Patent Application
20180244888
The present invention relates to a process for preparing a porous material, at least comprising the steps of providing a mixture (I) comprising a composition (A) at least comprising an isocyanate composition (A*) comprising a polymeric polyfunctional isocyanate as component (ai), a monomeric polyfunctional isocyanate as component (aii), at least one catalyst as component (ac), wherein composition (A) is substantially free of aromatic amines, and a solvent (B), reacting the components in the composition (A) obtaining an organic gel, and drying of the gel obtained in step b). The invention further relates to the porous materials which can be obtained in this way and the use of the porous materials as thermal insulation material and in vacuum insulation panels.
Porous materials, for example polymer foams, having pores in the size range of a few microns or significantly below and a high porosity of at least 70% are particularly good thermal insulators on the basis of theoretical considerations.
Such porous materials having a small average pore diameter can be, for example, in the form of organic aerogels or xerogels which are produced with a sol-gel process and subsequent drying. In the sol-gel process, a sol based on a reactive organic gel precursor is first produced and the sol is then gelled by means of a crosslinking reaction to form a gel. To obtain a porous material, for example an aerogel, from the gel, the liquid has to be removed. This step will hereinafter be referred to as drying in the interests of simplicity.
WO 95/02009 discloses isocyanate-based xerogels which are particularly suitable for applications in the field of vacuum insulation. The publication also discloses a sol-gel-based process for producing the xerogels, in which known, inter alia aromatic, polymeric isocyanates and an unreactive solvent are used. As further compounds having active hydrogen atoms, use is made of aliphatic or aromatic polyamines or polyols. The examples disclosed in the publication comprise ones in which a polyisocyanate is reacted with diaminodiethyltoluene. The xerogels disclosed generally have average pore sizes in the region of 50 μm. In one example, mention is made of an average pore diameter of 10 μm.
WO 2011/069959, WO 2012/000917 and WO 2012/059388 describe porous materials based on polymeric polyfunctional isocyanates and polyfunctional aromatic amines, where the amine component comprises polyfunctional substituted aromatic amines. The porous materials described are produced by reacting isocyanates with the desired amount of amine in a solvent which is inert toward the isocyanates. The use of catalysts is known from WO 2012/000917 and WO 2012/059388.
Aerogels and xerogels based on polymeric isocyanates and other compounds with isocyanate-reactive groups are also known from the state of the art. For example WO 95/03358 A1 discloses organic aerogels, in particular polyisocyanate based aerogels and to methods for their preparation. Also WO 98/44013 A1 and WO 98/44028 disclose gels based on organic polymeric isocyanates by trimerization in the presence of compounds containing an isocyanate-reactive group. WO 00/32663 discloses aerogels based on organic polymeric polyisocyanates and a carbodiimide catalyst and optionally a polyfunctional isocyanate-reactive compound. The shrinkage of the aerogels after supercritical drying is greater than 65%.
The preparation of aerogels based on organic polymeric polyisocyanates and isocyanate trimerisation catalysts without isocyanate-reactive compounds has also been described in the state of the art. In WO 98/37539 A1, a process is disclosed which results in a material with a shrinkage of >65% even after supercritical drying. For example WO 96/37539 A1 discloses aerogels based on organic polymeric polyisocyanates and isocyanate trimerisation catalysts. The aerogels disclosed display densities of >300 kg/m3 (WO 96/37539 A1). Only by using graphite as an additive, the shrinkage and thereby density could be reduced. Similarly the aerogels disclosed in WO 00/32663 show densities of >250 kg/m3, even with an optimized catalyst system.
However, the materials properties, in particular the mechanical stability and/or the compressive strength and also the thermal conductivity, of the known porous materials based on polyurea are not satisfactory for all applications. In particular, the thermal conductivities in the ventilated state are not sufficiently low. In the case of open-cell materials, the ventilated state is the state under ambient pressure of air, whereas in the case of partially or completely closed-cell materials such as rigid polyurethane foams this state is reached only after aging, after the cell gas has gradually been completely replaced.
A particular problem associated with the formulations based on isocyanates and amines which are known from the prior art are mixing defects. Mixing defects occur as a result of the high reaction rate between isocyanates and amino groups, since the gelling reaction has already proceeded a long way before complete mixing. Mixing defects lead to porous materials having heterogeneous and unsatisfactory materials properties.
Another disadvantage of known porous materials is often the high water uptake which results in an increased thermal conductivity, i.e. reduces the insulating properties of the material.
It was therefore an object of the invention to avoid the abovementioned disadvantages. In particular, a porous material which does not have the abovementioned disadvantages, or has them to a reduced extent, should be provided. The porous materials should have a low thermal conductivity in the ventilated state, i.e. at atmospheric pressure. Furthermore, the porous material should at the same time have a high porosity, a low density and a sufficiently high mechanical stability.
According to the present invention, this object is solved by a process for preparing a porous material, at least comprising the steps of:
According to the process of the present invention, it was surprisingly found, that only by blending polymeric isocyanate with monomeric isocyanate it is possible to prepare porous materials based on polyfunctional polymeric and monomeric isocyanates and an isocyanate trimerisation catalyst, with reduced shrinkage and density.
The porous materials of the present invention are preferably aerogels or xerogels.
Preferred embodiments may be found in the claims and the description. Combinations of preferred embodiments do not go outside the scope of the present invention. Preferred embodiments of the components used are described below.
According to the present invention, in the process for preparing a porous material a mixture (I) comprising a composition (A) comprising components suitable to form an organic gel and a solvent (B) is provided in step a). Composition (A) comprises an isocyanate composition (A*) comprising a polymeric polyfunctional isocyanate as component (ai), a monomeric polyfunctional isocyanate as component (aii). Furthermore, composition (A) comprises at least one catalyst as component (ac) and is substantially free of aromatic amines. According to step b) the components in composition (A) are reacted in the presence of the solvent (B) to form a gel. The gel is then dried according to step c) of the process of the present invention.
The process as disclosed above results in porous materials with improved properties, in particular improved thermal conductivity and reduced shrinkage as well as densities upon supercritical drying.
The composition (A) may be any composition comprising components suitable to form an organic gel which comprises an isocyanate composition (A*) comprising a polymeric polyfunctional isocyanate as component (ai), a monomeric polyfunctional isocyanate as component (aii), and at least one catalyst as component (ac) and is substantially free of aromatic amines. Composition (A) may also comprise further components.
In the context of the present invention, substantially free of aromatic amines means that the composition (A) comprises less than 1% by weight of aromatic amines, preferably less than 0.5% by weight of aromatic amines.
The isocyanate composition (A*) comprises a polymeric polyfunctional isocyanate as component (ai) and a monomeric polyfunctional isocyanate as component (aii).
In the context of the present invention, the term polymeric polyfunctional isocyanate also encompasses oligomeric polyfunctional isocyanates.
The ratio of the components (ai) and (aii) in composition (A*) may vary in broad ranges. Generally, composition (A*) comprises component (ai) in an amount of from 84 to 27% by weight. Preferably, composition (A*) comprises component (aii) in an amount of from 16 to 73% by weight. Preferred, composition (A*) comprises component (ai) in an amount of from 81 to 30% by weight and component (aii) in an amount of from 19 to 70% by weight. Most preferred, composition (A*) comprises component (ai) in an amount of from 78 to 33% by weight and component (aii) in an amount of from 22 to 67% by weight, where the % by weight of the components (ai) and (aii) in composition (A*) add up to 100% by weight.
According to a further embodiment, the present invention thus is directed to the process for preparing a porous material as disclosed above, wherein composition (A*) comprises component (ai) in an amount of from 84 to 27% by weight and component (aii) in an amount of from 16 to 73% by weight.
Composition (A) may also comprise further components, such as components which react with the polyfunctional isocyanate, in particular one or more further catalysts.
It has surprisingly been found that stable aerogels and xerogels can be obtained using a gel composition which comprises at least one polyfunctional isocyanate and a monool as building blocks without the use of further components such as for example aromatic amines. According to the present invention, the composition (A) is substantially free of aromatic amines.
Preferably, the composition (A) is further substantially free of monools. In the context of the present invention, substantially free of monool means that the composition (A) comprises less than 1% by weight of monool, preferably less than 0.5% by weight of monool.
