadiene-1 ,4-dicarboxylic acid,

1.4-benzenedicarboxylic acid, p-benzenedicarboxylic acid, imidazole-2, 4-dicarboxylic acid, 2- methylquinoline-3,4-dicarboxylic acid, quinoline-2, 4-dicarboxylic acid, quinoxaline-2,3-dicarbox- ylic acid, 6-chloroquinoxaline-2, 3-dicarboxylic acid, 4,4'-diaminophenylmethane-3,3'-dicarboxylic acid, quinoline-3, 4-dicarboxylic acid, 7-chloro-4-hydroxyquinoline-2,8-dicarboxylic acid, diimide- carboxylic acid, pyridine-2, 6-dicarboxylic acid, 2-methylimidazole-4,5-dicarboxylic acid, thio- phene-3, 4-dicarboxylic acid, 2-isopropylimidazole-4,5-dicarboxylic acid, tetrahydropyrane-

4.4-dicarboxylic acid, perylene-3,9-dicarboxylic acid, perylenedicarboxylic acid, Pluriol E 200- dicarboxylic acid, 3,6-dioxaoctanedicarboxylic acid, 3,5-cyclohexadiene-1,2-dicarboxylic acid, octadicarboxylic acid, pentane-3, 3-carboxylic acid, 4, 4'-diamino-1,1 '-diphenyl-3, 3'-dicarboxylic acid, 4,4'-diaminodiphenyl-3,3'-dicarboxylic acid, benzidine-3, 3'-dicarboxylic acid, 1,4-bis(phe- nylamino)benzene-2,5-dicarboxylic acid, 1,1'-dinaphthyldicarboxylic acid, 7-chloro-8-methylquin- oline-2, 3-dicarboxylic acid, 1-anilinoanthraquinone-2,4'-dicarboxylic acid, polytetrahydrofuran 250-dicarboxylic acid, 1,4-bis(carboxymethyl)piperazine-2, 3-dicarboxylic acid, 7-chloroquino- line-3,8-dicarboxylic acid, 1-(4-carboxy)phenyl-3-(4-chloro)phenylpyrazoline-4,5-dicarbo xylic acid, 1,4, 5, 6, 7, 7-hexachloro-5-norbornene-2, 3-dicarboxylic acid, phenylindanedicarboxylic acid, 1,3-dibenzyl-2-oxoimidazolidine-4,5-dicarboxylic acid, 1 ,4-cyclohexanedicarboxylic acid, naph- thalene-1 ,8-dicarboxylic acid, 2, -benzoylbenzene-1, 3-dicarboxylic acid, 1 ,3-dibenzyl-2-oxoimid- azolidine-4,5-cis-dicarboxylic acid, 2,2'-biquinoline-4,4'-dicarboxylic acid, pyridine-3, 4-dicarbox- ylic acid, 3,6,9-trioxaundecanedicarboxylic acid, hydroxybenophenonedicarboxylic acid, Plu riol E 300-dicarboxylic acid, Pluriol E 400-dicarboxylic acid, Pluriol E 600-dicarboxylic acid, pyra- zole-3, 4-dicarboxylic acid, 2,3-pyrazinedicarboxylic acid, 5,6-dimethyl-2,3-pyrazinedicarboxylic acid, 4,4'-diamino(diphenyl ether)diimidedicarboxylic acid, 4,4'-diaminodiphenylme- thanediimidedicarboxylic acid, 4,4'-diamino(diphenyl sulfone)diimidedicarboxylic acid, 1,4-naph- thalenedicarboxylic acid, 2,6-naphthalenedicarboxylic acid, 1 ,3-adamantanedicarboxylic acid,

1.8-naphthalenedicarboxylic acid, 2,3-naphthalenedicarboxylic acid, 8-methoxy-2,3-naphtha- lenedicarboxylic acid, 8-nitro-2,3-naphthalenecarboxylic acid, 8-sulfo-2,3-naphthalenedicarbox- ylic acid, anthracene-2, 3-dicarboxylic acid, 2',3'-diphenyl-p-terphenyl-4,4"-dicarboxylic acid, (di phenyl ether)-4,4'-dicarboxylic acid, imidazole-4, 5-dicarboxylic acid, 4(1H)-oxothiochromene-

