AU6829794A - Molded polyurethane foams - Google Patents

Molded polyurethane foams

Info

Publication number
AU6829794A
AU6829794A AU68297/94A AU6829794A AU6829794A AU 6829794 A AU6829794 A AU 6829794A AU 68297/94 A AU68297/94 A AU 68297/94A AU 6829794 A AU6829794 A AU 6829794A AU 6829794 A AU6829794 A AU 6829794A
Authority
AU
Australia
Prior art keywords
polyisocyanate
polyurethane foams
polyol
molded polyurethane
weight
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.)
Granted
Application number
AU68297/94A
Other versions
AU679997B2 (en
Inventor
Yoshiaki Miyazaki
Kazuo Mizumura
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dow Mitsubishi Kasei Ltd
Dow Chemical Co
Original Assignee
Dow Mitsubishi Kasei Ltd
Dow Chemical Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority claimed from JP5132352A external-priority patent/JPH06322057A/en
Priority claimed from JP5132364A external-priority patent/JPH06322058A/en
Application filed by Dow Mitsubishi Kasei Ltd, Dow Chemical Co filed Critical Dow Mitsubishi Kasei Ltd
Publication of AU6829794A publication Critical patent/AU6829794A/en
Assigned to DOW MITSUBISHI CHEMICAL LIMITED, DOW CHEMICAL COMPANY, THE reassignment DOW MITSUBISHI CHEMICAL LIMITED Amend patent request/document other than specification (104) Assignors: DOW CHEMICAL COMPANY, THE, DOW MITSUBISHI KASEI LIMITED
Application granted granted Critical
Publication of AU679997B2 publication Critical patent/AU679997B2/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/63Block or graft polymers obtained by polymerising compounds having carbon-to-carbon double bonds on to polymers
    • C08G18/632Block or graft polymers obtained by polymerising compounds having carbon-to-carbon double bonds on to polymers onto polyethers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/10Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/48Polyethers
    • C08G18/4854Polyethers containing oxyalkylene groups having four carbon atoms in the alkylene group
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2110/00Foam properties
    • C08G2110/0033Foam properties having integral skins
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2110/00Foam properties
    • C08G2110/0083Foam properties prepared using water as the sole blowing agent

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polyurethanes Or Polyureas (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Description