According to a further embodiment, the present invention therefore is directed to the process for preparing a porous material as disclosed above, wherein the composition (A) is substantially free of monool.
The polymeric polyfunctional isocyanates (ai) will hereinafter be referred to collectively as component (ai). It will be obvious to a person skilled in the art that the monomer components mentioned are present in reacted form in the porous material.
For the purposes of the present invention, the functionality of a compound is the number of reactive groups per molecule. In the case of the monomer component (ai), the functionality is the number of isocyanate groups per molecule. A polyfunctional compound has a functionality of at least 2.
If mixtures of compounds having different functionalities are used as component (ai), the functionality of the components is in each case given by the number average of the functionality of the individual compounds. A polyfunctional compound comprises at least two of the abovementioned functional groups per molecule.
For the purposes of the present invention, a xerogel is a porous material which has been produced by a sol-gel process in which the liquid phase has been removed from the gel by drying below the critical temperature and below the critical pressure of the liquid phase (“subcritical conditions”). An aerogel is a porous material which has been produced by a sol-gel process in which the liquid phase has been removed from the gel under supercritical conditions.
Composition (A) can further comprise small amounts of water. In a particularly preferred embodiment, water is not used. If water is present in the composition (A), the preferred amount of water is at most 1% by weight, in particular at most 0.9% by weight, particularly preferably at most 0.8% by weight, in particular at most 0.75% by weight, very particularly preferably at most 0.5% by weight, in particular at most 0.25% by weight, in each case based on the total weight of the composition (A), which is 100% by weight.
According to a further embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein no water is used.
According to an alternative further embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein the composition (A) comprises less than 1% by weight of water.
Composition (A) comprises components suitable to form an organic gel in suitable amounts.
According to a further embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein composition (A) comprises
in each case based on the total weight of the composition (A), where the % by weight of the components of the composition (A) add up to 100% by weight.
Within the abovementioned preferred ranges, the resulting gels are particularly stable and do not shrink or shrink only slightly in the subsequent drying step.
Component (ai)
In the process of the invention, at least one polymeric polyfunctional isocyanate is reacted as component (ai).
Preferably the amount of component (ai) used is at least 27% by weight, in particular at least 30% by weight, more preferable at least 33% by weight, particularly preferably at least 36% by weight. Preferably the amount of component (ai) used is at most 84% by weight, in particular at most 81% by weight, particularly preferably at most 78% by weight, especially at most 75% by weight, in each case based on the total weight of the composition (A*).
Possible polymeric polyfunctional isocyanates are aromatic, aliphatic, cycloaliphatic and/or araliphatic isocyanates. Such polyfunctional isocyanates are known per se or can be prepared by methods known per se. The polyfunctional isocyanates can also be used, in particular, as mixtures, so that the component (ai) in this case comprises various polymeric polyfunctional isocyanates. Polyfunctional isocyanates which are possible as building blocks (ai) have two (hereinafter referred to as diisocyanates) or more than two isocyanate groups per molecule of each component.
As polymeric polyfunctional isocyanates (ai), preference is given to aromatic isocyanates. Particularly preferred polyfunctional isocyanates of the component (ai) are the following embodiments:
i) polymeric polyfunctional isocyanates based on tolylene diisocyanate (TDI), in particular 2,4-TDI or 2,6-TDI or mixtures of 2,4- and 2,6-TDI;
ii) polymeric polyfunctional isocyanates based on diphenylmethane diisocyanate (MDI), in particular oligomeric MDI, also referred to as polyphenylpolymethylene isocyanate, or crude MDI which is obtained in the production of MDI or mixtures of at least one oligomer of MDI and at least one of the abovementioned low molecular weight MDI derivatives.
According to a further embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein an mixture of polymeric isocyanates is used as component (ai).
Oligomeric diphenylmethane diisocyanate is particularly preferred as polymeric polyfunctional isocyanate. Oligomeric diphenylmethane diisocyanate (hereinafter referred to as oligomeric MDI) is an oligomeric condensation product or a mixture of a plurality of oligomeric condensation products and thus a derivative/derivatives of diphenylmethane diisocyanate (MDI).
Oligomeric MDI comprises one or more condensation products of MDI which have a plurality of aromatic rings and a functionality of more than 2, in particular 3 or 4 or 5. Oligomeric MDI is known and is frequently referred to as polyphenylpolymethylene isocyanate or as polymeric MDI. Oligomeric MDI is usually made up of a mixture of MDI-based isocyanates having various functionalities. Oligomeric MDI is usually used in admixture with monomeric MDI.
The (average) functionality of an isocyanate comprising oligomeric MDI can vary in the range from about 2.2 to about 5, in particular from 2.3 to 3.5, in particular from 2.4 to 3. Such a mixture of MDI-based polyfunctional isocyanates having various functionalities is, in particular, crude MDI which is obtained in the production of MDI.
Polyfunctional isocyanates or mixtures of a plurality of polyfunctional isocyanates based on MDI are known and are marketed, for example, by BASF Polyurethanes GmbH under the name Lupranat®.
Thus, according to a further embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein component (ai) is selected from polymeric polyfunctional isocyanates based on diphenylmethane diisocyanate (MDI) and component (aii) is selected from monomeric diphenylmethane diisocyanate (MDI).
The functionality of the component (ai) is preferably at least two, in particular at least 2.2 and particularly preferably at least 2.4. The functionality of the component (ai) is preferably from 2.2 to 4 and particularly preferably from 2.4 to 3.
The viscosity of the component (ai) used can vary within a wide range. The component (ai) preferably has a viscosity of from 20 to 3000 mPa·s, particularly preferably from 60 to 2500 mPa·s.
The components (ai), (aii) and (ac) will hereinafter be referred to collectively as organic gel precursor (A′). It will be obvious to a person skilled in the art that the partial reaction of the component (ai), (aii) and (ac) leads to the actual gel precursor (A′) which is subsequently converted into a gel.
Component (aii)
In the process of the invention, at least one monomeric polyfunctional isocyanate is reacted as component (aii).
Preferably the amount of component (aii) used is at least 16% by weight, in particular at least 19% by weight, more preferable at least 22% by weight, particularly preferably at least 25% by weight. Preferably the amount of component (aii) used is at most 73% by weight, in particular at most 70% by weight, particularly preferably at most 67% by weight, especially at most 64% by weight, in each case based on the total weight of the composition (A*).
Possible monomeric polyfunctional isocyanates are aromatic, aliphatic, cycloaliphatic and/or araliphatic isocyanates. Such polyfunctional isocyanates are known per se or can be prepared by methods known per se. The polyfunctional isocyanates can also be used, in particular, as mixtures, so that the component (aii) in this case comprises various monomeric polyfunctional isocyanates. Polyfunctional isocyanates which are possible as monomer building blocks (aii) have two (hereinafter referred to as diisocyanates) or more than two isocyanate groups per molecule of the monomer component.
Particularly suitable monomeric polyfunctional isocyanates are diphenylmethane 2,2′-, 2,4′and/or 4,4′-diisocyanate (MDI), naphthylene 1,5-diisocyanate (NDI), tolylene 2,4- and/or 2,6-diisocyanate (TDI), 3,3′-dimethylbiphenyl diisocyanate, 1,2-diphenylethane diisocyanate and/or p-phenylene diisocyanate (PPDI), trimethylene, tetramethylene, pentamethylene, hexamethylene, heptamethylene and/or octamethylene diisocyanate, 2-methylpentamethylene 1,5-diisocyanate, 2-ethylbutylene 1,4-diisocyanate, pentamethylene 1,5-diisocyanate, butylene 1,4-diisocyanate, 1-isocyanato-3,3,5-trimethyl-5-isocyanatomethylcyclohexane (isophorone diisocyanate, IPDI), 1,4- and/or 1,3-bis(isocyanatomethyl)cyclohexane (HXDI), cyclohexane 1,4-diisocyanate, 1-methylcyclohexane 2,4- and/or 2,6-diisocyanate and dicyclohexylmethane 4,4′-, 2,4′- and/or 2,2′-diisocyanate.