2.8-dicarboxylic acid, 5-tert-butyl-1 ,3-benzenedicarboxylic acid, 7,8-quinolinedicarboxylic acid,

4.5-imidazoledicarboxylic acid, 4-cyclohexene-1 ,2-dicarboxylic acid, hexatriacontanedicarbox- ylic acid, tetradecanedicarboxylic acid, 1 ,7-heptadicarboxylic acid, 5-hydroxy-1 ,3-benzenedicar- boxylic acid, 2, 5-dihydroxy-1 ,4-dicarboxylic acid, pyrazine-2, 3-dicarboxylic acid, furan-2,5-dicar- boxylic acid, 1-nonene-6,9-dicarboxylic acid, eicosenedicarboxylic acid, 4,4'-dihydroxydiphenyl- methane-3,3'-dicarboxylic acid, 1 -amino-4-methyl-9, 10-dioxo-9, 10-dihydroanthracene-2,3-dicar- boxylic acid, 2,5-pyridinedicarboxylic acid, cyclohexene-2, 3-dicarboxylic acid, 2,9-dichloro- fluorubin-4,11-dicarboxylic acid, 7-chloro-3-methylquinoline-6,8-dicarboxylic acid, 2,4-dichloro- benzophenone-2',5'-dicarboxylic acid, 1 ,3-benzenedicarboxylic acid, 2,6-pyridinedicarboxylic acid, 1-methylpyrrole-3,4-dicarboxylic acid, 1 -benzyl-1 H-pyrrole-3,4-dicarboxylic acid, anthraqui- none-1 ,5-dicarboxylic acid, 3,5-pyrazoledicarboxylic acid, 2-nitrobenzene-1 ,4-dicarboxylic acid, heptane-1 ,7-dicarboxylic acid, cyclobutane-1 , 1-dicarboxylic acid, 1,14-tetradecanedicarboxylic acid, 5,-6-dehydronorbornane-2,3-dicarboxylic acid, 5-ethyl-2,3-pyridinedicarboxylic acid or camphordicarboxylic acid.

For example, the at least bidentate organic compound can be derived from a tricarboxylic acid that already has at least one isocyanate reactive functional group or that can serve as starting material for the preparation of a tricarboxylic acid by derivatization. Examples of tricarboxylic ac ids are

2-hydroxy-1 ,2,3-propanetricarboxylic acid, 7-chloro-2,3,8-quinolinetricarboxylic acid, 1,2,3-,

1.2.4-benzenetricarboxylic acid, 1,2,4-butanetricarboxylic acid, 2-phosphono-1 ,2,4-butanetricar- boxylic acid, 1,3,5-benzenetricarboxylic acid, 1 -hydroxy-1 , 2, 3-propanetricarboxylic acid, 4,5-di- hydro-4,5-dioxo-1 H-pyrrolo[2,3-F]quinoline-2,7,9-tricarboxylic acid, 5-acetyl-3-amino- 6-methylbenzene-1 ,2,4-tricarboxylic acid, 3-amino-5-benzoyl-6-methylbenzene-1 ,2,4-tricarbox- ylic acid, 1,2, 3-propanetricarboxylic acid or aurintricarboxylic acid.

Examples of an at least bidentate organic compound derived from a tetracarboxylic acid that can serve as starting material for the preparation of a tetracarboxylic acid by derivatization, are

1 ,1-dioxidoperylo[1,12-BCD]thiophene-3,4,9,10-tetracarboxylic acid, perylenetetracarboxylic ac ids such as perylene-3,4,9,10-tetracarboxylic acid or (perylene 1,12-sulfone)-3, 4,9,10-tetracar- boxylic acid, butanetetracarboxylic acids such as 1,2,3,4-butanetetracarboxylic acid or meso-

1.2.3.4-butanetetracarboxylic acid, decane-2, 4, 6, 8-tetracarboxylic acid, 1 ,4,7,10,13,16-hexao- xacyclooctadecane-2,3,11 ,12-tetracarboxylic acid, 1 ,2,4,5-benzenetetracarboxylic acid,

1 ,2,11,12-dodecanetetracarboxylic acid, 1,2,5,6-hexanetetracarboxylic acid, 1,2,7,8-oc- tanetetracarboxylic acid, 1,4,5,8-naphthalenetetracarboxylic acid, 1 ,2,9,10-decanetetracarbox- ylic acid, benzophenonetetracarboxylic acid, 3,3',4,4'-benzophenonetetracarboxylic acid, tetra- hydrofurantetracarboxylic acid or cyclopentanetetracarboxylic acids such as cyclopentane-

1.2.3.4-tetracarboxylic acid.

