WO2008112406A1 - Non-flammable hydrofluorocarbon blowing agent composition - Google Patents

Non-flammable hydrofluorocarbon blowing agent composition Download PDF

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Publication number
WO2008112406A1
WO2008112406A1 PCT/US2008/054718 US2008054718W WO2008112406A1 WO 2008112406 A1 WO2008112406 A1 WO 2008112406A1 US 2008054718 W US2008054718 W US 2008054718W WO 2008112406 A1 WO2008112406 A1 WO 2008112406A1
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WIPO (PCT)
Prior art keywords
foam
blowing agent
hfc
hfc32
flammable
Prior art date
Application number
PCT/US2008/054718
Other languages
French (fr)
Inventor
Benjamin B. Chen
Joseph S. Costa
Original Assignee
Arkema Inc.
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Filing date
Publication date
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Publication of WO2008112406A1 publication Critical patent/WO2008112406A1/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/12Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
    • C08J9/14Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent organic
    • C08J9/143Halogen containing compounds
    • C08J9/144Halogen containing compounds containing carbon, halogen and hydrogen only
    • 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
    • C08G18/4009Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
    • C08G18/4018Mixtures of compounds of group C08G18/42 with compounds of group C08G18/48
    • 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
    • C08G18/487Polyethers containing cyclic groups
    • C08G18/4879Polyethers containing cyclic groups containing aromatic groups
    • 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
    • C08G18/487Polyethers containing cyclic groups
    • C08G18/4883Polyethers containing cyclic groups containing cyclic groups having at least one oxygen atom in the ring
    • 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
    • C08G18/70Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72Polyisocyanates or polyisothiocyanates
    • C08G18/74Polyisocyanates or polyisothiocyanates cyclic
    • C08G18/76Polyisocyanates or polyisothiocyanates cyclic aromatic
    • C08G18/7657Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings
    • C08G18/7664Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups
    • 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
    • C08G2110/0041Foam properties having specified density
    • C08G2110/005< 50kg/m3
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2205/00Foams characterised by their properties
    • C08J2205/10Rigid foams