As monomeric polyfunctional isocyanates (aii), preference is given to aromatic isocyanates. Particularly preferred polyfunctional isocyanates of the component (aii) are the following embodinvents:
i) polyfunctional isocyanates based on tolylene diisocyanate (TDI), in particular 2,4-TDI or 2,6-TDI or mixtures of 2,4- and 2,6-TDI;
ii) polyfunctional isocyanates based on diphenylmethane diisocyanate (MDI), in particular 2,2′-MDI or 2,4′-MDI or 4,4′-MDI or mixtures of two or three of the abovementioned diphenylmethane diisocyanates;
iii) mixtures of at least one aromatic isocyanate according to embodiment i) and at least one aromatic isocyanate according to embodiment ii).
According to a further embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein an isocyanate mixture is used as component (aii).
Suitable mixtures of isomers of MDI comprise for example 2,4-MDI and 4,4′-MDI. The total proportion by weight of 2,4-MDI based on the total weight of the mixture comprising composition 2,4-MDI and 4,4′-MDI, which is 100% by weight, is preferably from 0 to 56% by weight, in particular from 0.4 to 50% by weight, more preferably from 0.8 to 45% by weight, particularly preferably from 1.2 to 40% by weight. Adherence to the amount of isomers in the starting materials in the range mentioned leads to porous materials having a particularly advantageous pore structure, low thermal conductivity and low shrinking during drying.
Thus, according to a further embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein component (aii) comprises a mixture of 2,2′-diphenylmethane diisocyanate, 2,4-diphenylmethane diisocyanate and 4,4′-diphenylmethane diisocyanate.
The functionality of the component (aii) is preferably at least 1.5, in particular at least 1.7 and particularly preferably at least 1.9. The functionality of the component (aii) is preferably from 1.7 to 3 and particularly preferably from 1.9 to 2.5.
In a preferred embodiment, the component (aii) comprises at least one polyfunctional isocyanate selected from among diphenylmethane 4,4′-diisocyanate, diphenylmethane 2,4′-diisocyanate, diphenylmethane 2,2′-diisocyanate.
The viscosity of the component (aii) used can vary within a wide range. The component (ai) preferably has a viscosity of from 1 to 300 mPa·s, particularly preferably from 4 to 200 mPa·s.
Catalyst (ac)
The composition (A) further comprises at least one catalyst as component (ac). The amount of component (ac) used is preferably at least 0.1% by weight, in particular at least 0.2% by weight, particularly preferably at least 0.4% by weight, in particular at least 0.5% by weight. The amount of component (ac) used is preferably at most 20% by weight, in particular at most 17% by weight, particularly preferably at most 13% by weight, in particular at most 10% by weight, in each case based on the total weight of the composition (A).
Possible catalysts are in principle all catalysts known to those skilled in the art which accelerate the trimerization of isocyanates (known as trimerization catalysts) and/or the reaction of isocyanates with amino or hydroxyl groups (known as gelling catalysts) and/or the reaction of isocyanates with water (known as blowing catalysts).
The corresponding catalysts are known per se and have different relative activities in respect of the abovementioned three reactions. Depending on the relative activity, they can thus be assigned to one or more of the abovementioned types. Furthermore, it will be known to a person skilled in the art that reactions other than those mentioned above can also occur.
Corresponding catalysts can be characterized, inter alia, according to their gelling to blowing ratio, as is known, for example, from Polyurethane, 3rd edition, G. Oertel, Hanser Verlag, Munich, 1993.
According to a further embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein the catalyst catalyzes the trimerization to form isocyanurate groups.
According to another embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein component (ac) comprises at least one tertiary amino group.
According to a further embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein component (ac) comprises a catalyst catalyzing the trimerization to form isocyanurate groups and optional an amine catalyst.
Preferred catalysts at the same time have a significant activity in respect of trimerization. This favorably influences the homogeneity of the network structure, resulting in particularly advantageous mechanical properties.
The catalysts can be able to be incorporated as a monomer building block (incorporatable catalyst) or not be able to be incorporated.
Catalysts preferred as component (ac) are selected from the group consisting of primary, secondary and tertiary amines, triazine derivatives, organic metal compounds, metal chelates, organophosphorus compounds, in particular oxides of phospholenes, quaternary ammonium salts, ammonium hydroxides and also alkali metal and alkaline earth metal hydroxides, alkoxides and carboxylates.
According to a further embodiment, the present invention thus is directed to the process for preparing a porous material as disclosed above, wherein component (ac) is selected from the group consisting of primary, secondary and tertiary amines, triazine derivatives, metal-organic compounds, metal chelates, oxides of phospholenes, quaternary ammonium salts, ammonium hydroxides and alkali metal and alkaline earth metal hydroxides, alkoxides and carboxylates.
Suitable organophosphorus compounds, in particular oxides of phospholenes, are, for example, 1-methylphospholene oxide, 3-methyl-1-phenylphospholene oxide, 1-phenylphospholene oxide, 3-methyl-1-benzylphospholene oxide.
The suitable catalysts are preferably trimerization catalysts. Suitable trimerization catalysts are in particular strong bases, for example quaternary ammonium hydroxides such as tetraalkylammonium hydroxides having from 1 to 4 carbon atoms in the alkyl radical and benzyltrimethylammonium hydroxide, alkali metal hydroxides such as potassium or sodium hydroxide and alkali metal alkoxides such as sodium methoxide, potassium and sodium ethoxide and potassium isopropoxide.
Further suitable trimerization catalysts are, in particular, alkali metal salts or ammonium salts of carboxylic acids, e.g. potassium formate, sodium acetate, potassium acetate, caesium acetate, ammonium acetate, potassium propionate, potassium sorbate, potassium 2-ethylhexanoate, potassium octanoate, potassium trifluoroacetate, potassium trichloroacetate, sodium chloroacetate, sodium dichloroacetate, sodium trichloroacetate, potassium adipate, potassium benzoate, sodium benzoate, alkali metal salts or ammonium salts of saturated and unsaturated long-chain fatty acids having from 10 to 20 carbon atoms, and optionally lateral OH groups.
According to a further embodiment, the present invention thus is directed to the process for preparing a porous material as disclosed above, wherein component (ac) comprises at least one metal salt of a carboxylic acid.
Further suitable trimerization catalysts are, in particular, N-hydroxyalkyl quaternary ammonium carboxylates, e.g. trimethylhydroxypropylammonium formate.
Further suitable trimerization catalysts are, in particular 1-ethyl-3-methylimidazolium acetate (EMIM acetate), 1-butyl-3-methylimidazolium acetate (BMIM acetate), 1-ethyl-3-methylimidazolium octanoate (EMIM octanoate) and 1-butyl-3-methylimidazolium octanoate (BMIM octanoate).
Tertiary amines are also known per se to those skilled in the art as trimerization catalysts. Tertiary amines, i.e. compounds having at least one tertiary amino group, are particularly preferred as catalysts (ac). Suitable tertiary amines having distinct properties as trimerization catalysts are, in particular, N,N′,N″-tris(dialkylaminoalkyl)-s-hexahydrotriazines, such as N,N′,N″-tris(dimethylaminopropyl)-s-hexahydrotriazine, tris(dimethylaminomethyl)phenol.
Metal-organic compounds are known per se as gel catalysts to a person skilled in the art. Tin-organic compounds such as tin 2-ethylhexanoate and dibutyltin dilaurate are particularly preferred.
Tertiary amines are also known per se as gel catalysts to a person skilled in the art. As mentioned above, tertiary amines are particularly preferred as catalysts (ac). Suitable tertiary amines having good properties as gel catalysts are, in particular, N,N-dimethylbenzylamine, N,N′-dimethylpiperazine and N,N-dimethylcyclohexylamine, bis(2-dimethylaminoethyl) ether, N,N,N,N,N-pentamethyldiethylenetriamine, methylimidazole, dimethylimidazole, aminopropylimidazole, dimethylbenzylamine, 1,6-diazabicyclo[5.4.0]undec-7-ene, triethylamine, triethylenediamine (1,4-diazabicyclo[2.2.2]octane), dimethylaminoethanolamine, dimethylaminopropylamine, N,N-dimethylaminoethoxyethanol, N,N,N-trimethylaminoethylethanolamine, triethanolamine, diethanolamine, triisopropanolamine, diisopropanolamine, methyldiethanolamine and butyldiethanolamine.
