CA2212117A1 - Recycling of microcellular polyurethanes - Google Patents
Recycling of microcellular polyurethanesInfo
- Publication number
- CA2212117A1 CA2212117A1 CA002212117A CA2212117A CA2212117A1 CA 2212117 A1 CA2212117 A1 CA 2212117A1 CA 002212117 A CA002212117 A CA 002212117A CA 2212117 A CA2212117 A CA 2212117A CA 2212117 A1 CA2212117 A1 CA 2212117A1
- Authority
- CA
- Canada
- Prior art keywords
- polyurethanes
- weight
- prepolymer
- diisocyanate
- comminuted
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
- C08G18/76—Polyisocyanates or polyisothiocyanates cyclic aromatic
- C08G18/7657—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings
- C08G18/7678—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing condensed aromatic rings
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/10—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L75/00—Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
- C08L75/04—Polyurethanes
Abstract
Polyurethanes are recycled by comminution to particle sizes of from 0.01 to 2 mm and addition to the polyaddition mixture for preparing polyurethanes from (a) polyisocyanates, (b) substances reactive toward isocyanates and having active hydrogens, and, if desired, (c) chain extenders and/or crosslinkers, catalysts, blowing agents and customary additives in an amount of from 0.1 to 40% by weight, based on the polyaddition mixture.
Description
BASF Aktiengesellschaft 960429 O.Z. 0050/47220 Recycling of microcellular polyurethanes The present invention relates to a process for the recycling of 5 microcellular polyurethanes.
Chemical processes such as hydrolysis, hydrogenation, pyrolysis and glycolysis are suitable for the recycling of polyurethanes.
Furthermore, the polyurethanes can be dissolved in isocyanates 10 and the resulting mixture can, after purification, be reused (DE-A-43 16 389). Common to these processes is the fact that the polyurethanes can be reintroduced into their production process only at considerable expense and usually not without a loss of quality (eg. reduced isocyanate content in the component after 15 dissolution~.
Further processes for recycling comprise the preparation of com-pact polyurethanes from comminuted elastomers ("flake bonding") or use as filler material in the preparation of new components 20 ("Polyurethanes Recycling - Status Report", K.W. Kroesen and D.A.
Hicks, 1993, Cellular Polymers, paper 16, 1-6). Introduction of comminuted polyurethanes into the polyol component for preparing polyisocyanate polyaddition products is described in US 4 692 470, where air introduced with the polyurethanes caused 25 considerable problems which became apparent in an undesired in-crease in the viscosity. This problem was solved by wetting the comminuted polyurethanes with volatile hydrocarbons. The addition of these substances may be disadvantageous for systems in which these materials are not used as blowing agents and is to be 30 avoided. A loss in quality of the polyurethane which is prepared using recycled polyurethanes compared with the recycled elastomers can be avoided only with difficulty in the known processes, particularly in the case of microcellular polyurethane elastomers.
It is an object of the present invention to develop a process for the recycling of polyurethanes in which these can be reintroduced into the production process for preparing polyurethanes without losses in quality having to be accepted.
We have found that this object is achieved by comminuting the polyurethanes and using them in a first reaction step together with a mixture which comprises the comminuted polyurethanes in an amount of from 0.1 to 40% by weight, based on the polyaddition 45 mixture, BASF Aktiengesellschaft 960429 O.Z. 0050/47220 (a) polyisocyanates, (b) substances reactive toward isocyanates and containing active hydrogens, and, if desired, (c) chain extenders and/or crosslinkers, catalysts, blowing agents and customary additives, to prepare a prepolymer and in a second step reacting this prepo-lymer with water and, if desired, (c) to give the polyurethane.
The polyurethanes comminuted by known milling methods and having 15 a preferred particle size of from 0.01 to 2 mm, in particular from 0.1 to 2 mm, are preferably based on the components (a), (b) and, if used, (c) used in the polyaddition. According to the present invention, the proportion of comminuted polyurethanes can be from 0.1 to 40% by weight, preferably from 1 to 20% by weight, based 20 on the weight of the polyaddition reaction mixture.
The polyurethanes used generally have a cellular structure. Prefe-rence is given to using cellu]ar polyurethane elastomers, par-ticularly preferably microcellular polyurethane elastomers, in 25 particular ones which have the same structure as those which are obtainable from the starting materials (a), (b) and, if desired, (c) by a polyaddition reaction. This has the advantage that microcellular polyurethane elastomers can, owing to their out-standing damping properties together with an excellent volume 30 compressibility, be recycled for producing vibration- and shock-damper systems (for an overview of microcellular polyurethane elastomers see, for example: "Naphthalene 1,5-Diisocyanate as a Building Block for High Performance Polyurethane Elastomers", E.C. Prolingheuer, J.J. Lindsay and H. Kleimann, 1989, Journal of 35 Elastomers and Plastics, 21, 100-121). Particular preference is given to using microcellular polyurethane elastomers obtained as waste from the production process in which they are to be re-cycled.
40 Before use according to the present invention, the comminuted polyurethanes are dried sufficiently by known methods. Drying is usually carried out at from 80 to 150~C and is generally complete after from 1 to 24 hours.
45 To prepare the polyurethane elastomers, the substances (a) and (b) and the comminuted polyurethanes, if desired together with (c), are reacted with an equivalence ratio of NCO groups to the BASF Aktiengesellschaft 960429 O.Z. 0050/47220 sum of the reactive hydrogens of 0.8 to 1.2 : 1, preferably 0.95 to 1.1 : 1, by the one-shot process described in the litera-ture, at the generally customary temperatures of from 80 to 160~C, preferably from 90 to 150~C. The comminuted elastomers can be in-5 troduced into the component (b) or/and into a prepolymer, pre-ferably into the prepolymer, without prior wetting of the milled material with volatile substances as is necessary according to US
4 692 470. During the usual processing time of the prepolymer or the reaction mixture of 5 hours, an increase in viscosity or a 10 decrease in reactivity do not have an adverse effect on the pro-duction process.
Preference is given to employing the prepolymer process in which, in particular, isocyanate-containing prepolymers are used. These 15 can be prepared by reacting a mixture comprising the comminuted polyurethane elastomers and at least one organic polyisocyanate (a), at least one compound (b) which is reactive toward iso-cyanates and, if desired, (c). The prepolymers preferably have isocyanate contents of from 1 to 30% by weight, particularly pre-20 ferably from 3 to 15% by weight, based on the total weight. Thesynthesis of the prepolymer is usually carried out at from 80 to 160~C, preferably from 90 to 150~C. The reaction is generally com-plete after from 15 to 200 minutes. This prepolymer is subsequent-ly reacted in a mixture comprising the component (b) and, if de-25 sired, (c) and having an equivalence ratio of NCO groups to thesum of the reactive hydrogens of 0.8 to 1.2 : 1, preferably 0.95 to 1.1 : 1, to give the desired polyurethane elastomer.