MOLDED POLYURETHANE FOAMS
BACKGROUND OF THE TNVENTTON
The present invention relates to molded polyurethane foams having excellent abrasion resistance useful for automotive material for steering wheels, headrests and armrests, material for furniture and the like.
Integral skin polyurethane foams having fine skin are well-known to the public and are widely utilized as automotive material for steering wheels, headrests and armrests, and material for furniture and the like in various fields. The formation of the skin layer in the integral skin foams is based on the function of a blowing agent such as chlorofluorocarbon ("CFC") in the exothermic reaction of a polyisocyanate with a polyol. The use of a physical blowing agent such as CFC provides to the foams excellent skin properties which are required to the stated products. On the contrary, the use of a chemical blowing agent such as water does not usually provide any excellent skin properties to the foams.
Some approaches to provide excellent skin properties to molded polyurethane foams have included, for example, those described in Japanese Kokai Patent No. H03-24108, in which a specific catalyst mixture comprising a urethane catalyst and a carbodiimide catalyst is employed to provide low core density in the presence of a non-reactive physical blowing agent, and Japanese Kokai Patent No. H03-33120, in which a specific catalyst mixture is employed in the presence of water as the primary blowing agent. Especially, the technology disclosed in the latter patent may be useful as an alternative technology of a CFC based blowing agent under the Freon Regulation.
Since several years ago, it has been pointing out that CFC destroys the ozone layer of the Earth, and consequently, the use of CFC is globally expected to be restricted or abolished in various industrial fields in present and future. In such situation, some approaches to employ water as the primary blowing agent have been trying. However, in such prior arts, there is a technical problem that demolding time of the process employing water as a sole blowing agent is longer than the one of the process employing CFC as a blowing agent, and also that the former foams are not better in skin properties and abrasion resistance than the latter foams prepared by employing CFC.
SUMMARY OF THE INVENTION The inventors researched to overcome the stated prior technical problems. That is, the purpose of the present invention is to provide molded polyurethane foams having excellent abrasion resistance under shorter demolding time.
The inventors discovered that the stated purpose of the invention can effectively be achieved by employing a specific polyisocyanate, polyol and catalyst in the presence of water as a blowing agent. That is, the present invention provides molded polyurethane foams prepared by reacting a polyisocyanate with a polyol in the presence of water as a blowing agent and a catalyst wherein (a) the polyisocyanate comprises a mixture of (i) from 2 to 30 weight percent polymethylene polyphenyl polyisocyanate ("Polymeric MDI") and (ii) a NCO-terminated prepolymer prepared from the reaction of an organic polyisocyanate with 20 to 45 weight percent poly(oxytetramethylene)glycol ("PTMG"), said weight percents being based on the total weight of organic polyisocyanate, poly(oxytetramethylene)glycol and polymethylene polyphenyl polyisocyanate, and (b) the polyol contains at least 30 weight percent polymer polyol prepared from the reaction of a polyetherpolyol with an ethylenic unsaturated monomer, and (c) the catalyst contains an organotin compound. The present invention also provides molded polyurethane foams prepared by reacting a polyisocyanate with a polyol in the presence of water as a blowing agent and a catalyst wherein (a) the polyisocyanate comprises a NCO-terminated prepolymer prepared from the reaction of (i) an organic polyisocyanate, (ii) from 2 to 30 weight percent polymethylene polyphenyl polyisocyanate and (iii) from 20 to 45 weight percent poly(oxytetr__methylene)glycol, said weight percents based on the total weight of the polyisocyanate, polymethylene polyphenyl polyisocyanate and poly(oxytetramethylene)glycol, and (b) the polyol contains at least 30 weight percent polymer polyol prepared from the reaction of a polyetherpolyol with an ethylenic unsaturated monomer, and the catalyst contains an organotin compound.
DETAILED DESCRIPTION OF THE INVENTION
Suitable polyisocyanates useful in the present invention include, for example, a mixture of a polymeric MDI and a NCO-terminated prepolymer prepared from the reaction of an organic polyisocyanate with PTMG, or a NCO-terminated prepolymer prepared from the reaction of an organic polyisocyanate containing a polymeric MDI with PTMG.