Catalysts which are particularly preferred as component (ac) are selected from the group consisting of dimethylcyclohexylamine, dimethylpiperazine, bis(2-dimethylaminoethyl) ether, N,N,N,N,N-pentamethyldiethylenetriamine, methylimidazole, dimethylimidazole, aminopropylimidazole, dimethylbenzylamine, 1,6-diazabicyclo[5.4.0]undec-7-ene, trisdimethylaminopropyl-hexahydrotriazine, triethylamine, tris(dimethylaminomethyl)phenol, triethylenediamine (diazabicyclo[2.2.2]octane), dimethylaminoethanolamine, dimethylaminopropylamine, N,N-dimethylaminoethoxyethanol, N,N,N-trimethylaminoethylethanolamine, triethanolamine, diethanolamine, triisopropanolamine, diisopropanolamine, methyldiethanolamine, butyldiethanolamine.
Very particular preference is given to dimethylcyclohexylamine, dimethylpiperazine, methylimidazole, dimethylimidazole, dimethylbenzylamine, 1,6-diazabicyclo[5.4.0]undec-7-ene, trisdimethylaminopropylhexahydrotriazine, triethylamine, tris(dimethylaminomethyl)phenol, triethylenediamine (diazabicyclo[2.2.2]octane), dimethylaminoethanolamine, dimethylaminopropylamine, N,N,N-trimethylaminoethylethanolamine, triethanolamine, diethanolamine, methyldiethanolamine, butyldiethanolamine, metal acetylacetonates, and metal acetates, propionates, sorbates, ethylhexanoates, octanoates and benzoates.
Therefore, according to a further embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein component (ac) is selected from the group consisting of dimethylcyclohexylamine, bis(2-dimethylaminoethyl) ether, N,N,N,N,N-pentamethyldiethylenetriamine, methylimidazole, dimethylimidazole, aminopropylimidazole, dimethylbenzylamine, 1,6-diazabicyclo[5.4.0]undec-7-ene, trisdimethylaminopropylhexahydrotriazine, triethylamine, tris(dimethylaminomethyl)phenol, triethylenediamine (diazabicyclo[2.2.2]octane), dimethylaminoethanolamine, dimethylaminopropylamine, N,N-dimethylaminoethoxyethanol, N,N,N-trimethylaminoethylethanolamine, triethanolamine, diethanolamine, triisopropanolamine, diisopropanolamine, methyldiethanolamine, butyldiethanolamine, metal acetylacetonates, and metal acetates, propionates, sorbates, ethylhexanoates, octanoates and benzoates.
According to the present invention, component (ac) can comprise one or more catalysts. For example a mixture comprising a trimerization catalyst as well as an amine can be used in the context of the present invention. Therefore, according to a further embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein component (ac) comprises a catalyst catalyzing the trimerization to form isocyanurate groups and an amine catalyst.
The ratio of the amount of the catalyst catalyzing the trimerization to form isocyanurate groups and the amine catalyst may vary in wide ranges in the context of the present invention. Preferably, the catalyst catalyzing the trimerization to form isocyanurate groups is used in an amount of from 100% to 30%, particularly preferred in an amount of from 100% to 40%, more preferred in an amount of from 100% to 45% of the sum of the catalyst catalyzing the trimerization to form isocyanurate groups and the amine catalyst.
Component (ac) can further comprise one or more acids. Thus, according to a further embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein component (ac) comprises at least one carboxylic acid.
In principle, any carboxylic acid can be used in the context of the present invention. It is also possible to use two or more carboxylic acids according to the present invention. Preferably, saturated or unsaturated monocarboxylic acids with 2 to 12 carbon atoms are used, for example saturated or unsaturated monocarboxylic acids with 2 to 10 carbon atoms, in particular 2 to 8 carbon atoms such as, formic acid, acetic acid, propionic acid, sorbic acid, benzoic acid, ethyl hexanoic acid, or octanoic acid.
Thus, according to a further embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein the carboxylic acid is selected from the group of saturated or unsaturated monocarboxylic acids with 2 to 12 carbon atoms.
Furthermore, the component (ac) can comprise a salt in combination with one or more acids. The salt may be selected from the group consisting of alkali metal and earth alkali metal, ammonium, ionic liquid salts of a saturated or unsaturated monocarboxylic acid. In principle, any alkali metal or earth alkali metal salt of a saturated or unsaturated monocarboxylic acid or ammonium or ionic liquid salt can be used in the context of the present invention. It is also possible to use mixtures of two or more alkali metal or earth alkali metal salts of a saturated or unsaturated monocarboxylic acid in the context of the present invention.
Preferably, the salt is selected from the group consisting of alkali metal and earth alkali metal salts of a saturated or unsaturated monocarboxylic acid with 2 to 8 carbon atoms, more preferably, the salt is selected from the group consisting of alkali metal and earth alkali metal salts of a linear saturated or unsaturated monocarboxylic acid with 2 to 8 carbon atoms. It has been found that using an alkali metal or earth alkali metal salts of saturated or unsaturated monocarboxylic acid with 2 to 8 carbon atoms as a catalyst results in porous materials with improved compressive strength. Suitable salts are for example sodium salts, potassium salts, or calcium salts of the respective monocarboxylic acid.
Preferably, a salt selected from the group consisting of alkali metal and earth alkali metal salts of a saturated or unsaturated monocarboxylic acid with 2 to 8 carbon atoms is used in combination with an acid selected from the group of saturated or unsaturated monocarboxylic acids with 2 to 12 carbon atoms.
More preferably, the salt is selected from the group consisting of alkali metal and earth alkali metal salts of a saturated or unsaturated monocarboxylic acid with 2 to 8 carbon atoms and at the same time the acid is selected from the group consisting of acetic acid and propionic acid.
The salt and the acid may for example be used in a ratio in the range of from 1:10 to 14:1, preferably in the range of from 1:5 to 12:1, more preferably in the range of from 1:1 to 10:1.
Solvent (B)
According to the present invention, the reaction takes place in the presence of a solvent (B).
For the purposes of the present invention, the term solvent (B) comprises liquid diluents, i.e. both solvents in the narrower sense and also dispersion media. The mixture can, in particular, be a true solution, a colloidal solution or a dispersion, e.g. an emulsion or suspension. The mixture is preferably a true solution. The solvent (B) is a compound which is liquid under the conditions of step (a), preferably an organic solvent.
The solvent (B) can in principle be any suitable compound or mixture of a plurality of compounds, with the solvent (B) being liquid under the temperature and pressure conditions under which the mixture is provided in step (a) (dissolution conditions for short). The composition of the solvent (B) is selected so that it is able to dissolve or disperse, preferably dissolve, the organic gel precursor. Preferred solvents (B) are those which are a solvent for the organic gel precursor (A′), i.e. ones which dissolve the organic gel precursor (A′) completely under the reaction conditions.
The reaction product of the reaction in the presence of the solvent (B) is initially a gel, i.e. a vis-coelastic chemical network which is swollen by the solvent (B). A solvent (B) which is a good swelling agent for the network formed in step (b) generally leads to a network having fine pores and a small average pore diameter, while a solvent (B) which is a poor swelling agent for the gel resulting from step (b) generally leads to a coarse-pored network having a large average pore diameter.
The choice of the solvent (B) thus influences the desired pore size distribution and the desired porosity. The choice of the solvent (B) is also generally made in such a way that precipitation or flocculation due to formation of a precipitated reaction product does not occur to a significant extent during or after step (b) of the process of the invention.
When a suitable solvent (B) is chosen, the proportion of precipitated reaction product is usually less than 1% by weight, based on the total weight of the mixture. The amount of precipitated product formed in a particular solvent (B) can be determined gravimetrically by filtering the reaction mixture through a suitable filter before the gelling point.
Possible solvents (B) are solvents known from the prior art for isocyanate-based polymers. Preferred solvents are those which are a solvent for the components (ai), (aii) and (ac), i.e. solvents which dissolve the constituents of the components (ai), (aii) and (ac) virtually completely under the reaction conditions. The solvent (B) is preferably inert, i.e. unreactive, toward component (ai) and (aii).
Possible solvents (B) are, for example, ketones, aldehydes, alkyl alkanoates, amides such as formamide and N-methylpyrollidone, sulfoxides such as dimethyl sulfoxide, aliphatic and cycloaliphatic hydrocarbons, cycloaromatic hydrocarbons, aliphatic and cycloaliphatic halogenated hydrocarbons, halogenated aromatic compounds and fluorine-containing ethers. Mixtures of two or more of the abovementioned compounds are likewise possible.