Suitable substances (a) and (b) for preparing microcellular poly-30 urethane elastomers are the compounds known from polyurethane chemistry, about which the following may be said:
a) Polyisocyanates (a) used are aromatic, aliphatic or/and cycloaliphatic diisocyanates. Examples of aromatic diiso-cyanates are: naphthylene 1,5-diisocyanate (1,5-NDI), toly-lene 2,4- and 2,6- diisocyanate (TDI) and also their mixtures, diphenylmethane 2,4'-, 2,2'- and preferably 4,4'-diisocyanate (MDI) and also mixtures of at least two of these isomers, 3,3'-dimethylbiphenyl diisocyanate, eg.
3,3'-dimethyl-4,4'-diisocyanatebiphenyl, 1,2-diphenylethane diisocyanate and phenylene diisocyanate, preferably phenylene 1,4-diisocyanate ~PPDI). The aromatic isocyanates are used individually or as a mixture of at least two different iso-cyanates. Aliphatic, branched or preferably linear diiso-cyanates having from 4 to 12 carbon atoms, preferably from 4 to 6 carbon atoms, which may be mentioned are: dodecane 1,12-diisocyanate, 2-ethylbutane 1,4-diisocyanate, 2-methyl-BASF Aktiengesellschaft 960429 O.Z. 0050/47220 .
pentane 1,5-diisocyanate or/and butane 1,4-diisocyanate, pre-ferably hexamethylene 1,6-diisocyanate (HDI). Cycloaliphatic diisocyanates having from 6 to 18 carbon atoms, preferably from 6 to 12 carbon atoms, in the alkyl-substituted or non-alkyl-substituted cycloalkyl radical whlch can be used are, for example: cyclohexane 1,3- or/and 1,4-diisocyanate, hexahydrotolylene 2,4- or/and 2,6-diisocyanate, dicyclo-hexanemethane 4,4'-, 2,4'- or/and 2,2'-diisocyanate, prefera-bly 1-isocyanato- 3,3,5-trimethyl-5-isocyanatomethylcyclohex-ane (IPDI).
b) Compounds (b) which are reactive toward isocyanates usuallycomprise polyhydroxyl compounds having a functionality of from 2 to 3, preferably 2, and a molecular weight of from 500 to 6000 g/mol, preferably from 800 to 3500 g/mol, particular-ly preferably from 1000 to 3300 g/mol. Examples of compounds which can be used as (b) are: polyester polyols derived from organic dicarboxylic acids and/or dicarboxylic acid deriva-tives and dihydric or trihydric alcohols and/or dialkylene glycols, hydroxyl-containing polycarbonates, hydroxy-carboxylic acids or lactones, polyacetals such as polyoxyme-thylenes or water-insoluble formals such as polybutanediol formal or polyhexanediol formal, polyoxyalkylene polyols such as polyoxybutylene glycols, polyoxypropylene glycols, poly-oxybutylene-polyoxypropylene glycols, polyoxybutylene-poly-oxyethylene glycols and polyoxybutylene-polyoxypropylene-polyoxyethylene glycols or mixtures of at least two of the polyhydroxyl compounds mentioned. Preference is given to using difunctional polyhydroxyl compounds selected from the groups consisting of polyester polyols, hydroxyl-containing polycarbonates and polyoxybutylene glycols and also mixtures of at least two of these groups.
The polyhydroxyl compounds can be prepared by known methods.
otherwise, the reaction can be carried out under conditions known per se and using customary additives as described, for example, in EP-A-482 476. Thus, the customary known chain extenders (eg.
diamines and alkanolamines, preferably alkanediols having from 2 40 to 12 carbon atoms, particularly preferably having 2, 4 or 6 carbon atoms, and dialkylene glycols as well as polyoxyalkylene glycols), and/or at least trifunctional crosslinkers can be used in proportions by weight of from 5 to 50% by weight for preparing rigid polyurethane elastomers, preferably from 30 to 50% by 45 weight, based on the component (b). Furthermore, the known blow-ing agents such as materials having a boiling point at atmos-pheric pressure in the range from -40~C to 120~C, gases and also BASF Aktiengesellschaft 960429 O.Z. 0050/47220 solid blowing agents and water, the customary catalysts such as inorganic and organic tin compounds and strongly basic amines, eg. in proportions of from 0.001 to 3~ by weight, in particular from 0.01 to 1% by weight, based on the weight of the components 5 ~a) and (b), the chain extenders and crosslinkers and also the comminuted polyurethane elastomers, and customary additives can be used. The additives can comprise, for example: surface-active substances, foam stabilizers, cell regulators, fillers, flame retardants, nucleated agents, oxidation inhibitors, stabilizers, 10 lubricants and mold release agents, dyes and pigments. Further details regarding the customary basic starting materials, auxiliaries and additives may be found in the specialist literature (see, inter alia "Kunststoff-Handbuch", Volume 7, Polyurethane, 2nd edition, 1983, edited by G. Oertel, Carl Hanser 15 Verlag, Munich).
The microcellular polyurethane elastomers prepared by the process of the present invention have densities of from 0.35 to 0.80 g/cm3 and are used for producing moldings which, owing to their very 20 good damping properties are employed, inter alia, for spring and damping elements, eg. in vehicles and in machine construction.
The microcellular polyurethane elastomers prepared according to the present invention with comminuted microcellular polyurethane 25 elastomers being incorporated into the reaction mixture and reacted therein have unexpectedly excellent static and dynamic properties which correspond to those of comparison products which have been prepared without the recycled elastomers.
30 This is demonstrated by means of the following examples:
Examples Comparative Example I
a) Preparation of a prepolymer containing isocyanate groups and based on 1,5-NDI
1000 g (0.5 mol) of a polyethanediol adipate having an average molecular weight of 2000 (calculated from the experimentally determined hydroxyl number) were heated to 140~C and at this temperature admixed and reacted with 240 g (1.14 mol) of solid l,5-NDI while stirring vigorously.