Suitable organic polyisocyanates useful in the present invention include, for example, aliphatic polyisocyanates, alicyclic polyisocyanates, aromatic polyisocyanates or hetrocyclic polyisocyanates which are well-known to the public in polyurethane or polyurea industrial field. More specifically, suitable organic polyisocyanates include, for example, 1,6-hexamethylene diisocyanate, cyclohexane-1,4 diisocyanate, 1,4-xylilene diisocyanate. 2,4-toluene diisocyanate. 2,6-toluene diisocyanate, 4,4'~diphenylmethane diisocyanate ("MDI"), 2,4-diphenylmethane diisocyanate, Polymeric MDI and modified polyisocyanates having a group such as urethane group, urea group, biuret group, carbodiimide group or isocyanurate group, and the mixture thereof. Among the polyisocyanates, preferable polyisocyanates are aromatic polyisocyanates such as MDI, a polymeric MDI, modified polyisocyanates thereof and the mixture thereof.
Suitable poly(oxytetramethylene)glycol ("PTMG") is a linear polyetherpolyol having a primary hydroxy group in its both terminals and has an weight average molecular weight of about 300 to about 3,000. The preferable molecular weight of PTMG to be employed in the preparation of the NCO-terminated prepolymer of the present invention is from about 500 to about 2.400.
The NCO-terminated prepolymer is prepared by reacting PTMG with an excess amount of an organic polyisocyanate in the range of temperature of about 40 to about 100°C. The NCO content of the prepolymer is from about 14 to about 28 weight percent ("wt%") and the PTMG content of the prepolymer is from about 10 to about 50 wt%, preferably, about 20 to about 45 wt%.
One of the polyisocyanates useful in the present invention is a mixture of a polymeric MDI and the stated PTMG-based prepolymer. The polymeric MDI content of the poly- isocyanate mixture is from about 1 to about 40 wt%, preferably, about 2 to about 30 wt%, more preferably, about 5 to about 20 wt%. The another polyisocyanate useful in the present invention is a prepolymer prepared from the reaction of an organic polyisocyanate containing a polymeric MDI with PTMG. The NCO content of the prepolymer is from about 14 to about 28 wt% and the PTMG content of the prepolymer is from about 10 to about 50 wt%, preferably, about 20 to about 45 wt%. The polymeric MDI content in the prepolymer is from about 1 to about 40 wt%, preferably, about 2 to about 30 wt%, more preferably, about 5 to about 20 wt%.
Suitable polyols useful in the present invention include, for example, polyetherpolyols prepared from the reaction of alkyleneoxides such as ethyleneoxide, propyleneoxide and butyleneoxide with low molecular weight polyols such as ethyleneglycol, propyleneglycol, glycerol, trimethyrolpropane, triethanolamine, pentaerythritol, sorbitol and sucrose, or polyamines such as ethylenediamine, xylilenediamine, piperazine and N-N-dimethylamino alkylamine, polymer polyols prepared from the reaction of the stated polyetherpolyols with ethylenic unsaturated monomers such as acrylonitrile, styrene, butadiene, methyl methacrylate, acrylic amide and vinyl acetate, or polyesthers prepared from the reaction of the stated low molecular weight polyols with polycarboxylic acids such as succinic acid, maleic acid, sebacic acid, adipic acid, fumaric acid, phthalic acid and dimeric acid. The inventors discovered that a polymer polyol is recommended to use as a polyol in order to improve abrasion resistance of molded polyurethane foams of the present invention. Suitable polymer polyols include, for example, polymer polyols prepared from the reaction of a polyetherpolyol with acrylonitrile only or a mixture of acrylonitrile and other ethylenic unsaturated monomer such as styrene. However, though the use of such polymer polyols is of good advantage to improvement of abrasion resistance of molded polyurethane foams, the amount employed of the polymer polyol should be determined under consideration of other properties such as processability since the polymer polyols have generally high viscosity. The amoimt employed of the polymer polyol in the total polyol is at least 30 wt%, preferably, about 30 to about 70 wt%, more preferably, about 35 to about 60 wt%.