Further possibilities as solvents (B) are acetals, in particular diethoxymethane, dimethoxymethane and 1,3-dioxolane.
Dialkyl ethers and cyclic ethers are likewise suitable as solvent (B). Preferred dialkyl ethers are, in particular, those having from 2 to 6 carbon atoms, in particular methyl ethyl ether, diethyl ether, methyl propyl ether, methyl isopropyl ether, propyl ethyl ether, ethyl isopropyl ether, dipropyl ether, propyl isopropyl ether, diisopropyl ether, methyl butyl ether, methyl isobutyl ether, methyl t-butyl ether, ethyl n-butyl ether, ethyl isobutyl ether and ethyl t-butyl ether. Preferred cyclic ethers are, in particular, tetrahydrofuran, dioxane and tetrahydropyran.
Aldehydes and/or ketones are particularly preferred as solvent (B). Aldehydes or ketones suitable as solvent (B) are, in particular, those corresponding to the general formula R2—(CO)—R1, where R1 and R2 are each hydrogen or an alkyl group having 1, 2, 3, 4, 5, 6 or 7 carbon atoms. Suitable aldehydes or ketones are, in particular, acetaldehyde, propionaldehyde, n-butyraldehyde, isobutyraldehyde, 2-ethylbutyraldehyde, valeraldehyde, isopentaldehyde, 2-methylpentaldehyde, 2-ethylhexaldehyde, acrolein, methacrolein, crotonaldehyde, furfural, acrolein dimer, methacrolein dimer, 1,2,3,6-tetrahydrobenzaldehyde, 6-methyl-3-cyclohexenaldehyde, cyanoacetaldehyde, ethyl glyoxylate, benzaldehyde, acetone, diethyl ketone, methyl ethyl ketone, methyl isobutyl ketone, methyl n-butyl ketone, methyl pentylketone, dipropyl ketone, ethyl isopropyl ketone, ethyl butyl ketone, diisobutylketone, 5-methyl-2-acetyl furan, 2-acetylfuran, 2-methoxy-4-methylpentan-2-one, 5-methylheptan-3-one, octanone, cyclohexanone, cyclopentanone, and acetophenone. The abovementioned aldehydes and ketones can also be used in the form of mixtures. Ketones and aldehydes having alkyl groups having up to 3 carbon atoms per substituent are preferred as solvent (B).
Further preferred solvents are alkyl alkanoates, in particular methyl formate, methyl acetate, ethyl formate, isopropyl acetate, butyl acetate, ethyl acetate, glycerine triacetate and ethyl acetoacetate. Preferred halogenated solvents are described in WO 00/24799, page 4, line 12 to page 5, line 4.
Further suitable solvents (B) are organic carbonates such as for example dimethyl carbonate, ethylene carbonate, propylene carbonate or butylene carbonate.
In many cases, particularly suitable solvents (B) are obtained by using two or more completely miscible compounds selected from the abovementioned solvents.
To obtain a sufficiently stable gel which does not shrink too much during drying in step (c) in step (b), the proportion of the composition (A) based on the total weight of the mixture (I) comprising composition (A) and the solvent (B), which is 100% by weight, must generally be not less than 1% by weight. The proportion of the composition (A) based on the total weight of the mixture (I) comprising composition (A) and the solvent (B), which is 100% by weight, is preferably at least 2% by weight, particularly preferably at least 3% by weight, in particular at least 3.5% by weight.
On the other hand, the concentration of the composition (A) in the mixture provided must not be too high since otherwise no porous material having favorable properties is obtained. In general, the proportion of the composition (A) based on the total weight of the mixture (I) comprising composition (A) and the solvent (B), which is 100% by weight, is not more than 50% by weight. The proportion of the composition (A) based on the total weight of the mixture (I) comprising composition (A) and the solvent (B), which is 100% by weight, is preferably not more than 45% by weight, particularly preferably not more than 42% by weight, more preferably not more than 39% by weight, in particular not more than 36% by weight.
The total proportion by weight of the composition (A) based on the total weight of the mixture (I) comprising composition (A) and the solvent (B), which is 100% by weight, is preferably from 1 to 45% by weight, in particular from 2 to 42% by weight, more preferably from 3 to 39% by weight, particularly preferably from 3.5 to 36% by weight. Adherence to the amount of the starting materials in the range mentioned leads to porous materials having a particularly advantageous pore structure, low thermal conductivity and low shrinking during drying.
Before the reaction, it is necessary to mix the components used, in particular to mix them homogeneously. The rate of mixing should be high relative to the rate of the reaction in order to avoid mixing defects. Appropriate mixing methods are known per se to those skilled in the art.
According to the present invention, a solvent (B) is used. The solvent (B) can also be a mixture of two or more solvents, for example three or four solvents. Suitable solvents are for example mixtures of two or more ketones, for example mixtures of acetone and diethyl ketone, mixtures of acetone and methyl ethyl ketone or mixtures of diethyl ketone and methyl ethyl ketone.
Further preferred solvents are mixtures of propylene carbonate with one or more solvents, for example mixtures of propylene carbonate and diethyl ketone, or mixtures of propylene carbonate with two or more ketones, for example mixtures of propylene carbonate with acetone and diethyl ketone, mixtures of propylene carbonate with acetone and methyl ethyl ketone or mixtures of propylene carbonate with diethyl ketone and methyl ethyl ketone.
Preferred Process for Producing the Porous Materials
The process of the invention comprises at least the following steps:
(a) provision of the mixture comprising the composition (A) and the solvent (B) as described above,
(b) reaction of the components in composition (A) in the presence of the solvent (B) to form a gel and
(c) drying of the gel obtained in the preceding step.
Preferred embodiments of steps (a) to (c) will be described in detail below.
Step (a)
According to the invention, a mixture comprising composition (A) and the solvent (B) are provided in step (a).
The components of composition (A), for example the components (ai), (aii) and (ac) are preferably provided separately from one another, each in a suitable partial amount of the solvent (B). The separate provision makes it possible for the gelling reaction to be optimally monitored or controlled before and during mixing.
Component (ac) is particularly preferably provided as a mixture, i.e. separately from components (ai) and (aii).
The mixture or mixtures provided in step (a) can also comprise customary auxiliaries known to those skilled in the art as further constituents. Mention may be made by way of example of surface-active substances, flame retardants, nucleating agents, oxidation stabilizers, lubricants and mold release agents, dyes and pigments, stabilizers, e.g. against hydrolysis, light, heat or discoloration, inorganic and/or organic fillers, reinforcing materials and biocides.
Further information regarding the abovementioned auxiliaries and additives may be found in the specialist literature, e.g. in Plastics Additive Handbook, 5th edition, H. Zweifel, ed. Hanser Publishers, Munich, 2001.
Step (b)
According to the invention, the reaction of the components of composition (A) takes place in the presence of the solvent (B) to form a gel in step (b). To carry out the reaction, a homogeneous mixture of the components provided in step (a) firstly has to be produced.
The provision of the components provided in step (a) can be carried out in a conventional way. A stirrer or another mixing device is preferably used here in order to achieve good and rapid mixing. The time required for producing the homogeneous mixture should be short in relation to the time during which the gelling reaction leads to at least partial formation of a gel, in order to avoid mixing defects. The other mixing conditions are generally not critical; for example, mixing can be carried out at from 0 to 100° C. and from 0.1 to 10 bar (absolute), in particular at, for example, room temperature and atmospheric pressure. After a homogeneous mixture has been produced, the mixing apparatus is preferably switched off.
The gelling reaction is a polyaddition reaction resulting in a polyisocyanurate crosslinked network.
For the purposes of the present invention, a gel is a crosslinked system based on a polymer which is present in contact with a liquid (known as Solvogel or Lyogel, or with water as liquid: aquagel or hydrogel). Here, the polymer phase forms a continuous three-dimensional network.
In step (b) of the process of the invention, the gel is usually formed by allowing to rest, e.g. by simply allowing the container, reaction vessel or reactor in which the mixture is present (hereinafter referred to as gelling apparatus) to stand. The mixture is preferably no longer stirred or mixed during gelling (gel formation) because this could hinder formation of the gel. It has been found to be advantageous to cover the mixture during gelling or to close the gelling apparatus.