Definitions

  • the present invention relates to thermosetting foam foamable compositions, such as polyurethane, which include non-flammable blowing agents. More particularly, the present invention relates to thermosetting foam foamable compositions which incorporate a non-flammable blowing agent combination including HFC- 134a and HFC-32.
  • the foamable compositions of the present invention generally are formed from one or more components capable of forming foam having a generally cellular structure and a blowing agent combination.
  • the one or more components comprise a thermosetting composition capable of forming foam and/or foamable compositions.
  • thermosetting compositions include polyurethane and polyisocyanurate foam compositions, and also phenolic foam compositions.
  • the blowing agent compositions of the present invention are included as a blowing agent in the foamable composition, or as a part of one or more of a two or more part foamable mixture.
  • the one or more parts include one or more components capable of reacting and/or foaming under the proper conditions to form a foam or cellular structure.
  • HFCs chlorofluorocarbons
  • HFC- 134a hydrofluorocarbons
  • HFC 134a (1,1,1,2-tetrafluoroethane) is non-flammable and contributes to long-term thermal insulation for thermosetting foams, such as polyurethane foams.
  • HFC 134a exhibits a lower solubility in foaming mixture components, relative to previous materials.
  • HFC134a This lower solubility makes HFC134a less desirable than previous materilas for the urethane industry.
  • HFC32 difluoromethane
  • use of HFC32 has been limted due to it's flammability.
  • HFC 134a suppressses the undesirable flammability of HFC32.
  • blends of HFC 134a and HFC32 that consist of less than about 30 wt% of HFC32 are not flammable. Working with such non-flammable blends, the inventors found improved solubility in polyol mixtures over HFC 134a alone. As a result of improved solubility, foams made with this blowing agent blend exhibited improved processing and performance.
  • the blowing agent combinations of the present invention can be used as a foaming agent for polyolefm foams by being mixed in a polyol mixture (typically referred to as the B side) which form foam when mixed with a polyisocyante mixture (typically referred to as the A side).
  • a polyol mixture typically referred to as the B side
  • a polyisocyante mixture typically referred to as the A side
  • the resulted foam products exhibit superior properties including decreased density and improved k-factor.
  • the foaming agent combination readily dissolves in the components of thermosetting foams, and provides a degree of plasticization sufficient to produce acceptable foams.
  • HFC32 can be used as a foam blow agent for thermoplastic plastic polymer such as polystyrene.
  • US 4,927,863 teaches that HCFC123, HCFC123a, and HCFC 14 IbI owing agents can be combined with shrinkage reducing hydrocarbons including CFC-11, CFC-12, HCFC-22, HFC-32, CFC-113, CFC-114, HCFC-124, HCFC- 133a, HFC- 134a, HCFC- 142b and HFC-152a to produce polyurethane which exhibits reduced foam shrinkage.
  • HFC32 is flammable which has limited its acceptance in certain applications.
  • HFC 134a can be combined with HFC32 to suppress its flammability. This is desirable for polyurethane foams especially for applications which are less tolerable to flammability.
  • the present inventors have examined blends including HFC 134a and HFC32 for flammability, solubility in polyol mixtures and performance in pour-in-place rigid polyurethane foam. It was found that when the blend consists of less than about 30 wt% of HFC32, the blend is not flammable. In addition, the blend was found to exhibit improved solubility in polyol mixtures over HFC 134a alone. As a result of the improved solubility, foams made with this blend exhibited improved processing and performance.
  • the HFCl 34a and HFC32 blend of the present invention can be used with other additives such as: co-blowing agent including but not limited to HFC245fa, HFC365mfc, HFC227, HFC125, and trans- 1,2-dichloroethylene; hydrogen bond forming blocking agents (e.g. organic ether, ester, or ketone) which reduce vapor pressure and reduce the escape of blowing agent from the foam to improve the thermal insulation value of the produced foam.
  • Blocking agents are typically used in amounts less than about 1 wt% of the foam.
  • a typical polyol mixture as set forth in Table 1 was used to measure the solubility of blowing agents.
  • the formulations tested (all had an Iso Index of 114) each contained: Rubinate M, a polymeric methyl diphenyl diisocyanate (MDI) available from Huntsman; Jeffol R-425-X, a polyol available from Huntsman; Voranol 490, a polyol available from Dow Chemical; Terate 2541, a polyol available from Invista; TCPP, a flame retardant available from Rhodia; TegostabB 8465 a surfactant available from Evonik-Degussa; Polycat 8 (DMCHA) and 5 (PMDETA) available from Air Products.
  • the total blowing level was 24.5 mls/g. Table 1 summarizes the test formula when HFC 134a was used alone.
  • a B-side made up of a mixture of the polyol, surfactant, catalysts, and other components without the blowing agent was pre-blended externally before pouring into the B-tank of Edge-Sweets high-pressure foam machine.
  • the B-tank was then sealed and agitated, and circulation started.
  • the B-tank was cooled to 7O 0 F with a cooling jacket.
  • the blowing agent was added to the B-tank mixture by static mixing in a circulation loop. After two hours of agitation and circulation, the B-tank pressure reached equilibrium.
  • Table 2 summarizes the tank pressure of different blowing agent mixtures at equilibrium.
  • Table 2 shows that the measured tank pressures were significantly lower than theoretical tank pressures when HFC32 was mixed with HFCl 34a.
  • the theoretical tank pressures were calculated based upon the assumption that HFC32 has same solubility in the polyol mixture as HFC 134a.
  • the lower tank pressures for the mixtures that include HFC32 indicate that HFC32 has significantly better solubility than HFC 134a.
  • the A-side, polymeric MDI and B-side mixture were mixed in the impingement mixer of the Edge-Sweets high-pressure foam machine and dispensed into a container.
  • the resulting foam had free rise density of 1.8 to 1.9 lb/ft 3 .
  • Molded foam was also made by dispensing the material in to a closed mold that was pre-heated at 115 0 F and allowing the mixture to expand. The mold was kept closed for approximately 30 minutes before releasing the foam.
  • the closed cell content was measured according to ASTM 2856.
  • the present invention provides a method for producing a thermosetting foam.
  • the blowing agent combination comprises a combination of HFC 134a and HFC32 comprising of less than about 30 wt% of HFC32.

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

Abstract

A thermosetting plastic foam such as expanded polyurethane made with a blowing agent for which is a blend that includes HFC-134a (1,1,1,2-tetrafluoroethane) and difluoromethane (HFC-32). The blowing agent combination is non-flammable and enhances processability of thermosetting foams.