Very particular preference is given to at least monosubstituted aromatic dicarboxylic, tricarbox ylic or tetracarboxylic acids having one, two, three, four or more rings, with each of the rings be ing able to comprise at least one heteroatom and two or more rings being able to comprise identical or different heteroatoms. For example, preference is given to one-ring dicarboxylic ac ids, one-ring tricarboxylic acids, one-ring tetracarboxylic acids, two-ring dicarboxylic acids, two- ring tricarboxylic acids, two-ring tetracarboxylic acids, three-ring dicarboxylic acids, three-ring tricarboxylic acids, three-ring tetracarboxylic acids, four-ring dicarboxylic acids, four-ring tricar boxylic acids and/or four-ring tetracarboxylic acids. Suitable heteroatoms are, for example, N,

O, S, B, P, and preferred heteroatoms are N, S and/or O. Suitable substituents are those isocy anate reactive functional groups mentioned above. Especially preferred is metal-organic framework material, wherein the at least bidentate organic compound is an at least monoaminosubstituted aromatic dicarboxylic acid selected from the group consisting of terephthalic acid, 2,6-naphthalenedicarboxylic acid, 1 ,4-naphthalenedicar- boxylic acid, 1 ,5-naphthalenedicarboxylic acid and derivatives thereof in which at least one CH group in the ring is replaced by nitrogen, wherein the framework in powder form preferably has a specific surface area determined by the Langmuir method (N2, 77 K) of at least 2500 m ² /g. Such MOFs are described in WO 2008/142059 A1.

In a particularly preferred embodiment the at least one at least bidentate organic compound is derived from an amino polycarboxylic acid, preferably derived from an amino dicarboxylic acid, even more preferably derived from 2-aminoterephthalic acid.

Apart from these at least bidentate organic compounds, the metal-organic framework can also comprise one or more monodentate ligands.

For the purposes of the present invention, the term "derived" means that the at least one at least bidentate organic compound is present in partially or completely deprotonated form. For the purposes of the present invention, the term "derived" also means that the carboxylic acid function can be present as a sulfur analogue. Sulfur analogues are -C(=0)SH and also its tauto mer and -C(S)SFI.

Suitable solvents for preparing the metal-organic framework are, inter alia, ethanol, dimethylfor- mamide, toluene, methanol, chlorobenzene, diethylformamide, dimethyl sulfoxide, water, hydro gen peroxide, methylamine, sodium hydroxide solution, N-methylpyrrolidone ether, acetonitrile, benzyl chloride, triethylamine, ethylene glycol and mixtures thereof. Further metal ions, at least bidentate organic compounds and solvents for the preparation of MOFs are described, inter alia, in US-A 5,648,508 or DE-A 101 11 230.

The pore size of the metal-organic framework can be controlled by selection of the appropriate ligand and/or the at least bidentate organic compound. In general, the larger the organic com pound, the larger the pore size. The pore size is preferably from 0.2 nm to 30 nm, particularly preferably in the range from 0.3 nm to 9 nm, based on the crystalline material.

Flowever, larger pores whose size distribution can vary also occur in a shaped body comprising a metal-organic framework. Preference is, however, given to more than 50% of the total pore volume, in particular more than 75%, being made up by pores having a pore diameter of up to 1000 mm. Flowever, preference is given to a major part of the pore volume being made up by pores having two diameter ranges. It is therefore preferred for more than 25% of the total pore volume, in particular more than 50% of the total pore volume, to be made up by pores which have a diameter in the range from 100 nm to 800 nm and more than 15% of the total pore vol ume, in particular more than 25% of the total pore volume, to be made up by pores which have a diameter up to 10 nm. The pore distribution can be determined by means of mercury porosim- etry. Examples of metal-organic frameworks that already has at least one isocyanate reactive func tional group or that can serve as starting material for the preparation of a metal-organic frame work material by derivatization are given below. The designation of the framework, the metal and the at least bidentate ligand and also the solvent and the cell parameters (angles a, b and y and the dimensions A, B and C in A) are indicated. The latter were determined by X-ray diffrac tion.