Gelling is known per se to a person skilled in the art and is described, for example, in WO 2009/027310 on page 21, line 19 to page 23, line 13.
Step (c)
According to the invention, the gel obtained in the previous step is dried in step (c).
Drying under supercritical conditions is in principle possible, preferably after replacement of the solvent by CO2 or other solvents suitable for the purposes of supercritical drying. Such drying is known per se to a person skilled in the art. Supercritical conditions characterize a temperature and a pressure at which CO2 or any solvent used for removal of the gelation solvent or mixtures of both is present in the supercritical state. In this way, shrinkage of the gel body on removal of the solvent can be reduced.
However, in view of the simple process conditions, preference is given to drying the gels obtained by conversion of the liquid comprised in the gel into the gaseous state at a temperature and a pressure below the critical temperature and the critical pressure of the liquid comprised in the gel.
The drying of the gel obtained is preferably carried out by converting the solvent (B) into the gaseous state at a temperature and a pressure below the critical temperature and the critical pressure of the solvent (B). Accordingly, drying is preferably carried out by removing the solvent (B) which was present in the reaction without prior replacement by a further solvent.
Such methods are likewise known to those skilled in the art and are described in WO 2009/027310 on page 26, line 22 to page 28, line 36.
According to a further embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein the drying according to step c) is carried out by converting the liquid comprised in the gel into the gaseous state at a temperature and a pressure below the critical temperature and the critical pressure of the liquid comprised in the gel.
According to a further embodiment, the present invention is directed to the process for preparing a porous material as disclosed above, wherein the drying according to step c) is carried out under supercritical conditions.
Properties of the Porous Materials and Use
The present invention further provides the porous materials which can be obtained by the process of the invention. Aerogels are preferred as porous materials for the purposes of the present invention, i.e. the porous material which can be obtained according to the invention is preferably an aerogel.
Furthermore, the present invention therefore is directed to a porous material which is obtained or obtainable by the process for preparing a porous material as disclosed above. In particular, the present invention is directed to a porous material which is obtained or obtainable by the process for preparing a porous material as disclosed above, wherein the drying according to step c) is carried out under supercritical conditions.
The average pore diameter is determined by scanning electron microscopy and subsequent image analysis using a statistically significant number of pores. Corresponding methods are known to those skilled in the art.
The volume average pore diameter of the porous material is preferably not more than 4 microns. The volume average pore diameter of the porous material is particularly preferably not more than 3 microns, very particularly preferably not more than 2 microns and in particular not more than 1 micron.
Although a very small pore size combined with a high porosity is desirable from the point of view of a low thermal conductivity, from the point of view of production and to obtain a sufficiently mechanically stable porous material, there is a practical lower limit to the volume average pore diameter. In general, the volume average pore diameter is at least 10 nm, preferably at least 30 nm.
The porous material which can be obtained according to the invention preferably has a porosity of at least 70% by volume, in particular from 70 to 99% by volume, particularly preferably at least 80% by volume, very particularly preferably at least 85% by volume, in particular from 85 to 95% by volume. The porosity in % by volume means that the specified proportion of the total volume of the porous material comprises pores. Although a very high porosity is usually desirable from the point of view of a minimal thermal conductivity, an upper limit is imposed on the porosity by the mechanical properties and the processability of the porous material.
The components of composition (A), for example the components (ai) and (aii) and (ac), as long as the catalyst can be incorporated, are present in reactive (polymer) form in the porous material which can be obtained according to the invention. Owing to the composition according to the invention, the monomer building blocks are predominantly bound via isocyanurate linkages in the porous material, with the isocyanurate groups being formed by trimerization of isocyanate groups of the monomer building blocks (ai) and (aii). If the porous material comprises further components, further possible linkages are, for example, urethane groups formed by reaction of isocyanate groups with alcohols or phenols.
The determination of the mol % of the linkages of the monomer building blocks in the porous material is carried out by means of NMR spectroscopy (nuclear magnetic resonance) in the solid or in the swollen state. Suitable methods of determination are known to those skilled in the art.
The density of the porous material which can be obtained according to the invention is usually from 20 to 600 g/l, preferably from 50 to 500 g/l and particularly preferably from 70 to 300 g/l.
The process of the invention gives a coherent porous material and not only a polymer powder or particles. Here, the three-dimensional shape of the resulting porous material is determined by the shape of the gel which is in turn determined by the shape of the gelling apparatus. Thus, for example, a cylindrical gelling vessel usually gives an approximately cylindrical gel which can then be dried to give a porous material having a cylindrical shape.
The porous materials which can be obtained according to the invention have a low thermal conductivity, a high porosity and a low density combined with high mechanical stability. In addition, the porous materials have a small average pore size. The combination of the abovementioned properties allows the materials to be used as insulation material in the field of thermal insulation, in particular for applications in the ventilated state as building materials.
The porous materials which can be obtained according to the invention have advantageous thermal properties and also further advantageous properties such as simple processability and high mechanical stability, for example low brittleness.
The present invention is also directed to the use of porous materials as disclosed above or a porous material obtained or obtainable according to a process as disclosed above as thermal insulation material or for vacuum insulation panels. The thermal insulation material is for example insulation material which is used for insulation in the interior or the exterior of a building. The porous material according to the present invention can advantageously be used in thermal insulation systems such as for example composite materials.
According to a further embodiment, the present invention therefore is directed to the use of porous materials as disclosed above, wherein the porous material is used in interior or exterior thermal insulation systems. According to a further embodiment, the present invention is also directed to the use of porous materials as disclosed above, wherein the porous material is used in water tank or ice maker thermal insulation systems.
The present invention includes the following embodiments, wherein these include the specific combinations of embodiments as indicated by the respective interdependencies defined therein.
1. Process for preparing a porous material, at least comprising the steps of:
2. The process according to embodiment 1, wherein composition (A*) comprises component (ai) in an amount of from 84 to 27% by weight and component (aii) in an amount of from 16 to 73% by weight.
3. The process according to any of embodiments 1 or 2, wherein component (ai) is selected from polymeric polyfunctional isocyanates based on diphenylmethane diisocyanate (MDI) and component (aii) is selected from monomeric diphenylmethane diisocyanate (MDI).
4. The process according to any of embodiments 1 to 3, wherein component (aii) comprises a mixture of 2,2′-diphenylmethane diisocyanate, 2,4-diphenylmethane diisocyanate and 4,4′-diphenylmethane diisocyanate.
5. The process according to any of embodiments 1 to 4, wherein the composition (A) comprises less than 1% by weight of water.
6. The process according to any of embodiments 1 to 5, wherein composition (A) comprises
7. The process according to any of embodiments 1 to 6, wherein the catalyst is selected from the group consisting of primary, secondary and tertiary amines, triazine derivatives, metal-organic compounds, metal chelates, oxides of phospholenes, quaternary ammonium salts, ammonium salts, ammonium hydroxides and alkali metal and alkaline earth metal hydroxides, alkoxides and carboxylates.
8. The process according to any of embodiments 1 to 7, wherein the catalyst catalyzes the trimerization to form isocyanurate groups.
9. The process according any of embodiments 1 to 8, wherein component (ac) comprises a catalyst catalyzing the trimerization to form isocyanurate groups and optional an amine catalyst.
10. The process according to any of embodiments 1 to 9, wherein component (ac) comprises at least one metal salt of a carboxylic acid.
11. The process according to any of embodiments 1 to 10, wherein the drying according to step c) is carried out by converting the liquid comprised in the gel into the gaseous state at a temperature and a pressure below the critical temperature and the critical pressure of the liquid comprised in the gel.
12. The process according to any of embodiments 1 to 10, wherein the drying according to step c) is carried out under supercritical conditions.
13. A porous material, which is obtained or obtainable by the process according to any of embodiments 1 to 12.
14. The use of porous materials according to embodiment 13 or a porous material obtained or obtainable by the process according to any of embodiments 1 to 12 as thermal insulation material or for vacuum insulation panels.
15. The use according to embodiment 14, wherein the porous material is used in interior or exterior thermal insulation systems.
Examples will be used below to illustrate the invention.
The thermal conductivity was measured according to DIN EN 12667 with a heat flow meter from Hesto (Lambda Control A50).