BASF Aktiengesellschaft 960429 O.Z. 0050/47220 This gave a prepolymer having an NCO content of 4.20% by weight and a viscosity at 90~C of 2300 mPas (measured using a rotation viscometer from Haake, by means of which the visco-sities in the following examples are also measured).
b) Production of cellular moldings The crosslinker component comprised 20.7 parts by weight of 2,2', 6,6'-tetraisopropyldiphenyl-carbodiimide 2.9 parts by weight of a mixture of ethoxylated oleic and ricinoleic acids having an average of 9 oxyethylene units 3.8 parts by weight of the monoethanolamine salt of n-alkylbenzenesulfonic acid having Cg-Cl5-alkyl radicals 36.3 parts by weight of the sodium salt of sulfated castor oil 36.3 parts by weight of water and 0.03 parts by weight of a mixture of 30% by weight of pentamethyldiethylenetriamine and 70% by weight of N-methyl-N'-(dimethylaminomethyl)-plperaz lne .
200 g of the isocyanate prepolymer prepared as described in Comparative Example Ia and heated to 90~C were stirred vigor-ously for about 8 seconds with 4.64 g of the crosslinker com-ponent. The reaction mixture was then introduced into a closable metal mold heated to 80~C, the mold was closed and the reaction mixture was allowed to cure. After 25 minutes, the microcellular molding was removed from the mold and heated for 16 hours at 110~C for further thermal curing.
Example 1 a) Preparation of a prepolymer containing isocyanate groups and based on 1,5-NDI together with 4% of milled material BASF Aktiengesellschaft 960429 O.Z. 0050/47220 1000 g (0.5 mol) of a polyethanediol adipate having an aver-age molecular weight of 2000 (calculated from the experiment-ally determined hydroxyl number) were heated to 140~C and at this temperature admixed and reacted with 240 g (1.14 mol) of solid 1,5-NDI while stirring vigorously. After cooling to 90~C, the prepolymer was admixed while stirring with 49.6 g of a comminuted microcellular polyurethane elastomer based on 1,5-NDI and prepared as described in Comparative Example I
(average particle size 500 llm, dried for 6 hours at 120~C).
This gave a prepolymer having an NCO content of 3.95% by weight and a viscosity of 3600 mPas.
b) Production of cellular moldings Moldings were produced by a method similar to that described in Comparative Example I from 100 parts by weight of the pre-polymer described in Example Ia and 4.36 parts by weight of the crosslin]cer component described in Comparative Example Ib. The moldings were removed from the mold after 30 minutes and were heated for 16 hours at 110~C for further thermal curing.
Example 2 a) Preparation of a prepolymer containing isocyanate groups and based on l,5-NDI together with 6% of milled material 10~0 g (0.5 mol) of a polyethanediol adipate having an aver-age molecular weight of 2000 (calculated from the experiment-ally determined hydroxyl number) were heated to 140~C at and this temperature admixed and reacted with 240 g (1.14 mol) of solid 1,5-NDI while stirring vigorously. After cooling to 90~C, the prepolymer was admixed while stirring with 74.4 g of a comminuted microcellular polyurethane elastomer based on 1,5-NDI and prepared as described in Comparative Example I
(average particle size 500 ~m, dried for 6 hours at 120~C).
This gave a prepolymer having an NCO content of 3.89% by weight and a viscosity at 90~C of 3700 mPas.
b) Production of cellular moldings Moldings were produced by a method similar to that described in Comparative Example I from 200 parts by weight of the pre-polymer described in Example 2a and 4.28 parts by weight of the crosslinker component described in Comparative Example BASF Aktiengesellschaft 960429 O.Z. 0050/47220 Ib. The moldings were removed from the mold after 30 minutes and heated for 16 hours at llO~C for further thermal curing.
Example 3 a) Preparation of a prepolymer containing isocyanate groups and based on l,5-NDI together with 8% of milled material 1000 g (0.5 mol) of a polyethanediol adipate having an aver-age molecular weight of 2000 (calculated from the experiment-ally determined hydroxyl number) were heated to 140~C and at this temperature admixed and reacted with 240 g (1.14 mol) of solid 1,5-NDI while stirring viqorously. After cooling to 90~C, the prepolymer was admixed while stirring with 99.2 g of a comminuted microcellular polyurethane elastomer based on 1,5-NDI and prepared as described in Comparative Example I
(average particle size 500 llm, dried for 6 hours at 120~C).
This gave a prepolymer having an NCO content of 3.83~ by weight and a viscosity at 90~C of 3800 mPas.
b) Production of cellular moldings Moldings were produced by a method similar to that described in Comparative Example I from 200 parts by weight of the pre-polymer described in Example 3a and 4.2 parts by weight of the crosslinker component described in Comparative Example Ib. The moldings were removed from the mold after 30 minutes and heated for 16 hours at 110~C for further thermal curing.
Example 4 35 a) Preparation of a prepolymer containing isocyanate groups and based on 1,5-NDI together with 4% of milled material 1000 g (0.5 mol) of a polyethanediol adipate having an aver-age molecular weight of 2000 (calculated from the experiment-ally determined hydroxyl number) were heated to 130~C and at this temperature admixed while stirring vigorously with 49.6 g of a comminuted microcellular polyurethane elastomer based on 1,5-NDI and prepared as described in Comparative Example I (average particle size 500~m, dried for 6 hours at 120~C). The mixture was heated to 140~C and at this tempera-BASF Aktiengesellschaft 960429 O.Z. 0050/47220 ture admixed and reacted with 240 g (1.14 mol~ of solid 1,5-NDI while stirring vigorously.
This gave a prepolymer having an NCO content of 3.97~ by weight and a viscosity at 90~C of 3200 mPas.
b) Production of cellular moldings Moldings were produced by a method similar to that described in Comparative Example I from 200 parts by weight of the pre-polymer described in Example 4a and 4.32 parts by weight of the crosslinker component described in Comparative Example Ib. The moldings were removed from the mold after 30 minutes and heated for 16 hours at 110~C for further thermal curing.
Example 5 a) Preparation of a prepolymer containing isocyanate groups and based on l,5-NDI together with 4$ of milled material 1000 g (0.5 mol) of a polyethanediol adipate having an aver-age molecular weight of 2000 (calculated from the experiment-ally determined hydroxyl number) were heated to 140~C and at this temperature admixed and reacted with 240 g (1.14 mol) of solid 1,5-NDI while stirring vigorously. At a temperature of 130~C the prepolymer was admixed while stirring with 49.6 g of a comminuted microcellular polyurethane elastomer based on 1,5-NDI and prepared as described in Comparative Example I
(avera~ge particle size 500 llm, dried for 6 hours at 120~C).
This gave a prepolymer having an NCO content of 3.97~~ by weight and a viscosity at 90~C of 3300 mPas.
b) Production of cellular moldings Moldings were produced by a method similar to that described in Comparative Example I from 200 parts by weight of the pre-polymer described in Example 5a and 4.38 parts by weight of the crosslinker component described in Comparative Example Ib. The moldings were removed from the mold after 30 minutes and heated for 16 hours at 110~C for further thermal curing.