ADC Acetylenedicarboxylic acid

NDC Naphthalenedicarboxylic acid BDC Benzenedicarboxylic acid

ATC Adamantanetetracarboxylic acid BTC Benzenetricarboxylic acid

BTB Benzenetribenzoic acid

MTB Methanetetrabenzoic acid

ATB Adamantanetetrabenzoic acid

ADB Adamantanedibenzoic acid

Further metal-organic frameworks are MOF-2 to 4, MOF-9, MOF-31 to 36, MOF-39, MOF-69 to 80, MOF103 to 106, MOF-122, MOF-125, MOF-150, MOF-177, MOF-178, MOF-235, MOF-236, MOF-500, MOF-501, MOF-502, MOF-505, IRMOF-1, iRMOF-61, IRMOP-13, IRMOP-51, MIL- 17, MIL-45, MIL-47, MIL-53, MIL-59, MIL-60, MIL-61, MIL-63, MIL-68, MIL-79, MIL-80, MIL-83, MIL-85, CPL-1 to 2, SZL-1, which are described in the literature.

Particularly preferred metal-organic frameworks are MIL-53, Zn-tBu-isophthalic acid, AI-BDC, MOF-5, MOF-177, MOF-505, IRMOF-8, IRMOF-11 , Cu-BTC, AI-NDC, AI-aminoBDC, Cu-BDC- TEDA, Zn-BDC-TEDA, AI-BTC, Cu-BTC, AI-NDC, Mg-NDC, Al-fumarate, Zn-2-methylimidazo- late, Zn-2-aminoimidazolate, Cu-biphenyldicarboxylate-TEDA, MOF-74, Cu-BPP, Sc-tereph- thalate. Greater preference is given to Sc-terephthalate, Cu-BTC, AI-BDC, AI-aminoBDC and AI- BTC Very particular preference is given to AI-aminoBDC.

Al-amino BDC (AI-2-aminoterephthalic acid MOF) can be prepared according to WO 2008/142059 A1.

Apart from the conventional method of preparing the MOFs, as described, for example, in US 5,648,508, these can also be prepared by an electrochemical route. In this respect, refer ence is made to DE-A 10355087 and WO-A 2005/049892. The metal-organic frameworks pre pared in this way have particularly good properties with regard to the adsorption and desorption of chemical substances, in particular gases.

Regardless of the method of preparation, the metal-organic framework is generally obtained in pulverulent or crystalline form. The metal-organic framework can also be converted into a shaped body and used in this form according to the present invention.

The contacting of the polyurethane prepolymer with the porous material can be carried out by simple mixing. No particular requirements are associated with the contacting. The porous mate rial can be dried before contacting. Preferably, conditions for allowing chemical reaction with the residual monomeric isocyanate are standard conditions, i.e no elevated pressure, stirring or shaking and room temperature or elevated temperatures. Thus, it is known that amino groups spontaneously react with the isocyanate functional group to yield a urea group. The polyurethane prepolymer according to the present invention has the same or very similar characteristics properties as the prepolymer before contacting with the porous material and can be used in the same fields mentioned above.

However, it is also possible to remove the porous material after contacting by separation, e.g. filtration. Optionally, a second and further contacting with porous material after separation is possible in order to further remove residual monomeric isocyanate.

The following examples further illustrate the invention

EXAMPLES

1. Raw materials

Isocyanate prepolymer 1 :

The prepolymer was prepared by charging 261 g of toluene diisocyanate (TDI) with a ratio of 2,4-TDI:2,6-TDI=80:20 and 0.1 g Diglycol-bis-chloroformiat (DIBIS) into a stirred four-necked flask under nitrogen blanket, heating to 60 °C and slowly adding 739 g of poly(tetramethylene ether glycol) with an OH value of 112 mg KOH/g. The reaction mixture was stirred for 2 hours at 80 °C. After cooling down to room temperature, the isocyanate prepolymer was stored at room temperature in a sealed PE bottle free of moisture. NCO content was 6.09%, free monomer content was 0.4% 2,4-TDI and 2.1% 2,6-TDI and the viscosity was determined as 11.4 Pas at 25 °C.