One or several gel monoliths were placed onto sample trays in an autoclave of 25 l volume. Subsequent to filling with supercritical carbon dioxide (scCO2), the gelation solvent was removed (drying) by flowing scCO2 through the autoclave for 24 h (20 kg/h). Process pressure was kept between 120 and 130 bar and process temperature at 45° C. in order to maintain carbon dioxide in a supercritical state. At the end of the process, the pressure was reduced to normal atmospheric pressure in a controlled manner while maintaining the system at a temperature of 45° C. The autoclave was opened, and the obtained porous monoliths were removed.
M200: oligomeric MDI (Lupranat M200) having an NCO content of 30.9 g per 100 g accordance with ASTM D-5155-96 A, a functionality in the region of three and a viscosity of 2100 mPa·s at 25° C. in accordance with DIN 53018 (hereafter “M200”)
Lupranat MI: monomeric MDI (Lupranat MI) having an NCO content of 33.5 g per 100 g accordance with ASTM D-5155-96 A, a functionality in the region of two and a viscosity of 12 mPa·s at 25° C. in accordance with DIN 53018 (hereafter “MI”)
Lupranat ME: monomeric MDI (Lupranat ME) having an NCO content of 33.5 g per 100 g accordance with ASTM D-5155-96 A, a functionality in the region of two and a viscosity of 5 mPa·s at 42° C. in accordance with DIN 53018 (hereafter “ME”)
Catalysts: Dabco K15 (potassium ethylhexanoate dissolved in diethylene glycol (85%))
Solvent: Acetone
In a polypropylene container, 56 g M200 were dissolved under stirring in 220 g MEK at 20° C. leading to a clear solution. Similarly, 2 g Dabco K15 were dissolved in 220 g MEK to obtain a second solution. The solutions were combined in a rectangular container (20×20 cm×5 cm height) by pouring one solution into the other, which led to a clear, homogeneous mixture of low viscosity. The container was closed with a lid and the mixture was gelled at room temperature for 24 h. The resulting monolithic gel slab was dried through solvent extraction with scCO2 in a 25 l autoclave leading to a porous material.
The gel-monolith was removed from the container and transferred to an autoclave. The autoclave was filled with >99 vol % of acetone, to fully cover the gel and then the lid closed. This prevents the gel from shrinking due to evaporating solvent, before the monolith gets in contact with sc. CO2. The gel was dried in a supercritical CO2 stream for 24 h. The pressure in the vessel was between 115-120 bar; the temperature was between 40-60° C. At the end of the drying step, the pressure of the system was reduced to 1 bar over 45 min at a temperature of 40° C. The autoclave was opened ant the destroyed monolith was removed. The internal tension resulted in a complete destruction of the material.
In a polypropylene container, 39.2 g M200 and 16.8 g MI were dissolved under stirring in 220 g MEK at 20° C. leading to a clear solution. Similarly, 2 g Dabco K15 were dissolved in 220 g MEK to obtain a second solution. The solutions were combined in a rectangular container (20×20 cm×5 cm height) by pouring one solution into the other, which led to a clear, homogeneous mixture of low viscosity. The container was closed with a lid and the mixture was gelled at room temperature for 24 h. The resulting monolithic gel slab was dried through solvent extraction with scCO2 in a 25 l autoclave leading to a porous material.
The gel-monolith was removed from the container and transferred to an autoclave. The autoclave was filled with >99 vol % of acetone, to fully cover the gel and then the lid closed. This prevents the gel from shrinking due to evaporating solvent, before the monolith gets in contact with sc. CO2. The gel was dried in a supercritical CO2 stream for 24 h. The pressure in the vessel was between 115-120 bar; the temperature was between 40-60° C. At the end of the drying step, the pressure of the system was reduced to 1 bar over 45 min at a temperature of 40° C. The autoclave was opened ant the monolith was removed. The thermal conductivity λ was measured according to DIN EN 12667 with a plate apparatuses from Hesto (Lambda Control A50). The thermal conductivity was 18.4 mW/m*K at 10° C. The density was 202 kg/m3.
In a polypropylene container, 28 g M200 and 28 g MI were dissolved under stirring in 220 g MEK at 20° C. leading to a clear solution. Similarly, 2 g Dabco K15 were dissolved in 220 g MEK to obtain a second solution. The solutions were combined in a rectangular container (20×20 cm×5 cm height) by pouring one solution into the other, which led to a clear, homogeneous mixture of low viscosity. The container was closed with a lid and the mixture was gelled at room temperature for 24 h. The resulting monolithic gel slab was dried through solvent extraction with scCO2 in a 25 l autoclave leading to a porous material.
The gel-monolith was removed from the container and transferred to an autoclave. The autoclave was filled with >99 vol % of acetone, to fully cover the gel and then the lid closed. This prevents the gel from shrinking due to evaporating solvent, before the monolith gets in contact with sc. CO2. The gel was dried in a supercritical CO2 stream for 24 h. The pressure in the vessel was between 115-120 bar; the temperature was between 40-60° C. At the end of the drying step, the pressure of the system was reduced to 1 bar over 45 min at a temperature of 40° C. The autoclave was opened ant the monolith was removed. The thermal conductivity λ was measured according to DIN EN 12667 with a plate apparatuses from Hesto (Lambda Control A50). The thermal conductivity was 18.9 mW/m*K at 10° C. The density was 189 kg/m3.
In a polypropylene container, 39.2 g M200 and 8.4 g MI and 8.4 g ME were dissolved under stirring in 220 g Acetone at 20° C. leading to a clear solution. Similarly, 2 g Dabco K15 were dissolved in 220 g Acetone to obtain a second solution. The solutions were combined in a rectangular container (20×20 cm×5 cm height) by pouring one solution into the other, which led to a clear, homogeneous mixture of low viscosity. The container was closed with a lid and the mixture was gelled at room temperature for 24 h. The resulting monolithic gel slab was dried through solvent extraction with scCO2 in a 25 l autoclave leading to a porous material.
The gel-monolith was removed from the container and transferred to an autoclave. The autoclave was filled with >99 vol % of acetone, to fully cover the gel and then the lid closed. This prevents the gel from shrinking due to evaporating solvent, before the monolith gets in contact with sc. CO2. The gel was dried in a supercritical CO2 stream for 24 h. The pressure in the vessel was between 115-120 bar; the temperature was between 40-60° C. At the end of the drying step, the pressure of the system was reduced to 1 bar over 45 min at a temperature of 40° C. The autoclave was opened ant the monolith was removed. The thermal conductivity λ was measured according to DIN EN 12667 with a plate apparatuses from Hesto (Lambda Control A50). The thermal conductivity was 21.2 mW/m*K at 10° C. The density was 286 kg/m3.
In a polypropylene container, 39.2 g M200 and 8.4 g MI and 8.4 g ME were dissolved under stirring in 220 g MEK at 20° C. leading to a clear solution. Similarly, 2 g Dabco K15 were dissolved in 220 g MEK to obtain a second solution. The solutions were combined in a rectangular container (20×20 cm×5 cm height) by pouring one solution into the other, which led to a clear, homogeneous mixture of low viscosity. The container was closed with a lid and the mixture was gelled at room temperature for 24 h. The resulting monolithic gel slab was dried through solvent extraction with scCO2 in a 25 l autoclave leading to a porous material.
The gel-monolith was removed from the container and transferred to an autoclave. The autoclave was filled with >99 vol % of acetone, to fully cover the gel and then the lid closed. This prevents the gel from shrinking due to evaporating solvent, before the monolith gets in contact with sc. CO2. The gel was dried in a supercritical CO2 stream for 24 h. The pressure in the vessel was between 115-120 bar; the temperature was between 40-60° C. At the end of the drying step, the pressure of the system was reduced to 1 bar over 45 min at a temperature of 40° C. The autoclave was opened ant the monolith was removed. The thermal conductivity λ was measured according to DIN EN 12667 with a plate apparatuses from Hesto (Lambda Control A50). The thermal conductivity was 19.8 mW/m*K at 10° C. The density was 229 kg/m3.