The cellular moldings produced as described in the Comparative Example and Examples 1 to 5 were used to measure the static and 45 dynamic mechanical properties of the microcellular PU elastomers.
BASF Aktiengesellschaft 960429 O.Z. 0050/47220 The static mechanical properties measured were the tensile strength in accordance with DIN 53 571, the elongation at break in accordance with DIN 53 571, the tear propagation resistance in accordance with DIN 53 515 and the compressive set at 80~C by a 5 modification of DIN 53 572 using 18 mm high spacers and test specimens having a base area of 40 x 40 mm and a height of 30 + 1 mm. The compressive set (CS) was calculated according to the equation Ho - H2 CS = Ho - Hl 1OO [%]
where Ho is the original height of the test specimen in mm, H1 is the height of the test specimen in the deformed state in mm and H2 is the height of the test specimen after decompression in mm.
The dynamic mechanical properties were determined using the dis-placement increase (DI) at maximum force and the consolidation (CN). The molding for measuring the consolidation was a cylindri-cal test spring having 3 segment constrictions and a height of 25 100 mm, an external diameter of 50 mm and an internal diameter of 10 mm. After loading the spring over 100,000 load cycles at a force of 6 kN and a frequency of 1. 2 HZ, the CN was measured as the difference between the initial and final heights of the test spring and is reported in percent. The consolidation is a measure 30 of the permanent deformation of the cellular PU elastomers during the cyclic fatigue test. The lower this consolidation, the better the dynamic performance of the material.
The height HR for determining the consolidation after the dynamic 35 test is determined after recording the characteristic line of the spring: HO is the initial height; the molding is precompressed 3x using the maximum force (maximum force for the characteristic lines) and the characteristic line is then recorded in the 4th cycle at a compression rate of 50 mm/min. After 10 minutes, H
40 is determined; this is the height of the component after record-ing the characteristic line. Only then is the dynamic test com-menced.
HR = residual height after the dynamic test measured after storage 45 for 24 hours at 23~C/50% relative atmospheric humidity after the end of the dynamic test. The reference point (=initial height) used for determining the permanent consolidation after the BASF Aktiengesellschaft 960429 O.Z. 0050/47220 dynamic test is HO, the height of the spring in a completely "as new" condition, without any compression:
HO ~ HR X 100 [%]
HO
The dynamic test was carried out without additional cooling in an air conditioned room at 23~C and 50% relative atmospheric humid-ity. The mechanical properties measured on the test specimens are 10 summarized in the following table.
The static and dynamic mechanical properties of the cellular polyurethane (PU) elastomers of the present invention show no differences in comparison with the elastomers prepared in the 15 comparative experiment. Thus, as shown in Table 1, the properties such as compressive set, tensile strength, elongation, tear propagation resistance, consolidation and displacement increase for Examples 1 to 5 correspond to those for Comparative Example I.
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Chemical processes such as hydrolysis, hydrogenation, pyrolysis and glycolysis are suitable for the recycling of polyurethanes.
Furthermore, the polyurethanes can be dissolved in isocyanates 10 and the resulting mixture can, after purification, be reused (DE-A-43 16 389). Common to these processes is the fact that the polyurethanes can be reintroduced into their production process only at considerable expense and usually not without a loss of quality (eg. reduced isocyanate content in the component after 15 dissolution~.
Further processes for recycling comprise the preparation of com-pact polyurethanes from comminuted elastomers ("flake bonding") or use as filler material in the preparation of new components 20 ("Polyurethanes Recycling - Status Report", K.W. Kroesen and D.A.
Hicks, 1993, Cellular Polymers, paper 16, 1-6). Introduction of comminuted polyurethanes into the polyol component for preparing polyisocyanate polyaddition products is described in US 4 692 470, where air introduced with the polyurethanes caused 25 considerable problems which became apparent in an undesired in-crease in the viscosity. This problem was solved by wetting the comminuted polyurethanes with volatile hydrocarbons. The addition of these substances may be disadvantageous for systems in which these materials are not used as blowing agents and is to be 30 avoided. A loss in quality of the polyurethane which is prepared using recycled polyurethanes compared with the recycled elastomers can be avoided only with difficulty in the known processes, particularly in the case of microcellular polyurethane elastomers.
It is an object of the present invention to develop a process for the recycling of polyurethanes in which these can be reintroduced into the production process for preparing polyurethanes without losses in quality having to be accepted.
We have found that this object is achieved by comminuting the polyurethanes and using them in a first reaction step together with a mixture which comprises the comminuted polyurethanes in an amount of from 0.1 to 40% by weight, based on the polyaddition 45 mixture, BASF Aktiengesellschaft 960429 O.Z. 0050/47220 (a) polyisocyanates, (b) substances reactive toward isocyanates and containing active hydrogens, and, if desired, (c) chain extenders and/or crosslinkers, catalysts, blowing agents and customary additives, to prepare a prepolymer and in a second step reacting this prepo-lymer with water and, if desired, (c) to give the polyurethane.
The polyurethanes comminuted by known milling methods and having 15 a preferred particle size of from 0.01 to 2 mm, in particular from 0.1 to 2 mm, are preferably based on the components (a), (b) and, if used, (c) used in the polyaddition. According to the present invention, the proportion of comminuted polyurethanes can be from 0.1 to 40% by weight, preferably from 1 to 20% by weight, based 20 on the weight of the polyaddition reaction mixture.
The polyurethanes used generally have a cellular structure. Prefe-rence is given to using cellu]ar polyurethane elastomers, par-ticularly preferably microcellular polyurethane elastomers, in 25 particular ones which have the same structure as those which are obtainable from the starting materials (a), (b) and, if desired, (c) by a polyaddition reaction. This has the advantage that microcellular polyurethane elastomers can, owing to their out-standing damping properties together with an excellent volume 30 compressibility, be recycled for producing vibration- and shock-damper systems (for an overview of microcellular polyurethane elastomers see, for example: "Naphthalene 1,5-Diisocyanate as a Building Block for High Performance Polyurethane Elastomers", E.C. Prolingheuer, J.J. Lindsay and H. Kleimann, 1989, Journal of 35 Elastomers and Plastics, 21, 100-121). Particular preference is given to using microcellular polyurethane elastomers obtained as waste from the production process in which they are to be re-cycled.
40 Before use according to the present invention, the comminuted polyurethanes are dried sufficiently by known methods. Drying is usually carried out at from 80 to 150~C and is generally complete after from 1 to 24 hours.
