Polyurethane integral skin foam of low ozone depletion potential

Abstract

A process for preparing polyurethane integral skin foam with low ozone depletion potential, which comprises mixing 100 pph of a polyether polyol, 5-50 pph of a chain extender, 0.1-2.0 pph of a surfactant, 0.01-0.20 pph of an amine and 0.01-0.20 pph of an organotin catalyst, 0-3.0 pph of a nucleating agent and 1.0-30 pph of a blowing agent comprising 50 to 100 weight percent of HCFC-123 and 50 to 0 weight percent of HCFC-141b to form a polyol mixture; blending said polyol mixture with isocyanate having an ISO index=0.95 to 1.10 and reacting said blend at a temperature from 0.degree.-70.degree. C. in a mold at a temperature of from 10.degree. to 90.degree. C. for a molding time of 1 to 9 minutes to form a polyurethane integral skin foam, and the product of said process.

Description

BACKGROUND OF THE INVENTION

The traditional process of producing polyurethane (PU) integral skin foam comprises using CFC-11 as the blowing agent to yield products used in automobile parts and sporting goods, such as instrument panels, head and hand rests, bumpers, rims, handles and seats for motorcycles.

The production of PU integral skin foam is a one-step process in contrast to the old process where a PVC synthetic leather cover was applied to the PU foam. Because of the smooth surface given by the PVC cover in the old process, the appearance and physical properties of the skin in the one-step process remains a very important feature. Traditional chemical blowing agents, such as water, used in PU foaming cannot completely or partially replace physical blowing agents, such as CFC-11, for integral skin foam because serious skin defect problems occur in the production. Unfortunately, CFC-11 and fully halogenated chlorofluorocarbons (CFCs) deplete the ozone layer and their continued use has been severely limited.

Accordingly, it is desirable to provide a commercially feasible, low ozone depletion potential product, using pollution free technique for the production of a PU integral skin foam which has physical properties comparable to the current commercial products.

SUMMARY OF THE INVENTION

In accordance with the invention, it has been discovered that a polyurethane (PU) integral skin foam having physical properties comparable to that of the current commercial products and low ozone depletion potential (ODP) can be obtained by using the two-carbon hydrogen-containing halocarbon, such as HCFC-123 or HCFC-141b. These materials have an ODP of 0.05 compared to CFC-11 which has an ODP of 1. To accomplish this result, compounding of polyurethane and the processing conditions must be carefully controlled. This result is particularly surprising since, as noted in M. J. Cartmell, "Developments in the Use of CFCs in Polyurethane Foams," (European Isocyanate Producers Association (ISOPA), 250 Avenue Louise, Bte. 52, 1050 Brussels, Belgium), it was widely recognized that CFC-11 was a key element in all integral skin foams because the latter condenses at the mold surface during the molding operation to produce the "self skinning" foam (pages 186, 192-193). Also U.S. Pat. No. 4,927,863, noted that HCFCs cause undesirable shrinkage in closed-cell PU foams.

DETAILED DESCRIPTION OF THE INVENTION

While the use of HCFCs as replacements for CFCs has been widely studied since the ozone depletion effect of CFCs has been noted, the successful replacement of the blowing agents in integral skin PU foams has been elusive. In accordance with the instant invention, applicants have found that HCFCs may be used, though they dissolve PU to a greater extent than CFC-11. To accomplish this end, it is necessary to use selected polyether polyols in combination with selected chain extenders so as to develop a formulation which resists the dissolution of the HCFC blowing agents. As will be understood by those skilled in the art, a system wherein the blowing agent dissolves the polyurethane cannot form a practical product, especially where the product is a fine cell foam having this blowing agent entrained therein.

In addition to the foregoing, it has been found that only selected catalyst systems can be used in combination with the HCFC blowing agents to form the desired products. Particularly preferred are amine and organotin catalysts which, though well known in the art, are but a few of the many catalysts used in the preparation of polyurethanes.

Additional constituents are surfactants to produce an end product with a fine skin and nucleating agents to make the integral skin PU foam cells uniform and delicate.

Surprisingly, when the appropriate balance of components is used along with appropriately selected mold and material temperatures and molding times, products which are comparable to those currently in use may be obtained. Advantageously, these processing conditions are similar to those currently in use. Naturally, the ability to use such processing conditions with the novel formulation of the invention is a marked advantage for the foam producer, since no new processing equipment is necessary in order to achieve the benefits of the instant invention. The markedly different physical properties of CFC-11 as compared to the HCFCs used in the instant invention are shown in the following table.