In a polypropylene container, 39.2 g M200 and 8.4 g MI and 8.4 g ME were dissolved under stirring in 220 g DEK at 20° C. leading to a clear solution. Similarly, 2 g Dabco K15 were dissolved in 220 g DEK to obtain a second solution. The solutions were combined in a rectangular container (20×20 cm×5 cm height) by pouring one solution into the other, which led to a clear, homogeneous mixture of low viscosity. The container was closed with a lid and the mixture was gelled at room temperature for 24 h. The resulting monolithic gel slab was dried through solvent extraction with scCO2 in a 25 l autoclave leading to a porous material.
The gel-monolith was removed from the container and transferred to an autoclave. The autoclave was filled with >99 vol % of acetone, to fully cover the gel and then the lid closed. This prevents the gel from shrinking due to evaporating solvent, before the monolith gets in contact with sc. CO2. The gel was dried in a supercritical CO2 stream for 24 h. The pressure in the vessel was between 115-120 bar; the temperature was between 40-60° C. At the end of the drying step, the pressure of the system was reduced to 1 bar over 45 min at a temperature of 40° C. The autoclave was opened ant the monolith was removed. The thermal conductivity λ was measured according to DIN EN 12667 with a plate apparatuses from Hesto (Lambda Control A50). The thermal conductivity was 17.0 mW/m*K at 10° C. The density was 212 kg/m3.
In a polypropylene container, 39.2 g M200 and 18.8 g ME were dissolved under stirring in 220 g DEK at 20° C. leading to a clear solution. Similarly, 2 g Dabco K15 were dissolved in 220 g DEK to obtain a second solution. The solutions were combined in a rectangular container (20×20 cm×5 cm height) by pouring one solution into the other, which led to a clear, homogeneous mixture of low viscosity. The container was closed with a lid and the mixture was gelled at room temperature for 24 h. The resulting monolithic gel slab was dried through solvent extraction with scCO2 in a 25 l autoclave leading to a porous material.
The gel-monolith was removed from the container and transferred to an autoclave. The autoclave was filled with >99 vol % of acetone, to fully cover the gel and then the lid closed. This prevents the gel from shrinking due to evaporating solvent, before the monolith gets in contact with sc. CO2. The gel was dried in a supercritical CO2 stream for 24 h. The pressure in the vessel was between 115-120 bar; the temperature was between 40-60° C. At the end of the drying step, the pressure of the system was reduced to 1 bar over 45 min at a temperature of 40° C. The autoclave was opened ant the monolith was removed. The thermal conductivity λ was measured according to DIN EN 12667 with a plate apparatuses from Hesto (Lambda Control A50). The thermal conductivity was 16.6 mW/m*K at 10° C. The density was 242 kg/m3.
In a polypropylene container, 39.2 g M200 and 18.8 g MI were dissolved under stirring in 220 g DEK at 20° C. leading to a clear solution. Similarly, 2 g Dabco K15 were dissolved in 220 g DEK to obtain a second solution. The solutions were combined in a rectangular container (20×20 cm×5 cm height) by pouring one solution into the other, which led to a clear, homogeneous mixture of low viscosity. The container was closed with a lid and the mixture was gelled at room temperature for 24 h. The resulting monolithic gel slab was dried through solvent extraction with scCO2 in a 25 l autoclave leading to a porous material.
The gel-monolith was removed from the container and transferred to an autoclave. The autoclave was filled with >99 vol % of acetone, to fully cover the gel and then the lid closed. This prevents the gel from shrinking due to evaporating solvent, before the monolith gets in contact with sc. CO2. The gel was dried in a supercritical CO2 stream for 24 h. The pressure in the vessel was between 115-120 bar; the temperature was between 40-60° C. At the end of the drying step, the pressure of the system was reduced to 1 bar over 45 min at a temperature of 40° C. The autoclave was opened ant the monolith was removed. The thermal conductivity λ was measured according to DIN EN 12667 with a plate apparatuses from Hesto (Lambda Control A50). The thermal conductivity was 16.7 mW/m*K at 10° C. The density was 214 kg/m3.
In a polypropylene container, 39.2 g M200 and 8.4 g MI and 8.4 g ME were dissolved under stirring in 180 g DEK and 40 g toulene at 20° C. leading to a clear solution. Similarly, 2 g Dabco K15 were dissolved in 180 g DEK and 40 g toluene to obtain a second solution. The solutions were combined in a rectangular container (20×20 cm×5 cm height) by pouring one solution into the other, which led to a clear, homogeneous mixture of low viscosity. The container was closed with a lid and the mixture was gelled at room temperature for 24 h. The resulting monolithic gel slab was dried through solvent extraction with scCO2 in a 25 l autoclave leading to a porous material.
The gel-monolith was removed from the container and transferred to an autoclave. The autoclave was filled with >99 vol % of acetone, to fully cover the gel and then the lid closed. This prevents the gel from shrinking due to evaporating solvent, before the monolith gets in contact with sc. CO2. The gel was dried in a supercritical CO2 stream for 24 h. The pressure in the vessel was between 115-120 bar; the temperature was between 40-60° C. At the end of the drying step, the pressure of the system was reduced to 1 bar over 45 min at a temperature of 40° C. The autoclave was opened ant the monolith was removed. The thermal conductivity λ was measured according to DIN EN 12667 with a plate apparatuses from Hesto (Lambda Control A50). The thermal conductivity was 16.8 mW/m*K at 10° C. The density was 208 kg/m3.
In a polypropylene container, 48 g M200 and 8 g ME were dissolved under stirring in 220 g DEK at 20° C. leading to a clear solution. Similarly, 2 g Dabco K15 were dissolved in 220 g DEK to obtain a second solution. The solutions were combined in a rectangular container (20×20 cm×5 cm height) by pouring one solution into the other, which led to a clear, homogeneous mixture of low viscosity. The container was closed with a lid and the mixture was gelled at room temperature for 24 h. The resulting monolithic gel slab was dried through solvent extraction with scCO2 in a 25 l autoclave leading to a porous material.
The gel-monolith was removed from the container and transferred to an autoclave. The autoclave was filled with >99 vol % of acetone, to fully cover the gel and then the lid closed. This prevents the gel from shrinking due to evaporating solvent, before the monolith gets in contact with sc. CO2. The gel was dried in a supercritical CO2 stream for 24 h. The pressure in the vessel was between 115-120 bar; the temperature was between 40-60° C. At the end of the drying step, the pressure of the system was reduced to 1 bar over 45 min at a temperature of 40° C. The autoclave was opened ant the monolith was removed. The thermal conductivity λ was measured according to DIN EN 12667 with a plate apparatuses from Hesto (Lambda Control A50). The thermal conductivity was 17.2 mW/m*K at 10° C. The density was 216 kg/m3.
In a polypropylene container, 48 g M200 and 8 g MI were dissolved under stirring in 220 g DEK at 20° C. leading to a clear solution. Similarly, 2 g Dabco K15 were dissolved in 220 g DEK to obtain a second solution. The solutions were combined in a rectangular container (20×20 cm×5 cm height) by pouring one solution into the other, which led to a clear, homogeneous mixture of low viscosity. The container was closed with a lid and the mixture was gelled at room temperature for 24 h. The resulting monolithic gel slab was dried through solvent extraction with scCO2 in a 25 l autoclave leading to a porous material.
The gel-monolith was removed from the container and transferred to an autoclave. The autoclave was filled with >99 vol % of acetone, to fully cover the gel and then the lid closed. This prevents the gel from shrinking due to evaporating solvent, before the monolith gets in contact with sc. CO2. The gel was dried in a supercritical CO2 stream for 24 h. The pressure in the vessel was between 115-120 bar; the temperature was between 40-60° C. At the end of the drying step, the pressure of the system was reduced to 1 bar over 45 min at a temperature of 40° C. The autoclave was opened ant the monolith was removed. The thermal conductivity λ was measured according to DIN EN 12667 with a plate apparatuses from Hesto (Lambda Control A50). The thermal conductivity was 17.4 mW/m*K at 10° C. The density was 243 kg/m3.
H2O Water
K15 Dabco K15 (PUR catalyst)
M200 Lupranate M200 (polyisocyanate)
MI Lupranat MI (monomeric isocyanate)
ME Lupranat ME (monomeric isocyanate)
DEK Diethyl ketone
MEK Methyl ethyl ketone
MDEA 4,4′-Methylene-bis(2,6-diethylaniline)
| Number | Date | Country | Kind |
|---|---|---|---|
| 15186429.5 | Sep 2015 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2016/072127 | 9/19/2016 | WO | 00 |