45 To prepare the polyurethane elastomers, the substances (a) and (b) and the comminuted polyurethanes, if desired together with (c), are reacted with an equivalence ratio of NCO groups to the BASF Aktiengesellschaft 960429 O.Z. 0050/47220 sum of the reactive hydrogens of 0.8 to 1.2 : 1, preferably 0.95 to 1.1 : 1, by the one-shot process described in the litera-ture, at the generally customary temperatures of from 80 to 160~C, preferably from 90 to 150~C. The comminuted elastomers can be in-5 troduced into the component (b) or/and into a prepolymer, pre-ferably into the prepolymer, without prior wetting of the milled material with volatile substances as is necessary according to US
4 692 470. During the usual processing time of the prepolymer or the reaction mixture of 5 hours, an increase in viscosity or a 10 decrease in reactivity do not have an adverse effect on the pro-duction process.
Preference is given to employing the prepolymer process in which, in particular, isocyanate-containing prepolymers are used. These 15 can be prepared by reacting a mixture comprising the comminuted polyurethane elastomers and at least one organic polyisocyanate (a), at least one compound (b) which is reactive toward iso-cyanates and, if desired, (c). The prepolymers preferably have isocyanate contents of from 1 to 30% by weight, particularly pre-20 ferably from 3 to 15% by weight, based on the total weight. Thesynthesis of the prepolymer is usually carried out at from 80 to 160~C, preferably from 90 to 150~C. The reaction is generally com-plete after from 15 to 200 minutes. This prepolymer is subsequent-ly reacted in a mixture comprising the component (b) and, if de-25 sired, (c) and having an equivalence ratio of NCO groups to thesum of the reactive hydrogens of 0.8 to 1.2 : 1, preferably 0.95 to 1.1 : 1, to give the desired polyurethane elastomer.
Suitable substances (a) and (b) for preparing microcellular poly-30 urethane elastomers are the compounds known from polyurethane chemistry, about which the following may be said:
a) Polyisocyanates (a) used are aromatic, aliphatic or/and cycloaliphatic diisocyanates. Examples of aromatic diiso-cyanates are: naphthylene 1,5-diisocyanate (1,5-NDI), toly-lene 2,4- and 2,6- diisocyanate (TDI) and also their mixtures, diphenylmethane 2,4'-, 2,2'- and preferably 4,4'-diisocyanate (MDI) and also mixtures of at least two of these isomers, 3,3'-dimethylbiphenyl diisocyanate, eg.
3,3'-dimethyl-4,4'-diisocyanatebiphenyl, 1,2-diphenylethane diisocyanate and phenylene diisocyanate, preferably phenylene 1,4-diisocyanate ~PPDI). The aromatic isocyanates are used individually or as a mixture of at least two different iso-cyanates. Aliphatic, branched or preferably linear diiso-cyanates having from 4 to 12 carbon atoms, preferably from 4 to 6 carbon atoms, which may be mentioned are: dodecane 1,12-diisocyanate, 2-ethylbutane 1,4-diisocyanate, 2-methyl-BASF Aktiengesellschaft 960429 O.Z. 0050/47220 .
pentane 1,5-diisocyanate or/and butane 1,4-diisocyanate, pre-ferably hexamethylene 1,6-diisocyanate (HDI). Cycloaliphatic diisocyanates having from 6 to 18 carbon atoms, preferably from 6 to 12 carbon atoms, in the alkyl-substituted or non-alkyl-substituted cycloalkyl radical whlch can be used are, for example: cyclohexane 1,3- or/and 1,4-diisocyanate, hexahydrotolylene 2,4- or/and 2,6-diisocyanate, dicyclo-hexanemethane 4,4'-, 2,4'- or/and 2,2'-diisocyanate, prefera-bly 1-isocyanato- 3,3,5-trimethyl-5-isocyanatomethylcyclohex-ane (IPDI).
b) Compounds (b) which are reactive toward isocyanates usuallycomprise polyhydroxyl compounds having a functionality of from 2 to 3, preferably 2, and a molecular weight of from 500 to 6000 g/mol, preferably from 800 to 3500 g/mol, particular-ly preferably from 1000 to 3300 g/mol. Examples of compounds which can be used as (b) are: polyester polyols derived from organic dicarboxylic acids and/or dicarboxylic acid deriva-tives and dihydric or trihydric alcohols and/or dialkylene glycols, hydroxyl-containing polycarbonates, hydroxy-carboxylic acids or lactones, polyacetals such as polyoxyme-thylenes or water-insoluble formals such as polybutanediol formal or polyhexanediol formal, polyoxyalkylene polyols such as polyoxybutylene glycols, polyoxypropylene glycols, poly-oxybutylene-polyoxypropylene glycols, polyoxybutylene-poly-oxyethylene glycols and polyoxybutylene-polyoxypropylene-polyoxyethylene glycols or mixtures of at least two of the polyhydroxyl compounds mentioned. Preference is given to using difunctional polyhydroxyl compounds selected from the groups consisting of polyester polyols, hydroxyl-containing polycarbonates and polyoxybutylene glycols and also mixtures of at least two of these groups.
The polyhydroxyl compounds can be prepared by known methods.
otherwise, the reaction can be carried out under conditions known per se and using customary additives as described, for example, in EP-A-482 476. Thus, the customary known chain extenders (eg.
diamines and alkanolamines, preferably alkanediols having from 2 40 to 12 carbon atoms, particularly preferably having 2, 4 or 6 carbon atoms, and dialkylene glycols as well as polyoxyalkylene glycols), and/or at least trifunctional crosslinkers can be used in proportions by weight of from 5 to 50% by weight for preparing rigid polyurethane elastomers, preferably from 30 to 50% by 45 weight, based on the component (b). Furthermore, the known blow-ing agents such as materials having a boiling point at atmos-pheric pressure in the range from -40~C to 120~C, gases and also BASF Aktiengesellschaft 960429 O.Z. 0050/47220 solid blowing agents and water, the customary catalysts such as inorganic and organic tin compounds and strongly basic amines, eg. in proportions of from 0.001 to 3~ by weight, in particular from 0.01 to 1% by weight, based on the weight of the components 5 ~a) and (b), the chain extenders and crosslinkers and also the comminuted polyurethane elastomers, and customary additives can be used. The additives can comprise, for example: surface-active substances, foam stabilizers, cell regulators, fillers, flame retardants, nucleated agents, oxidation inhibitors, stabilizers, 10 lubricants and mold release agents, dyes and pigments. Further details regarding the customary basic starting materials, auxiliaries and additives may be found in the specialist literature (see, inter alia "Kunststoff-Handbuch", Volume 7, Polyurethane, 2nd edition, 1983, edited by G. Oertel, Carl Hanser 15 Verlag, Munich).