TABLE A______________________________________ CFC-11 HCFC-123 HCFC-141b______________________________________Molecular formula CCl.sub.3 F CHCl.sub.2 CF.sub.3 CH.sub.3 CFCl.sub.2Molecular weight 137.4 152.9 116.9Boiling point (.degree.C.) 23.8 28 32Heat conductivity of gas 0.0045 0.0054 0.0053(BTU/(hr)(ft)(.degree.F.) @ 25.degree. C. @ 30.degree. C. @ 32.degree. C.Heat of evaporation cal/g 43.1 40 53Life in atmosphere (years) 60 2 5Relative ozone depletion 1 <0.05 <0.05potentialRelative greenhouse effect 0.4 <0.1 <0.1______________________________________ Not only do these materials have divergent boiling points, heat conductivities and heats of evaporation but they also have markedly different effects on the atmosphere. It will be noted

that CFC-11 remains in the atmosphere 12-30 times longer than HCFCs and that the latters, relative ozone depletion potential is some 20 times better.

Essential to the success of the formulation of the instant invention is the use of a polyether polyol which, it has been found, prevents the dissolution of the polyurethane in the HCFCs.

Other compounding ingredients are chain extenders, surfactants, amine-type and organotin-type catalysts and nucleating agents. Chain extenders include ethylene glycol, propylene glycol, 1,4 butylene glycol, and diethylene glycol. The surfactant is preferably of silicone glycol type. The amine catalyst includes dimethylethanol amine (DMEA), triethylene amine (TEA) and triethylene diamine (DABCO). Suitable tin catalyst include dibutyl tin dilaurate (DBTDL) and stannous octoate. A preferred nucleating agent is SiO, powder having a particle size .ltoreq.30m.mu.. The liquid diisocyanate is diisocyanate diphenyl methane (MDI)

The formulations of the invention are broadly described in the following table:

TABLE B______________________________________Polyether polyol, pph* 100Chain extender, pph 0-150Surfactant, pph 0.1-2.0Amine catalyst, pph 0.01-0.20Tin catalyst, pph 0.01-0.20Blowing agent, pph 1.0-30Nucleating agent, pph 0-3.0Liquid Isocyanate ISO index = 0.95-1.1______________________________________ *pph = parts per hundred of polyol

The process of the instant invention may be described as follows:

The polyether polyol, chain extender, surfactant and nucleating agent are metered in suitable proportions into a vessel stirred at high speed for 10 minutes. The necessary amine and organotin catalysts are added to the mixture and stirred vigorously for another 5 minutes while maintaining the temperature of the mixture at 20.degree. C. The blowing agent (kept at 10.degree. C) is rapidly added thereafter and stirred at high speed for another 5 minutes. The blend formed is referred to hereafter as the polyol mixture.

The polyol mixture and the liquid diisocyanate diphenyl methane are stored in separate storage tanks. To form the foam, the liquids are metered, with separate metering pumps, and mixed in suitable proportion in a mixing head to form a homogeneous blend. The blend is injected into an aluminum alloy mold (20 cm .times.20 cm .times.4 cm) which is maintained at a selected mold temperature. The upper mold plate is closed and the blend is permitted to react, foam and cure for the predetermined molding time. Finally, the mold is opened and the product removed.

A broad range of processing conditions may be used. These and the preferred ranges are shown in Table C.

TABLE C______________________________________ Broad Range Preferred Range______________________________________Mold temperature, .degree.C. 10-90 40-60Material temperature, .degree.C. 0-70 20-50Molding time, min. 1-9 3-7______________________________________

To illustrate the invention, examples using HCFC-123 and/or HCFC-141b as blowing agent are compared with traditional polyurethane integral skin foam using CFC-11 as the blowing agent.

In the examples the polyether polyol was obtained from Chiunglong Enterprise Corp., Ltd.; the MDI from ICI; the surfactant is Dow Corning DC-5043 and the nucleating agent is SiO, Japan Silica, VN-3.

EXAMPLE 1

Integral skin PU foams using 10 pph of blowing agent were prepared using the following formulations:

TABLE 1______________________________________ Traditional The Instant method Invention______________________________________Polyether polyol 100 100 100 100MDI (ISO index = 1.05) 57.53 57.53 60.07 65.14Ethylene glycol 9.50 9.50 10.0 11.0Triethylene diamine 0.1 0.1 0.1 0.1Dibutyltin dilaurate 0.1 0.15 0.2 0.25Surfactant 0.5 1.0 1.5 2.0Nucleating Agent -- 0.5 0.8 1.0CFC-11 10 -- -- --HCFC-123 -- 10 7 5HCFC-141b -- 0 3 5______________________________________

The physical properties of the skin are shown in the following table:

TABLE 2______________________________________ Tradi- Test tional The instantPhys. Properties Method Method invention______________________________________Density (g/cm.sup.3) ASTM792 0.902 0.899 0.908 0.915Tensile strength ASTM412 25.6 31.1 25.3 24.2(kg/cm.sup.2)Elongation (%) ASTM412 110 100 100 110Tear strength ASTM624 12.0 10.5 12.5 11.6(kg/cm)Hardness (Shore A) ASTM2240 62 66 61 61______________________________________

The physical properties of the foam are shown in Table 3 below:

TABLE 3______________________________________ Tradi- Test tional The instantPhys. Properties Method Method invention______________________________________Density (g/cm.sup.3) ASTM3574 0.225 0.239 0.227 0.228Tensile strength ASTM412 7.9 8.6 7.8 7.5(kg/cm.sup.2)Elongation (%) ASTM412 110 110 110 100Tear strength ASTM624 2.2 2.0 2.1 2.2(kg/cm)Hardness (Shore A) ASTM2240 18 20 18 18______________________________________

EXAMPLE 2

Integral skin PU foams using 20 pph of blowing agent were prepared using the following formulations:

TABLE 4______________________________________ Traditional The Instant method Invention______________________________________Polyether polyol 100 100 100 100MDI (ISO index = 1.05) 48.64 48.64 50.72 54.85Propylene glycol 9.50 9.50 10.0 11.0Triethylene amine 0.1 0.1 0.1 0.1Stannous octoate 0.1 0.15 0.2 0.25Surfactant 0.5 1.0 1.5 2.0Nucleating Agent -- 0.5 0.8 1.0CFC-11 20 -- -- --HCFC-123 -- 20 14 10HCFC-141b -- 0 6 10______________________________________

The physical properties of the skin are shown in the following table:

TABLE 5______________________________________ Tradi- Test tional The instantPhys. Properties Method Method invention______________________________________Density (g/cm.sup.3) ASTM792 0.895 0.860 0.897 0.895Tensile strength ASTM412 21.5 20.1 21.3 20.8(kg/cm.sup.2)Elongation (%) ASTM412 110 125 110 100Tear strength ASTM624 7.3 7.8 7.2 6.9(kg/cm)Hardness (Shore A) ASTM2240 62 64 64 65______________________________________

The physical properties of the foam are shown in Table 6 below:

TABLE 6______________________________________ Tradi- Test tional The instantPhys. Properties Method Method invention______________________________________Density (g/cm.sup.3) ASTM3574 0.178 0.187 0.180 0.182Tensile strength ASTM412 7.5 7.7 7.0 6.9(kg/cm.sup.2)Elongation (%) ASTM412 120 120 120 100Tear strength ASTM624 2.2 2.0 1.8 2.1(kg/cm)Hardness (Shore A) ASTM2240 12 14 11 11______________________________________

EXAMPLE 3

Integral skin PU foams using 5 pph of blowing agent were prepared using the following formulations:

TABLE 7______________________________________ Traditional The Instant method Invention______________________________________Polyether polyol 100 100 100 100MDI (ISO Index = 1.05) 42.51 42.51 44.26 47.751,4 Butylene glycol 9.50 9.50 10.0 11.0Dimethyl ethanol amine 0.1 0.1 0.1 0.1Dibutyltin dilaurate 0.1 0.15 0.2 0.25Surfactant 0.5 1.0 1.5 2.0Nucleating Agent -- 0.5 0.8 1.0CFC-11 5 -- -- --HCFC-123 -- 5 3.5 2.5HCFC-141b -- 0 1.5 2.5______________________________________

The physical properties of the skin are shown in the following table:

TABLE 8______________________________________ Tradi- Test tional The instantPhys. Properties Method Method invention______________________________________Density (g/cm.sup.3) ASTM792 0.945 0.955 0.955 0.962Tensile strength ASTM412 41.5 40.4 40.2 39.8(kg/cm.sup.2)Elongation (%) ASTM412 120 100 120 120Tear strength ASTM624 11.5 12.0 11.6 11.7(kg/cm)Hardness (Shore A) ASTM2240 80 78 80 81______________________________________

The physical properties of the foam are shown in Table 9 below:

TABLE 9______________________________________ Tradi- Test tional The instantPhys. Properties Method Method invention______________________________________Density (g/cm.sup.3) ASTM3574 0.332 0.341 0.335 0.328Tensile strength ASTM412 15.5 16 15.2 15.3(kg/cm.sup.2)Elongation (%) ASTM412 100 100 100 100Tear strength ASTM624 2.7 2.9 2.5 2.7(kg/cm)Hardness (Shore A) ASTM2240 30 29 28 29______________________________________

EXAMPLE 4

Integral skin PU foams using 30 pph of blowing agent were prepared using the following formulations:

TABLE 10______________________________________ Traditional The Instant method Invention______________________________________Polyether polyol 100 100 100 100MDI (ISO Index = 1.05) 37.49 37.49 38.98 41.95diethylene glycol 9.50 9.50 10.0 11.0Triethylene diamine 0.1 0.1 0.1 0.1Stannous octoate 0.1 0.15 0.2 0.25Surfactant 0.5 1.0 1.5 2.0Nucleating agent -- 0.5 0.8 1.0CFC-11 30 -- -- --HCFC-123 -- 30 21 15HCFC-141b -- 0 9 15______________________________________

The physical properties of the skin are shown in the following table:

TABLE 11______________________________________ Tradi- Test tional The instantPhys. Properties Method Method invention______________________________________Density (g/cm.sup.3) ASTM792 0.772 0.765 0.785 0.780Tensile strength ASTM412 16.5 17.5 16.3 15.8(kg/cm.sup.2)Elongation (%) ASTM412 100 90 100 100Tear strength ASTM624 6.3 6.1 6.5 6.3(kg/cm)Hardness (Shore A) ASTM2240 50 51 50 51______________________________________

The physical properties of the foam are shown in Table 12 below:

TABLE 12______________________________________ Tradi- Test tional The instantPhys. Properties Method Method invention______________________________________Density (g/cm.sup.3) ASTM3574 0.112 0.119 0.115 0.118Tensile strength ASTM412 4.8 4.7 4.6 4.3(kg/cm.sup.2)Elongation (%) ASTM412 120 130 120 120Tear strength ASTM624 1.2 1.1 1.3 1.3(kg/cm)Hardness (Shore A) ASTM2240 5 4 5 5______________________________________

In the above mentioned examples, 5, 10, 20 and 30 pph of blowing agents are used. To totally replace CFC-11 by HCFC123 and/or HCFC-141b, the ratios of HCFC-123 to HCFC-141b are 10/0, 7/3 and 5/5 respectively. In order to obtain a PU integral skin foam whose physical properties are comparable to those of traditional commercial product, the amount of chain extender, amine and organotin catalysts used in the formulation must be carefully adjusted.

Most surprisingly, the physical properties of polyurethane foam which uses HCFC-123 as blowing agent are superior to those of tradition PU foam which uses CFC-11 as blowing agent. HCFC-141b is unable to completely replace CFC-11 in the foaming of polyurethane. It must be combined with HCFC-123 in proportion of more than 5/5 to obtain a product which is not inferior than traditional CFC-11 foam. In all events, the process disclosed in the instant invention lessens the global pollution problem caused by ozone depletion and the greenhouse effect.

Claims

1. A process for preparing polyurethane integral skin foam with low ozone depletion potential, which comprises mixing 100 pph of a polyether polyol, 5-50 pph of a chain extender, 0.1-2.0 pph of a surfactant, 0.01-0.20 pph of an amine and 0.01-0.20 pph of an organotin catalyst, 0-3.0 pph of a nucleating agent and 1.0-30 pph of a blowing agent comprising 50 to 100 weight percent of HCFC-123 (CHCl.sub.2 CF.sub.3) and 50 to 0 weight percent of HCFC-141b (CH.sub.3 CFCL.sub.2) to form a polyol mixture; blending said polyol mixture with isocyanate having an ISO index =0.95 to 1.10 and reacting said blend at a temperature from 0.degree. -70.degree. C. in a mold at a temperature of from 10 to 90.degree. C. for a molding time of 1 to 9 minutes to form a polyurethane integral skin foam.

2. The process of claim 1 wherein the chain extender has a general formula as HO--R--OH, where R=C.sub.2 -C.sub.4.

3. The process of claim 2 wherein the chain extender is ethylene glycol, propylene glycol, 1,4 butylene glycol, or diethylene glycol.

4. The process of claim 1 wherein the surfactant is a silicone glycol.

5. The process of claim 1 wherein the amine catalyst is dimethylethanol amine, triethylene amine, or triethylene diamine.

6. The process of claim 1 wherein the organotin catalyst is dibutyl tin dilaurate or stannous octoate.

7. The process of claim 1 wherein the nucleating agent is SiO.sub.2 powder with a particle size .ltoreq.30m.mu..

8. The process of claim 1 wherein the isocyanate is a liquid comprising diisocyanate diphenyl methane.

9. The process of claim 1 wherein the mold temperature is in the range of 40.degree.-60.degree. C.

10. The process of claim 1 wherein the material temperature is in the range of 20.degree.-50.degree. C.

11. The process of claim 1 wherein the molding time is in the range of 3-7 minutes.