Description

Non-Flammable Hydrofluorocarbon Blowing Agent Composition
Field of the Invention
The present invention relates to thermosetting foam foamable compositions, such as polyurethane, which include non-flammable blowing agents. More particularly, the present invention relates to thermosetting foam foamable compositions which incorporate a non-flammable blowing agent combination including HFC- 134a and HFC-32.
Description of the Invention
The foamable compositions of the present invention generally are formed from one or more components capable of forming foam having a generally cellular structure and a blowing agent combination. In certain embodiments, the one or more components comprise a thermosetting composition capable of forming foam and/or foamable compositions. Examples of thermosetting compositions include polyurethane and polyisocyanurate foam compositions, and also phenolic foam compositions. In such thermosetting foam embodiments, the blowing agent compositions of the present invention are included as a blowing agent in the foamable composition, or as a part of one or more of a two or more part foamable mixture. The one or more parts include one or more components capable of reacting and/or foaming under the proper conditions to form a foam or cellular structure.
The Montreal Protocol for the protection of the ozone layer, signed in October 1987, mandated the phase out of the use of chlorofluorocarbons (CFCs) which had been used as blowing agents for thermosetting foams. Materials more "friendly" to the ozone layer, such as hydrofluorocarbons (HFCs) eg HFC- 134a replaced chlorofluorocarbons. HFC 134a (1,1,1,2-tetrafluoroethane) is non-flammable and contributes to long-term thermal insulation for thermosetting foams, such as polyurethane foams. However, HFC 134a exhibits a lower solubility in foaming mixture components, relative to previous materials. This lower solubility makes HFC134a less desirable than previous materilas for the urethane industry. The present inventors found that use of HFC 134a in combination with HFC32 (difluoromethane) provided a foaming agent blend that exhibits a higher, acceptable solubility in polyol mixtures. Use of HFC32 has been limted due to it's flammability. The present inventors discovered that HFC 134a suppressses the undesirable flammability of HFC32. The present inventors have found that blends of HFC 134a and HFC32 that consist of less than about 30 wt% of HFC32 are not flammable. Working with such non-flammable blends, the inventors found improved solubility in polyol mixtures over HFC 134a alone. As a result of improved solubility, foams made with this blowing agent blend exhibited improved processing and performance.
The blowing agent combinations of the present invention can be used as a foaming agent for polyolefm foams by being mixed in a polyol mixture (typically referred to as the B side) which form foam when mixed with a polyisocyante mixture (typically referred to as the A side). The resulted foam products exhibit superior properties including decreased density and improved k-factor. The foaming agent combination readily dissolves in the components of thermosetting foams, and provides a degree of plasticization sufficient to produce acceptable foams.
Prior art teaches that HFC32 can be used as a foam blow agent for thermoplastic plastic polymer such as polystyrene. US 4,927,863 teaches that HCFC123, HCFC123a, and HCFC 14 IbI owing agents can be combined with shrinkage reducing hydrocarbons including CFC-11, CFC-12, HCFC-22, HFC-32, CFC-113, CFC-114, HCFC-124, HCFC- 133a, HFC- 134a, HCFC- 142b and HFC-152a to produce polyurethane which exhibits reduced foam shrinkage.
HFC32 is flammable which has limited its acceptance in certain applications. However, the present inventors found that HFC 134a can be combined with HFC32 to suppress its flammability. This is desirable for polyurethane foams especially for applications which are less tolerable to flammability.
The present inventors have examined blends including HFC 134a and HFC32 for flammability, solubility in polyol mixtures and performance in pour-in-place rigid polyurethane foam. It was found that when the blend consists of less than about 30 wt% of HFC32, the blend is not flammable. In addition, the blend was found to exhibit improved solubility in polyol mixtures over HFC 134a alone. As a result of the improved solubility, foams made with this blend exhibited improved processing and performance.
The HFCl 34a and HFC32 blend of the present invention can be used with other additives such as: co-blowing agent including but not limited to HFC245fa, HFC365mfc, HFC227, HFC125, and trans- 1,2-dichloroethylene; hydrogen bond forming blocking agents (e.g. organic ether, ester, or ketone) which reduce vapor pressure and reduce the escape of blowing agent from the foam to improve the thermal insulation value of the produced foam. Blocking agents are typically used in amounts less than about 1 wt% of the foam.
EXAMPLES
Example 1 Solubility of Blowing Agents in Polyol Mixtures
A typical polyol mixture as set forth in Table 1 was used to measure the solubility of blowing agents. The formulations tested (all had an Iso Index of 114) each contained: Rubinate M, a polymeric methyl diphenyl diisocyanate (MDI) available from Huntsman; Jeffol R-425-X, a polyol available from Huntsman; Voranol 490, a polyol available from Dow Chemical; Terate 2541, a polyol available from Invista; TCPP, a flame retardant available from Rhodia; TegostabB 8465 a surfactant available from Evonik-Degussa; Polycat 8 (DMCHA) and 5 (PMDETA) available from Air Products. The total blowing level was 24.5 mls/g. Table 1 summarizes the test formula when HFC 134a was used alone.
Table 1 Foam Formula
Figure imgf000004_0001
Figure imgf000005_0001
A B-side made up of a mixture of the polyol, surfactant, catalysts, and other components without the blowing agent was pre-blended externally before pouring into the B-tank of Edge-Sweets high-pressure foam machine. The B-tank was then sealed and agitated, and circulation started. The B-tank was cooled to 7O0F with a cooling jacket. The blowing agent was added to the B-tank mixture by static mixing in a circulation loop. After two hours of agitation and circulation, the B-tank pressure reached equilibrium. Table 2 summarizes the tank pressure of different blowing agent mixtures at equilibrium.
Table 2 Solubility of Blowing Agents in Polyol Blend
Figure imgf000005_0002
^correction after excluding contribution from air in the tank
The data in Table 2 shows that the measured tank pressures were significantly lower than theoretical tank pressures when HFC32 was mixed with HFCl 34a. The theoretical tank pressures were calculated based upon the assumption that HFC32 has same solubility in the polyol mixture as HFC 134a. The lower tank pressures for the mixtures that include HFC32 indicate that HFC32 has significantly better solubility than HFC 134a.
Example 2 k-Factor of Foams
The A-side, polymeric MDI and B-side mixture were mixed in the impingement mixer of the Edge-Sweets high-pressure foam machine and dispensed into a container. The resulting foam had free rise density of 1.8 to 1.9 lb/ft3. Molded foam was also made by dispensing the material in to a closed mold that was pre-heated at 1150F and allowing the mixture to expand. The mold was kept closed for approximately 30 minutes before releasing the foam.
The k-factor measurements (in accordance with ASTM C518) on the resulting foams were conducted between 10°F and 1300F. Initial k- factors are taken within 24 hours after removing the foam skin with a band saw. Lower k-factors indicate better insulation values. The results are summarized in Table 3.
Table 3 k-Factor of Foam
Figure imgf000006_0001
The results in Table 3 show that as the level of HFC32 increased, k- factor decreased up to a point, thereafter, further increase in the HFC32 level resulted in increased k-factor.
Example 3 Dimensional Stability of Foams
The dimensional stability of resulted foam was measured according the ASTM
D2126.
Table 4 Dimensional Stability of Foam
Figure imgf000007_0001
The results were as shown in Table 4 show that the higher the percentage of HFC32, the better the dimensional stability.
Example 4 Closed Cell Content of Foam
The closed cell content was measured according to ASTM 2856.
Table 5 Closed Cell Content of Foam
Figure imgf000007_0002
The data in Table 5 shows that the closed cell content increases as the percentage of HFC32 is increase up to a point, thereafter, further increase in the HFC32 level resulted in reducing the number of closed cells.
The present invention provides a method for producing a thermosetting foam. The blowing agent combination comprises a combination of HFC 134a and HFC32 comprising of less than about 30 wt% of HFC32.
While the present invention has been described with respect to particular embodiments thereof, it is apparent that numerous other forms and modifications of this invention will be obvious to those skilled in the art. The appended claims and this invention generally should be construed to cover all such obvious forms and modifications which are within the true spirit and scope of the present invention.