Suitable blowing agents useful in the present invention include, for example, water, chlorofluorocarbon ("CFC") or a mixture thereof. The suitable blowing agent is water only or a blowing agent containing water as primary component. The amount employed of water is from about 0.05 to about 5 parts by weight ("pbw") based on the total polyol, preferably, about 0.1 to about 3 pbw, more preferably, about 0.3 to about 2 pbw. Solvents, having low boiling point, such as pentane, methyienechloride, dichloromethane and 4,4'-diaminodiphenylmethane, can optionally be employed as a blowing agent together with water.
In the present invention, it is essential to employ an organotin compound as a catalyst. Suitable organotin catalysts include, for example, organotin compounds such as dibutyltin dilaurate, dibutyltin diacetate, dihexyltin diacetate, dimethyltin dimercaptide, dibuthyltin dimercaptide, diocthyltin dimercaptide, di-2-ethylhexyltin oxide, stannous octoate and stannous oleate. Among the stated organotin compounds, more preferable compound is a mercaptide type organotin compound such as dibutyltin dimercaptide, having good hydrolysis resistance. The amount employed of the organotin catalyst is less than 0.5 pbw, preferably about 0.01 to about 0.5 pbw, more preferably about 0.03 to about 0.1 pbw, based on the total polyol of 100 pbw.
Suitable other catalysts to be optionally employed in the present invention include, for example, tertiary amine compounds such as trialkylamines like trimethylamine and triethylamine, heterocyclic amines like N-alkylmorpholine. ethers like 2,2'-bis -(dimethylamino)diethylether, aliphatic polyamines like 1 ,4-dimethylpiperazine, triethylenediamine, N,N,N',N'- tetramethyl-l,3-butanedi__mine and N-methyldiethanolEimine, or a mixture thereof. The amount employed of the amine type catalyst is usually within the range well-known to the public in the polyurethane chemistry. Suitable cross-linking agents to be optionally employed in the present invention include, for example, amine-based low molecular weight polyols such as triethanolamine and diethanolamine, and low molecular weight polyols such as ethyleneglycol, diethyleneglycol, butanediol, trimethyrolpropane and glycerol, or a mixture thereof. The amoimt employed of the cross-linking agent is usually from about 2 to about 20 pbw based on the total polyol, preferably, about 3 to about 10 pbw.
In addition to the stated components, other additives such as emulsifying agent, stabilizing agent, surfactant, filler, pigment and antioxidant can optionally be employed in the present invention. Incidentally, molded polyurethane foams of the present invention can be manufactured in accordance with prior making methods such as open-mold process or closed-mold process.
EXAMPLES
The present invention is described more specifically in the following Examples and Comparative Examples. It is to be understood, however, that the invention is not to be limited by the embodiments described in the following Examples. Reactive components employed in Examples and Comparative Examples are as follows. The term "pbw" or "%" is on the basis of weight unless there is specific description.
(1) Polyisocyanates:
Three polyisocyanates, diphenylmethane diisocyanate ("MDI") (1-125; NCO content:33.6 wt%), a modified MDI (1-143; NCO content:29.4 wt%) and Polymeric MDI (PAPI-135; NCO content:31.0 wt%) were selected as organic polyisocyanate component. Three PTMGs having different average molecular weight of 700, 1,000 and 1,500 (respectively "PTMG700", "PTMG1000" and "PTMG 1500") were selected as polyol component. In addition, a polyetherpolyol having an average equivalent weight of 1,600 and capped ethyleneoxide (EO) content of 14 wt% ("Polyol PI"), prepared from the reaction of glycerol as an initiator with propyleneoxide (PO), was selected as another polyol component. Various NCO-terminated prepolymers were prepared employing the stated polyisocyanate components and polyols components. The composition of each prepolymer and polyisocyanate mixture is shown in Table 1, Table 2 and Table3.
(2) Polyols:
Polyol P2: A propyleneoxide ("PO")-added polyetherpolyol initiated with glycerol (Functionality^, Average equivalent weight ("EW"): 1,600, PO content:83 wt%, Capped EO content: 17 wt%) This polyetherpolyol was prepared capping EO after the reaction of glycerol as an initiator with PO in the presence of potassium hydroxide as a catalyst.
Polyol CPP1: A polymer polyol (Functionality^, OH value:28. solid content:20 wt%) This polymer polyol was prepared polymerising the stated Polyol P2 with acrylonitrile.
Polyol CPP2: A polymer polyol (Functionality^, OH value:28. solid content:20 wt%) This polymer polyol was prepared polymerising the stated Polyol P2 with a monomer mixture of acrylonitrile styrene (70/30 weight ratio).
(3)Additives: Catalyst:
Organotin type catalyst: Dibutyltin dimercaptide (FOMREZ UL-l:Witco) Amine type catalyst 1: Triethylenediamine (dipropyleneglycol 33 % solution)
(Dabco 33LV: Air Products) Amine type catalyst 2: Bis(dime_hylaminoethyl)ether
(NIAX A-l: Union Carbide) Cross-linking agent: monoethyleneglycol (MEG) Blowing agent: Water; Trichlorofluoromethane (CFC-11)
EXAMPLES 1 TO 35 AND COMPARATIVE EXAMPLES 1 TO 4
According to the formulations shown in Table 4, 5, 6, 7 8, 9 and 10, various molded polyurethane foams (steering wheels) were prepared based on the following manner.
A polyol and other additives except a polyisocyanate were mixed for 10 seconds at 3,000 r.p.m. Next, the polyisocyanate measured was mixed with the polyol mixture for 3 seconds at 3,000 r.p.m. and continually the mixture was injected into an iron-made mold being maintained under 50 °C. After curing for certain time (e.g. 180 seconds, 150 seconds, 120 seconds, 90 seconds and 60 seconds), a polyurethane foam was demolded from the mold. The surface properties such as blistering and skin delamination of the foam obtained were immediately observed as an evaluation of demoldability. The results are shown in each Table. The meaning of each mark is as follows. "A" means "good", "B" means "almost good" and "C" means "not good". Some samples for abrasion test were prepared from the normal foam obtained. The abrasion test was carried out in the following manner. The results of the abrasion test are shown in each Table.
Evaluation of Abrasion Resistance: Testing samples having outer peripheral length of about 80 mm were cut and prepared from a foam moldings (steering wheel) obtained as stated above. The foam moldings was prepared covering an iron-made pipe (outside diameter: 14 mm) with polyurethane foam (shape of a cross section to the diameter-direction: ellipse having a 28 mm long diameter and a 23 mm short diameter). The abrasion resistance of the testing sample was evaluated using a testing machine for abrasion resistance, "SUGA FR-2-S Type" (produced by Suga Test Instruments in Japan). The testing sample was set in the machine as the outer surface of the sample contacted a white cloth
(Canvas Cloth No.10) having a 100 g weighting in its one end. The surface of the sample was rubbed against the cloth for certain times (3 x 10 4 , 5 x 104 and 10 x 104 times) under the stated conditions.
The abrasion test was evaluated by visual observation and the ranking of 1 to 5 was given to each result. The meaning of each rank shown as "5", "4" and "3" in each Table is as follows.
5: no abrasion (no change) 4: slight abrasion with polish 3: more abrasion
As evident from results shown in each Table, all Invention Examples show better demoldability even in the use of water as a sole blowing agent and also show excellent abrasion properties than Comparative Examples. Accordingly, the molded polyurethane foams of the present invention can be produced under very cycle times and can be useful for automotive material such as steering wheels, headrests and armrests, material for furniture and the like, in which abrasion resistance is required.
Table 1
Polyisocyanates (Examples)
Total NCO% of 20.6 21.5 22.4 22.5 20.6 19.8 20.5 the mixture
O 94/26800
Table 2
Polyisocyanates (Examples)
Table 3
Polyisocyanates (Comparative Examples)
O 94/26800
10
Table 4
Formulations and Properties (Examples 1 to 7)
No.
Polyisocyanate I 100
Polyisocyanate II - 100
Polyisocyanate III - - 100 Polyisocyanate IV - 100 Polyisocyanate V - 100 Polyisocyanate VI . . . 100 Polyisocyanate VII . . . 100
Polyol P2 60 60 60 60 60 60 60
Polyol CPP1 40 40 40 40 40 40 40
MEG 7 7 7 7 7 7 7
Fomrez UL-1 0.07 0.07 0.07 0.07 0.07 0.07 0.07
Dabco 33LV 1.5 1.5 1.5 1.5 1.5 1.5 1.5
NIAX A-1 0.4 0.4 0.4 0.4 0.4 0.4 0.4
Water 0.5 0.5 0.5 0.5 0.5 0.5 0.5
(Note) Amount employed: pbw (Polyisocyanate: NCO Index)
O 94/26800
1 1
Table 5
Formulations and Properties (Examples 8 to 15)
(Note) Amount employed: pbw (Polyisocyanate: NCO Index)
O 94/26800
12
Table 6
Formulations and Properties (Examples 16 to 18)
(Note) Amount employed: pbw (Polyisocyanate: NCO Index)
94/26800
13
Table 7
Formulations and Properties (Examples 19 to 24)
(Note) Amount employed: pbw (Polyisocyanate: NCO Index)
94/26800
14
Table 8
Formulations and Properties (Examples 25 to 32)
(Note) Amount employed: pbw (Polyisocyanate: NCO Index)
94/26800
15
Table 9
Formulations and Properties (Examples 33 to 35)
(Note) Amount employed: pbw (Polyisocyanate: NCO Index)
O 94/26800
16
Table 10
Formulations and Properties (Comparative Examples 1 to 4)
(Note) Amount employed: pbw (Polyisocyanate: NCO Index)