The microcellular polyurethane elastomers prepared by the process of the present invention have densities of from 0.35 to 0.80 g/cm3 and are used for producing moldings which, owing to their very 20 good damping properties are employed, inter alia, for spring and damping elements, eg. in vehicles and in machine construction.
The microcellular polyurethane elastomers prepared according to the present invention with comminuted microcellular polyurethane 25 elastomers being incorporated into the reaction mixture and reacted therein have unexpectedly excellent static and dynamic properties which correspond to those of comparison products which have been prepared without the recycled elastomers.
30 This is demonstrated by means of the following examples:
Examples Comparative Example I
a) Preparation of a prepolymer containing isocyanate groups and based on 1,5-NDI
1000 g (0.5 mol) of a polyethanediol adipate having an average molecular weight of 2000 (calculated from the experimentally determined hydroxyl number) were heated to 140~C and at this temperature admixed and reacted with 240 g (1.14 mol) of solid l,5-NDI while stirring vigorously.
BASF Aktiengesellschaft 960429 O.Z. 0050/47220 This gave a prepolymer having an NCO content of 4.20% by weight and a viscosity at 90~C of 2300 mPas (measured using a rotation viscometer from Haake, by means of which the visco-sities in the following examples are also measured).
b) Production of cellular moldings The crosslinker component comprised 20.7 parts by weight of 2,2', 6,6'-tetraisopropyldiphenyl-carbodiimide 2.9 parts by weight of a mixture of ethoxylated oleic and ricinoleic acids having an average of 9 oxyethylene units 3.8 parts by weight of the monoethanolamine salt of n-alkylbenzenesulfonic acid having Cg-Cl5-alkyl radicals 36.3 parts by weight of the sodium salt of sulfated castor oil 36.3 parts by weight of water and 0.03 parts by weight of a mixture of 30% by weight of pentamethyldiethylenetriamine and 70% by weight of N-methyl-N'-(dimethylaminomethyl)-plperaz lne .
200 g of the isocyanate prepolymer prepared as described in Comparative Example Ia and heated to 90~C were stirred vigor-ously for about 8 seconds with 4.64 g of the crosslinker com-ponent. The reaction mixture was then introduced into a closable metal mold heated to 80~C, the mold was closed and the reaction mixture was allowed to cure. After 25 minutes, the microcellular molding was removed from the mold and heated for 16 hours at 110~C for further thermal curing.
Example 1 a) Preparation of a prepolymer containing isocyanate groups and based on 1,5-NDI together with 4% of milled material BASF Aktiengesellschaft 960429 O.Z. 0050/47220 1000 g (0.5 mol) of a polyethanediol adipate having an aver-age molecular weight of 2000 (calculated from the experiment-ally determined hydroxyl number) were heated to 140~C and at this temperature admixed and reacted with 240 g (1.14 mol) of solid 1,5-NDI while stirring vigorously. After cooling to 90~C, the prepolymer was admixed while stirring with 49.6 g of a comminuted microcellular polyurethane elastomer based on 1,5-NDI and prepared as described in Comparative Example I
(average particle size 500 llm, dried for 6 hours at 120~C).
This gave a prepolymer having an NCO content of 3.95% by weight and a viscosity of 3600 mPas.
b) Production of cellular moldings Moldings were produced by a method similar to that described in Comparative Example I from 100 parts by weight of the pre-polymer described in Example Ia and 4.36 parts by weight of the crosslin]cer component described in Comparative Example Ib. The moldings were removed from the mold after 30 minutes and were heated for 16 hours at 110~C for further thermal curing.
Example 2 a) Preparation of a prepolymer containing isocyanate groups and based on l,5-NDI together with 6% of milled material 10~0 g (0.5 mol) of a polyethanediol adipate having an aver-age molecular weight of 2000 (calculated from the experiment-ally determined hydroxyl number) were heated to 140~C at and this temperature admixed and reacted with 240 g (1.14 mol) of solid 1,5-NDI while stirring vigorously. After cooling to 90~C, the prepolymer was admixed while stirring with 74.4 g of a comminuted microcellular polyurethane elastomer based on 1,5-NDI and prepared as described in Comparative Example I
(average particle size 500 ~m, dried for 6 hours at 120~C).
This gave a prepolymer having an NCO content of 3.89% by weight and a viscosity at 90~C of 3700 mPas.
b) Production of cellular moldings Moldings were produced by a method similar to that described in Comparative Example I from 200 parts by weight of the pre-polymer described in Example 2a and 4.28 parts by weight of the crosslinker component described in Comparative Example BASF Aktiengesellschaft 960429 O.Z. 0050/47220 Ib. The moldings were removed from the mold after 30 minutes and heated for 16 hours at llO~C for further thermal curing.
Example 3 a) Preparation of a prepolymer containing isocyanate groups and based on l,5-NDI together with 8% of milled material 1000 g (0.5 mol) of a polyethanediol adipate having an aver-age molecular weight of 2000 (calculated from the experiment-ally determined hydroxyl number) were heated to 140~C and at this temperature admixed and reacted with 240 g (1.14 mol) of solid 1,5-NDI while stirring viqorously. After cooling to 90~C, the prepolymer was admixed while stirring with 99.2 g of a comminuted microcellular polyurethane elastomer based on 1,5-NDI and prepared as described in Comparative Example I
(average particle size 500 llm, dried for 6 hours at 120~C).
This gave a prepolymer having an NCO content of 3.83~ by weight and a viscosity at 90~C of 3800 mPas.
b) Production of cellular moldings Moldings were produced by a method similar to that described in Comparative Example I from 200 parts by weight of the pre-polymer described in Example 3a and 4.2 parts by weight of the crosslinker component described in Comparative Example Ib. The moldings were removed from the mold after 30 minutes and heated for 16 hours at 110~C for further thermal curing.
Example 4 35 a) Preparation of a prepolymer containing isocyanate groups and based on 1,5-NDI together with 4% of milled material 1000 g (0.5 mol) of a polyethanediol adipate having an aver-age molecular weight of 2000 (calculated from the experiment-ally determined hydroxyl number) were heated to 130~C and at this temperature admixed while stirring vigorously with 49.6 g of a comminuted microcellular polyurethane elastomer based on 1,5-NDI and prepared as described in Comparative Example I (average particle size 500~m, dried for 6 hours at 120~C). The mixture was heated to 140~C and at this tempera-BASF Aktiengesellschaft 960429 O.Z. 0050/47220 ture admixed and reacted with 240 g (1.14 mol~ of solid 1,5-NDI while stirring vigorously.