Isocyanate prepolymer 2:

The prepolymer was prepared by charging 320 g of methylene diphenyl diisocyanate (MDI) with a ratio of 4,4’-MDI:2,4’-MDI:2,2’-MDI=1:1:0.05 and 0.1 g Diglycol-bis-chloroformiat (DIBIS) into a stirred four-necked flask under nitrogen blanket, heating to 60 °C and adding 679.9 g of polypropylene glycol) with an OH value of 104 mg KOH/g. The reaction mixture was stirred for 2 hours at 80 °C. After cooling down to room temperature, the isocyanate prepolymer was stored at room temperature in a sealed PE bottle free of moisture. NCO content was 5.27%, free monomer content was 2.1% 4,4’-MDI, 4.7% 2,4’-MDI and 0.4% 2,2’-MDI and the viscosity was determined as 2.8 Pas at 60 °C.

Basolite A 100:

Metal-organic framework (MOF) based of aluminum terephthalate with MIL-53 structure from BASF.

Basolite A 120:

Metal-organic framework (MOF) based of aluminum 2-aminoterephthalate prepared according to example 1 of WO 2008/142059 A1 . Aerosil R 504:

Fumed silica from EVONIK with (3-aminopropyl)trimethoxysilane surface functionalization and 125-175 m ² /g BET surface area.

Omyacarb 2T-AV:

Fine chalk powder from OMYA, composition is 97,5% calcium carbonate and <2% magnesium carbonate.

2-Ethyl-1-hexanol: Purity >99% from Sigma-Aldrich.

Purolite A110:

Ion exchange resin from PUROLITE based on spherical beads (300-1200 pm) of microporous polystyrene crosslinked with divinylbenzene. Surface functionalized with primary amines.

Lewatit VP OC 1065:

Ion exchange resin from LANXESS based on a microporous polystyrene crosslinked with divi nylbenzene in spherical bead form (300-1200 pm). Surface functionalized with benzylamine groups. 50 m ² /g BET surface.

Aerosil VPR 511:

Fumed silica from EVONIK with (3-aminopropyl)trimethoxysilane surface functionalization, 125- 175 m ² /g BET surface area.

Mg-Dihydroxyterephthalate:

12 g of 2,5-dihydroxyterephthalic acid has been dissolved in 685 g N,N-dimethylformamide. To this solution 53.3 g magnesiumacetate-tetrahydrate have been added. The solution has been stirred for 2 hours at 20 °C. The solid was filtered off and washed with 150 ml N,N-dimethylfor- mamide and 150 ml methanol, followed by 16 hours of hot extraction with methanol. The mate rial was dried at 130°C for 16 hours. The BET surface area was determined with nitrogen ad sorption and was found to be 1126 m ² /g.

Mg-Flydroxyterephthalate:

10 g of 2-hydroxyterephthalic acid has been dissolved in 634 g N,N-dimethylformamide. To this solution 49.3 g magnesiumacetate-tetrahydrate have been added. The solution has been stirred for 2 hours at 20 °C. The solid was filtered off and washed with 100 ml N,N-dimethylformamide and 100 ml methanol, followed by 16 hours of hot extraction with methanol. The material was dried at 130°C for 16 hours. The BET surface area was determined with nitrogen adsorption and was found to be 45.5 m ² /g.

Al-Dihydroxyterephthalate:

12.24 g of 2,5-dihydroxyterephthalic acid has been dissolved in 698.5 g N,N-dimethylforma- mide. To this solution 39.2 g basic aluminum-diacetate have been added. The solution has been stirred for 2 hours at 20 °C. The solid was filtered off and washed with 150 ml N,N-dime- thylformamide and 150 ml methanol, followed by hot extraction with methanol for 16 hours. The material was dried at 130°C for 16 hours. The BET surface area was determined with nitrogen adsorption and was found to be 364 m ² /g.

Al-Hydroxyterphthalate:

9.5 g of 2-hydroxyterephthalic acid has been dissolved in 600 g N,N-dimethylformamide. To this solution 33.8 g basic aluminum-diacetate have been added. The solution has been stirred for 2 hours at 20 °C. The solid was filtered off and washed with 100 ml N,N-dimethylformamide and 100 ml methanol, followed by 16 hours of hot extraction with methanol. The material was dried at 130°C for 16 hours. The BET surface area was determined with nitrogen adsorption and was found to be 332 m ² /g

2. Analytical methods

The NCO content of prepolymers and prepolymer/absorbent mixtures was determined by back- titration of the respective samples derivatized with 1 molar n-butylamine solution in chloroben zene using 1 molar hydrochloric acid.