Claims (14)

WHAT IS CLAIMED IS:
1. Molded polyurethane foams prepared reacting a polyisocyanate with a polyol in the presence of water as a blowing agent and a catalyst, wherein (a) the polyisocyanate comprises a mixture of (i) from about 1 to about 40 weight percent polymethylene polyphenyl polyisocyanate and (ii) a NCO-terminated prepolymer prepared from the reaction of an organic polyisocyanate with from about 10 to about 50 weight percent poly(oxytetramethylene)glycol, said weight percents being based on the total weight of organic polyisocyanate, poly(oxytetramethylene)glycol and polymethylene polyphenyl polyisocyanate, (b) the polyol contains at least 30 weight percent polymer polyol prepared from the reaction of a polyetherpolyol with an ethylenic unsaturated monomer, and (c) the catalyst contains an organotin compound.
2. Molded polyurethane foams prepared by reacting a polyisocyanate with a polyol in the presence of water as a blowing agent and a catalyst, wherein (a) the polyisocyanate comprises a NCO-terminated prepolymer prepared from the reaction of (i) an organic polyisocyanate, (ii) from about 1 to about 40 weight percent polymethylene polyphenyl polyisocyanate and (iii) from about 10 to about 50 weight percent poly(oxytetramethylene)glycol, said weight percents based on the total weight of the polyisocyanate, polymethylene polyphenyl polyisocyanate and poly(oxytetramethylene)glycol, (b) the polyol contains at least 30 weight percent polymer polyol prepared from the reaction of a polyetherpolyol with an ethylenic unsaturated monomer, and (c) the catalyst contains an organotin compound.
3. The molded polyurethane foams of Claim 1 wherein the organic polyisocyanate is 4,4'-diphenylmethane diisocyanate or a modified 4,4'-diphenylmethane diisocyanate.
4. The molded polyurethane foams of Claim 1 wherein the weight average molecular weight of the poly(oxytetramethylene)glycol is from about 500 to about 2,400, the polymethylene polyphenyl polyisocyanate and poly(oxytetramethylene)glycol contents are from about 2 to 30 weight percent and from about 20 to 45 weight percent respectively, based on the total weight of polyisocyanate component (a), and the polyol contains from about 30 to about 70 weight percent polymer polyol based on the total weight of polyol component (b).
5. The molded polyurethane foams of Claim 1 wherein the ethylenic unsaturated monomer is acrylonitrile.
6. The molded polyurethane foams of Claim 1 wherein the water content is from aboutθ.3 to about 2 parts by weight based on the total weight of the polyol component.
7. The molded polyurethane foams of Claim 1 wherein the organotin compound is a mercaptide type organotin compound.
8. The molded polyurethane foams of Claim 7 wherein the mercaptide type organotin compound is dimethyltin dimercaptide, dibutyltin dimercaptide or dioctyltin dimercaptide.
9. The molded polyurethane foams of Claim 2 wherein the organic polyisocyanate is 4,4'-diphenylmethane diisocyanate or a modified 4,4'-diphenylmeth__ne diisocyanate.
10. The molded polyurethane foams of Claim 2 wherein the weight average molecular weight of the poly(oxytetramethylene)glycol is from about 500 to 2,400, the polymethylene polyphenyl polyisocyanate and poly(oxytetramethylene)glycol contents are from about 2 to 30 weight percent and from about 20 to 45 weight percent respectively, based on the total weight of polyisocyanate component (a), and the polyol contains from about 30 to about 70 weight percent polymer polyol based on the total weight of the polyol component (b).
11. The molded polyurethane foams of Claim 2 wherein the ethylenic unsaturated monomer is acrylonitrile.
12. The molded polyurethane foams of Claim 2 wherein the water content is from about 0.3 to about 2 parts by weight based on the total polyol component (b).
13. The molded polyurethane foams of Claim 2 wherein the organotin compound is a mercaptide type organotin compound.
14. The molded polyurethane foams of Claim 2 wherein the mercaptide type organotin compound is dimethyltin dimercaptide, dibutyltin dimercaptide or dioctyltin dimercaptide.
AU68297/94A 1993-05-12 1994-05-10 Molded polyurethane foams Ceased AU679997B2 (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
JP5132352A JPH06322057A (en) 1993-05-12 1993-05-12 Molded polyurethane foam
JP5132364A JPH06322058A (en) 1993-05-12 1993-05-12 Molded polyurethane foam
JP5-132352 1993-05-12
JP5-132364 1993-05-12
PCT/US1994/005173 WO1994026800A1 (en) 1993-05-12 1994-05-10 Molded polyurethane foams