This gave a prepolymer having an NCO content of 3.97~ by weight and a viscosity at 90~C of 3200 mPas.
b) Production of cellular moldings Moldings were produced by a method similar to that described in Comparative Example I from 200 parts by weight of the pre-polymer described in Example 4a and 4.32 parts by weight of the crosslinker component described in Comparative Example Ib. The moldings were removed from the mold after 30 minutes and heated for 16 hours at 110~C for further thermal curing.
Example 5 a) Preparation of a prepolymer containing isocyanate groups and based on l,5-NDI together with 4$ of milled material 1000 g (0.5 mol) of a polyethanediol adipate having an aver-age molecular weight of 2000 (calculated from the experiment-ally determined hydroxyl number) were heated to 140~C and at this temperature admixed and reacted with 240 g (1.14 mol) of solid 1,5-NDI while stirring vigorously. At a temperature of 130~C the prepolymer was admixed while stirring with 49.6 g of a comminuted microcellular polyurethane elastomer based on 1,5-NDI and prepared as described in Comparative Example I
(avera~ge particle size 500 llm, dried for 6 hours at 120~C).
This gave a prepolymer having an NCO content of 3.97~~ by weight and a viscosity at 90~C of 3300 mPas.
b) Production of cellular moldings Moldings were produced by a method similar to that described in Comparative Example I from 200 parts by weight of the pre-polymer described in Example 5a and 4.38 parts by weight of the crosslinker component described in Comparative Example Ib. The moldings were removed from the mold after 30 minutes and heated for 16 hours at 110~C for further thermal curing.
The cellular moldings produced as described in the Comparative Example and Examples 1 to 5 were used to measure the static and 45 dynamic mechanical properties of the microcellular PU elastomers.
BASF Aktiengesellschaft 960429 O.Z. 0050/47220 The static mechanical properties measured were the tensile strength in accordance with DIN 53 571, the elongation at break in accordance with DIN 53 571, the tear propagation resistance in accordance with DIN 53 515 and the compressive set at 80~C by a 5 modification of DIN 53 572 using 18 mm high spacers and test specimens having a base area of 40 x 40 mm and a height of 30 + 1 mm. The compressive set (CS) was calculated according to the equation Ho - H2 CS = Ho - Hl 1OO [%]
where Ho is the original height of the test specimen in mm, H1 is the height of the test specimen in the deformed state in mm and H2 is the height of the test specimen after decompression in mm.
The dynamic mechanical properties were determined using the dis-placement increase (DI) at maximum force and the consolidation (CN). The molding for measuring the consolidation was a cylindri-cal test spring having 3 segment constrictions and a height of 25 100 mm, an external diameter of 50 mm and an internal diameter of 10 mm. After loading the spring over 100,000 load cycles at a force of 6 kN and a frequency of 1. 2 HZ, the CN was measured as the difference between the initial and final heights of the test spring and is reported in percent. The consolidation is a measure 30 of the permanent deformation of the cellular PU elastomers during the cyclic fatigue test. The lower this consolidation, the better the dynamic performance of the material.
The height HR for determining the consolidation after the dynamic 35 test is determined after recording the characteristic line of the spring: HO is the initial height; the molding is precompressed 3x using the maximum force (maximum force for the characteristic lines) and the characteristic line is then recorded in the 4th cycle at a compression rate of 50 mm/min. After 10 minutes, H
40 is determined; this is the height of the component after record-ing the characteristic line. Only then is the dynamic test com-menced.
HR = residual height after the dynamic test measured after storage 45 for 24 hours at 23~C/50% relative atmospheric humidity after the end of the dynamic test. The reference point (=initial height) used for determining the permanent consolidation after the BASF Aktiengesellschaft 960429 O.Z. 0050/47220 dynamic test is HO, the height of the spring in a completely "as new" condition, without any compression:
HO ~ HR X 100 [%]
HO
The dynamic test was carried out without additional cooling in an air conditioned room at 23~C and 50% relative atmospheric humid-ity. The mechanical properties measured on the test specimens are 10 summarized in the following table.
The static and dynamic mechanical properties of the cellular polyurethane (PU) elastomers of the present invention show no differences in comparison with the elastomers prepared in the 15 comparative experiment. Thus, as shown in Table 1, the properties such as compressive set, tensile strength, elongation, tear propagation resistance, consolidation and displacement increase for Examples 1 to 5 correspond to those for Comparative Example I.
BASF AktiengeSe11SC1C1A 0L212117~19U9~7-08-18 O.Z. 0050/47220 ~V Ln u~
, O ~~ ~ O
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,~o ~ 0~ 0 a' ~ ~
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h o Ul O ~ o ~D
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J - a~
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a) o ~ ~ -rl ~ Q~ V ~ r.~ ~ I
C) ~ ~ ~ ~n u ~V ~ 4 Ll, '~ O '~ C I--n s~ ~ u O u~ rd ~ rd ~ L u ~ z ~ ~ , a) z; ~, c -~
Claims (6)
1. A process for the recycling of microcellular polyurethanes, which comprises comminuting the polyurethanes and using them in a first reaction step together with a mixture which comprises the comminuted polyurethanes in an amount of from 0.1 to 40% by weight, based on the polyaddition mixture, (a) polyisocyanates, (b) substances reactive toward isocyanates and containing active hydrogens, and, if desired, (c) chain extenders and/or crosslinkers, catalysts, blowing agents and customary additives, to prepare a prepolymer and in a second step reacting this prepolymer with water and, if desired, (c) to give the polyurethane.
2. A process as claimed in claim 1, wherein the comminuted polyurethanes have a particle size of from 0.01 to 2 mm.
3. A process as claimed in claim 1, wherein the comminuted polyurethanes used are microcellular polyurethane elastomers which have the same structure as the polyurethanes obtainable from the starting materials (a), (b) and, if desired, (c) by a polyaddition reaction.
4. A process as claimed in claim 1, wherein the prepolymer has an NCO content of from 1 to 30% by weight.
5. A process as claimed in claim 1, wherein the polyisocyanates (a) used are tolylene diisocyanate, diphenylmethane diisocyanate, 3,3'-dimethyl-4,4'-diisocyanatobiphenyl, an aliphatic diisocyanate having from 4 to 12 carbon atoms or a cycloaliphatic diisocyanate having from 6 to 18 carbon atoms, or naphthylene 1,5-diisocyanate.