The free isocyanate monomer content of prepolymers and prepolymer/absorbent mixtures was measured using high performance liquid chromatography (HPLC) with UV detection of samples derivatized with 1-(2-Piridyl)piperazine This method was applied for MDI and TDI monomer de termination.

The viscosity was determined with a Haake-Mars rheometer with plate-plate geometry in rota tion and 1 mm gap width at a shear rate of 10 and 40 S ¹ at the given temperature.

3. Working Examples

All absorbents were dried under vacuo at 80 °C overnight before use. Lewatit VPOC 1065, Purolite A110 and Aerosil VPR 511 were dried under vacuo at 80 °C for an extended time of 3 days. The residual content of volatiles (mainly water) was determined gravimetrically with Sarto- rius MA30 moisture analyzed by heating the samples for 10 min at 120 °C. Residual moisture was 1.7% for Basolite A100, 2.6% for Basolite A120, 1.3% for Aerosil R 504, 0.1% for Om- yacarb 2T-AV, 0.6% for Purolite A110, 0,8% for Lewatit VPOC 1065, 1.1% for Aerosil VPR 511 , 4.0% for Mg-DHT, 4.3% for Mg-HT, 1.1% for AI-DHT and 1.8% for AI-HT. After drying the absor bents were directly used for the prepolymer/absorbent mixtures.

Typical preparation procedure: 47.5 g of isocyanate prepolymer was charged into a PE cup, closed with a lid and heated to 60 °C in a laboratory heating oven. 2.5 g of dried absorbent was added and homogenized with a Vollrath laboratory mixer. The mixtures with isocyanate prepoly mer 1 were stored at 60 °C for 1 hour, those with isocyanate prepolymer 2 at 60 °C for 2 hours. After the thermal annealing the samples were stored in sealed glass vials at room temperature for another 24 hours. NCO content, viscosity and monomer content of the mixtures was deter mined. The examples 1-12 were prepared following the above mentioned process and demonstrate the individual ability of TDI monomer capture for various absorbents. As shown in Table 1 the NCO values of the examples 1-12 decrease in the mixtures, from 6.09% of the untreated isocyanate prepolymer 1 to 4.47% as minimum. The initial TDI monomer content of 2.5% was reduced in all examples 1-12, however, only example 2 containing Basolite A 120 achieved a monomer con tent as low as 0.05%. This corresponds to a capture of 98% of the free TDI monomers and is significantly improved compared to the examples 1 and 3-12. At the same time the viscosity in creased only moderately in example 2 from initially 11.4 (20 °C) Pas to 22.7 Pas (20 °C). The best performing comparison example 8, which achieved a TDI monomer content of 0.72%, ex- hibits a viscosity of 54.5 Pas (20 °C). These results demonstrate that Basolite A 120 very effi ciently captures the TDI monomers to yield prepolymer mixtures with lower than 0,1% residual monomer while keeping the viscosity increase on a moderate level. Table 1. Examples 1-12 using isocyanate prepolymer 1 based on TDI.

^* ) comparative example The same absorbents were tested in examples 13-24 with the MDI based isocyanate prepoly mer 2 having a NCO value of 5.27% and a residual MDI monomer content of 7.2%. The NCO content could be reduced to 4.16% and residual MDI monomer content of 2.5% in example 14 which contains Basolite A 120; the performance of the other absorbents in example 13 and 15- 24 was worse. These examples demonstrate that Basolite A 120 in example 14 has again the highest efficiency to capture MDI monomers which is in analogy to the TDI prepolymer exam ples 1-12. Table 2. Examples 13-24 using isocyanate prepolymer 2 based on MDL

^* ) comparative example Additionally to the MOF type absorbents the monomer removal using zeolites was also tested with isocyanate prepolymer 1 and isocyanate prepolymer 2.