Claims

1. A method for producing a rigid thermosetting foam wherein the improvement using as blowing agent, a nonflammable combination of difiuoromethane and 1,1,1,2- tetrafluoroethane.
2. The method of claim 1 wherein said nonflammable combination comprises less than about 30 wt% difiuoromethane.
3. The method of claim 1 wherein said nonflammable blowing agent further comprises a coblowing agent selecteed from the group consisting of HFC245fa, HFC365mfc, HFC227, HFC125, and trans- 1 ,2-dichloroethylene
4. The method of claim 1 wherein said nonflammable blowing agent further comprises a hydrogen bond forming blocking agent.
5. The method of claim 1 wherein said rigid thermosetting foam is a polyurethane foam, a polyisocyanurate foam or a phenolic foam.
PCT/US2008/054718 2007-03-09 2008-02-22 Non-flammable hydrofluorocarbon blowing agent composition WO2008112406A1 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014206679A1 (en) * 2013-06-28 2014-12-31 Basf Se Hydrolysis-resistant polyurethane moulding

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5716549A (en) * 1993-03-05 1998-02-10 Ikon Corporation Fluoroiodocarbon blends as CFC and halon replacements

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5716549A (en) * 1993-03-05 1998-02-10 Ikon Corporation Fluoroiodocarbon blends as CFC and halon replacements

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014206679A1 (en) * 2013-06-28 2014-12-31 Basf Se Hydrolysis-resistant polyurethane moulding
EP2818489A1 (en) * 2013-06-28 2014-12-31 Basf Se Hydrolysis resistant PUR molded parts
CN105492483A (en) * 2013-06-28 2016-04-13 巴斯夫欧洲公司 Hydrolysis-resistant polyurethane moulding

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