6. A process as claimed in claim 1, wherein the component (b) used comprises polyhydroxyl compounds having a functionality of from 2 to 3 and a molecular weight of from 500 to 6000 g/mol.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19633891A DE19633891A1 (en) | 1996-08-22 | 1996-08-22 | Processes for the reuse of polyurethanes |
| DE19633891.3 | 1996-08-22 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2212117A1 true CA2212117A1 (en) | 1998-02-22 |
Family
ID=7803363
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002212117A Abandoned CA2212117A1 (en) | 1996-08-22 | 1997-08-18 | Recycling of microcellular polyurethanes |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US5891927A (en) |
| EP (1) | EP0826705B1 (en) |
| JP (1) | JPH1095825A (en) |
| AT (1) | ATE268789T1 (en) |
| BR (1) | BR9704473A (en) |
| CA (1) | CA2212117A1 (en) |
| DE (2) | DE19633891A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110684501A (en) * | 2019-09-25 | 2020-01-14 | 郑州骏惠材料技术有限公司 | Polyurethane hard foam powder filled single-component polyurethane sealant and preparation method thereof |
Families Citing this family (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6258867B1 (en) * | 1999-07-23 | 2001-07-10 | Bayer Corporation | Method for making semi-rigid energy-absorbing foam with polyurethane fillers |
| DE60028905D1 (en) * | 1999-11-16 | 2006-08-03 | C U E | High performance microcellular foam and manufacturing method and apparatus therefor |
| EP1242517B1 (en) * | 1999-12-23 | 2005-03-02 | Mobius Technologies, Inc. | Polymeric foam processing |
| US20040058163A1 (en) * | 2000-05-18 | 2004-03-25 | Peter Gansen | Composite material |
| MY131962A (en) * | 2001-01-24 | 2007-09-28 | Nichia Corp | Light emitting diode, optical semiconductor device, epoxy resin composition suited for optical semiconductor device, and method for manufacturing the same |
| JP4597567B2 (en) * | 2004-05-07 | 2010-12-15 | 株式会社イノアックコーポレーション | Polyurethane foam and laminate thereof |
| US20080132591A1 (en) * | 2006-12-01 | 2008-06-05 | Lawrence Gary M | Method of producing a thermoplastic polyurethane compound |
| JP6261128B2 (en) * | 2014-04-02 | 2018-01-17 | 住友ゴム工業株式会社 | Rubber composition and semiconductive foam rubber roller |
| EP3492518A1 (en) | 2017-11-29 | 2019-06-05 | Covestro Deutschland AG | Method for treating a polyurethane foam |
| JP2019099631A (en) * | 2017-11-30 | 2019-06-24 | 株式会社イノアックコーポレーション | Chip dispersion soft polyurethane foam and its production method |
| EP3828213A1 (en) * | 2019-11-28 | 2021-06-02 | Covestro Deutschland AG | Bulk material containing solid diisocyanates and urethane group-containing prepolymers obtainable therefrom |
| KR102377611B1 (en) * | 2021-09-07 | 2022-03-22 | 동세철 | Manufacturing method for environment-friendly bio polyurethane resin of enhanced cold resistance synthesized with waste resin of the polyurethane fiber process and the bio polyurethane resin thereof |
| CN114656673A (en) * | 2022-04-13 | 2022-06-24 | 澳森传动系统(昆山)有限公司 | Polyurethane microcellular foam and production method thereof |
Family Cites Families (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3256218A (en) * | 1962-11-19 | 1966-06-14 | Du Pont | Dispersing coarse fillers in polyurethane foams |
| GB1585260A (en) * | 1976-07-09 | 1981-02-25 | Gen Foam Products | Flexible polyurethane moulded product |
| FR2357357A2 (en) * | 1970-07-02 | 1978-02-03 | Gen Foam Products | Moulded prods. from comminuted foam in polyurethane matrix - esp. useful in shoe soles |
| DE2035175B2 (en) * | 1970-07-15 | 1973-03-08 | Elastomer Ag, Chur (Schweiz) | PROCESS FOR THE RECOVERY OF WASTE, WASTE PARTS AND / OR DISPOSAL MATERIALS FROM POLYADDUCTS MANUFACTURED BY THE ISOCYANATE POLYADDITION PROCESS |
| US4692470A (en) * | 1986-02-04 | 1987-09-08 | Air Products And Chemicals, Inc. | Process for incorporating powders in viscous fluids |
| DE4316389A1 (en) * | 1993-05-17 | 1994-11-24 | Bayer Ag | Process for the preparation of isocyanate prepolymers by dissolving polyurethane in isocyanates |
| DE4328076A1 (en) * | 1993-08-20 | 1995-02-23 | Bayer Ag | Process for the production of soft foams containing urethane groups |
| DE4334549A1 (en) * | 1993-10-11 | 1995-04-13 | Bayer Ag | Polyisocyanate preparations |
| DE4409546A1 (en) * | 1994-03-19 | 1995-09-21 | Kabelmetal Ag | Utilisation of waste polyurethane foams |
| DE4418506A1 (en) * | 1994-05-27 | 1995-11-30 | Bayer Ag | Process for the production of moldings from two-component reactive systems with a high filler content |
| EP0693526A1 (en) * | 1994-07-20 | 1996-01-24 | Bayer Ag | Process for the preparation of rigid urethane foams, optionally containing isocyanurate groups |
-
1996
- 1996-08-22 DE DE19633891A patent/DE19633891A1/en not_active Withdrawn
-
1997
- 1997-08-11 AT AT97113931T patent/ATE268789T1/en not_active IP Right Cessation
- 1997-08-11 EP EP97113931A patent/EP0826705B1/en not_active Expired - Lifetime
- 1997-08-11 DE DE59711696T patent/DE59711696D1/en not_active Expired - Lifetime
- 1997-08-18 CA CA002212117A patent/CA2212117A1/en not_active Abandoned
- 1997-08-20 JP JP9223247A patent/JPH1095825A/en not_active Withdrawn
- 1997-08-20 BR BR9704473A patent/BR9704473A/en not_active Application Discontinuation
- 1997-08-21 US US08/916,181 patent/US5891927A/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110684501A (en) * | 2019-09-25 | 2020-01-14 | 郑州骏惠材料技术有限公司 | Polyurethane hard foam powder filled single-component polyurethane sealant and preparation method thereof |
| CN110684501B (en) * | 2019-09-25 | 2022-03-22 | 郑州大学 | Polyurethane hard foam powder filled single-component polyurethane sealant and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| ATE268789T1 (en) | 2004-06-15 |
| BR9704473A (en) | 1999-01-12 |
| DE59711696D1 (en) | 2004-07-15 |
| EP0826705A1 (en) | 1998-03-04 |
| JPH1095825A (en) | 1998-04-14 |
| US5891927A (en) | 1999-04-06 |
| DE19633891A1 (en) | 1998-02-26 |
| EP0826705B1 (en) | 2004-06-09 |
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