Description of the raw materials:

Zeolite MU 0169: Deboronated beta, 42% Si / 0,05% B, BET 488 m ² /g

Zeolite DY 43: HY, 718 m2/g

Zeolite CBV 100: NaY, Si0 ₂ :AI ₂ 0 ₃ =5, 727 m ² /g

Zeolite CBV 760: HY, SiO ₂ :AI ₂ O ₃ =60, 720 g/m ²

All zeolites were dried under vacuum at 80 °C overnight before use. After drying the absorbents were directly used for the prepolymer/absorbent mixtures. Typical preparation procedure: 47.5 g of isocyanate prepolymer 1 or 2 was charged into a PE cup, closed with a lid and heated to 60 °C in a laboratory heating oven. 2.5 g of dried absorbent was added and homogenized with a Vollrath laboratory mixer. The samples were filled into airtight glass vials and annealed as fol lows. Example 25 and 26 were annealed after 1 day for 3 hours at 60 °C and then stored for 3 days at room temperature before analysis. Example 27 and 28 were stored at 60 °C for 1 hour, then kept at room temperature for 6 days and additionally annealed for 2 hours at 60 °C, those with isocyanate prepolymer 2 at 60 °C for 2 hours. Example 29 and 30 were stored at room temperature for 14 days. Example 31 and 32 were stored at 60 °C for 1 hour, then kept at room temperature for 6 days and additionally annealed for 2 hours at 60 °C. NCO content was deter mined by titration, viscosity measured with a Brookfield viscosimeter with cone-plate geometry and monomer content was determined with a HPLC method as described earlier.

The results in Table 3 and 4 clearly demonstrate that the ability of the zeolites to capture the free isocyanate monomer from prepolymers is relatively low compared to the Basolite A 120 in example 2 and 14.

For some cases, e.g. example 27, 28, 31 and 32, the monomer content was not even deter mined since the measured NCO content of the mixture was so close to the theoretical NCO of the plain mixture. As the Basolite references show the drop of NCO content is an essential indi cator for the removal of the monomeric isocyanate.

Furthermore, in Example 29 with Basolite A 120 and the MDI prepolymer 1 the monomer re moval even takes place also at room temperature granting 14 days of storage time. No such re sults were obtained with zeolites even not at thermal annealing at 60 °C for 3 hours.

Table 3. Examples 25-28 using zeolites and isocyanate prepolymer 1 based on TDL

^* ) Comparative example

Table 4. Examples 29-32 using zeolites isocyanate prepolymer 2 based on MDL

^* ) comparative example

4. Application tests in PU hot cast elastomers

The demonomerized isocyanate prepolymer 1 was prepared following the above described pro cess in two mixing ratios: 95 wt% isocyanate prepolymer 1 with 5 wt% Basolite A120 and 97 wt% isocyanate prepolymer 1 with 3 wt% Basolite A 120. All three prepolymers including the un- treated isocyanate prepolymer 1 were heated to 80 °C in a laboratory oven, the curing agent 3,5-Dimethylthio-toluenediamine was used at room temperature. Both components were charged in the given weight ratio into a PE container and homogenized using a SpeedMixer™ under vacuum for 20 sec at 1820 rpm. The reaction mixture was then poured into a preheated aluminum mold at 90 °C and post-cured for 24 hours at 90 °C. Mechanical testing included Shore A and D hardness (DIN ISO 7619-1), tensile strength and elongation at break with S2 test specimen (DIN 53504), tear strength with Graves geometry (DIN ISO 34-1 , B), E modulus with S2 test specimen, compression set with 10% compression (DIN ISO 815-1) and abrasion (DIN ISO 4649). The mechanical properties of the obtained hot cast elastomers are shown in Table 5. The me chanical performance of the elastomers with isocyanate prepolymer 1 with <0.1% TDI (example 34) or 0.3% TDI (example 35) remains below the reference (example 33) since the monomer was captured by the Basolite A 120 scavenger. The absence of isocyanate monomers leads to the situation that no hard segments can be formed which typically are strongly influencing the final mechanical properties in polyurethane elastomers. However, this observation is well known for monomer-free prepolymers used for polyurethane elastomers independent of the method of demonomehzation. The examples 34-35 illustrate that prepolymers which were demonomehzed with Basolite A 120 can be processed and used for hot cast elastomer applications. Table 5. Polyurethane hot cast elastomers.