Publications (2)

Publication Number Publication Date
AU6829794A true AU6829794A (en) 1994-12-12
AU679997B2 AU679997B2 (en) 1997-07-17

Family

ID=26466945

Family Applications (1)

Application Number Title Priority Date Filing Date
AU68297/94A Ceased AU679997B2 (en) 1993-05-12 1994-05-10 Molded polyurethane foams

Country Status (6)

Country Link
EP (1) EP0650501A1 (en)
CN (1) CN1110877A (en)
AU (1) AU679997B2 (en)
BR (1) BR9405366A (en)
CA (1) CA2139654A1 (en)
WO (1) WO1994026800A1 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100489003C (en) * 2003-12-24 2009-05-20 日本聚氨酯工业株式会社 Process for producing soft polyurethane foam, process for producing conductive soft polyurethane foam
JP2011528726A (en) 2008-07-18 2011-11-24 ダウ グローバル テクノロジーズ エルエルシー Cellular structure and viscoelastic polyurethane foam
CN103788337B (en) * 2014-01-14 2015-12-02 北京理工大学 A kind of flame retardant polyurethane rigid foam for external wall outer insulation and preparation method thereof

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1204100A (en) * 1968-05-15 1970-09-03 Bayer Ag Process for the production of foam plastics which contain urethane groups
DE3113690A1 (en) * 1981-04-04 1982-10-28 Elastogran GmbH, 2844 Lemförde "METHOD FOR PRODUCING CLOSED-CELL POLYURETHANE MOLDED PARTS WITH A COMPRESSED EDGE ZONE"
GB8911853D0 (en) * 1989-05-23 1989-07-12 Ici Plc Co2 blown integral skin foams
EP0451559A3 (en) * 1990-04-05 1992-11-25 Basf Corporation (A Delaware Corp.) Integral skin polyurethane foam
IT1240635B (en) * 1990-05-04 1993-12-17 Dow Italia MICROCELLULAR POLYURETHANE POLYMERS PREPARED FROM THREE POLY POLYMERS (TETRAMETHYLENE) GLYCOLS WITH ISOCYANATE GROUPS TERMINALS
US5491175A (en) * 1992-04-10 1996-02-13 The Dow Chemical Company Polyurethane foam molding
US5234961A (en) * 1992-12-07 1993-08-10 Basf Corporation Polyurethane water-blown integral skin system produced with a polyterahydrofuran prepolymer

Also Published As

Publication number Publication date
BR9405366A (en) 1999-09-08
AU679997B2 (en) 1997-07-17
CA2139654A1 (en) 1994-11-24
WO1994026800A1 (en) 1994-11-24
EP0650501A1 (en) 1995-05-03
CN1110877A (en) 1995-10-25

Similar Documents

Publication Publication Date Title
KR100245236B1 (en) Polyurethane foams
US4297444A (en) Process for rim elastomers with superior high temperature dimensional stability
US5236961A (en) Water-blown integral skin polyurethane foams having a skin with abrasion resistance
CA1171622A (en) Rim elastomers with improved heat distortion and tear properties
CA1242848A (en) Flexible polyurethane foams
US4997858A (en) Method for preparing a flexible polyurethane foam
KR100347495B1 (en) Manufacturing Method of Foamed Polyurethane Molded Parts without CFC
KR100441926B1 (en) Polyurethane Elastomers
CA1165929A (en) Stable emulsions of polyols and crosslinkers for polyurethanes
US5246977A (en) Microcellular polyurethane polymers prepared from isocyanate-terminated poly(oxytetramethylene) glycol prepolymers
US4341875A (en) High flexural modulus reaction injection molded urethanes
US4927861A (en) Rigid polyurethane preparation process
US5308882A (en) Preparation of polyurethane foam without a tertiary amine catalyst
AU641768B2 (en) Microcellular polyurethane polymers prepared from isocyanate-terminated poly(oxytetramethylene) glycol prepolymers
US5491175A (en) Polyurethane foam molding
CA1172009A (en) Reinforced reaction injection molded elastomers
US5266234A (en) Water-blown integral skin polyurethane foams having a skin with abrasion resistance
US4362824A (en) Method for making RIM polyurethane elastomers using as the catalyst system dimethylethanolamine, dibutyltin dilaurate and an alkyltin mercaptide
US4359540A (en) Method for making rim elastomers using a catalyst system which is a polymer containing tertiary amine moieties
AU6829794A (en) Molded polyurethane foams
US4436843A (en) High-resilience polyurethane foams having improved resistance to shrinkage
JPH06322057A (en) Molded polyurethane foam
US4469657A (en) Rim elastomers with improved catalyst efficiency
JPH06322058A (en) Molded polyurethane foam
CA1185040A (en) Method for making rim elastomers using a catalyst system containing a polymeric component