US20090253820A1 - Foaming agents and compositions containing fluorine sustituted olefins and methods of foaming - Google Patents

Foaming agents and compositions containing fluorine sustituted olefins and methods of foaming Download PDF

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Publication number
US20090253820A1
US20090253820A1 US12/276,137 US27613708A US2009253820A1 US 20090253820 A1 US20090253820 A1 US 20090253820A1 US 27613708 A US27613708 A US 27613708A US 2009253820 A1 US2009253820 A1 US 2009253820A1
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US
United States
Prior art keywords
hfc
blowing agent
foam
hfo
composition
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
Application number
US12/276,137
Other languages
English (en)
Inventor
James M. Bowman
David J. Williams
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.)
Honeywell International Inc
Original Assignee
Honeywell International Inc
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 US11/474,887 external-priority patent/US9796848B2/en
Priority claimed from PCT/US2007/064570 external-priority patent/WO2007109748A2/en
Application filed by Honeywell International Inc filed Critical Honeywell International Inc
Priority to US12/276,137 priority Critical patent/US20090253820A1/en
Priority to KR1020167023520A priority patent/KR20160104745A/ko
Priority to KR20157005312A priority patent/KR20150038512A/ko
Priority to CA2706774A priority patent/CA2706774C/en
Priority to EP08851933A priority patent/EP2215152A4/en
Priority to KR1020177021108A priority patent/KR20170091757A/ko
Priority to CN201510436991.2A priority patent/CN105111491A/zh
Priority to CA2997980A priority patent/CA2997980A1/en
Priority to JP2010535113A priority patent/JP2011504538A/ja
Priority to CN201510437927.6A priority patent/CN105111492A/zh
Priority to KR1020147023257A priority patent/KR20140119134A/ko
Priority to KR1020197000987A priority patent/KR20190007105A/ko
Priority to PCT/US2008/084512 priority patent/WO2009067720A2/en
Priority to KR1020107014118A priority patent/KR20100112562A/ko
Priority to MX2010005669A priority patent/MX2010005669A/es
Priority to CN2008801257097A priority patent/CN101925644A/zh
Priority to TW104134781A priority patent/TWI612085B/zh
Priority to TW97145587A priority patent/TW200932807A/zh
Priority to US12/351,807 priority patent/US9499729B2/en
Assigned to HONEYWELL INTERNATIONAL INC. reassignment HONEYWELL INTERNATIONAL INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: BOWMAN, JAMES M., WILLIAMS, DAVID J.
Publication of US20090253820A1 publication Critical patent/US20090253820A1/en
Priority to US13/394,289 priority patent/US8962707B2/en
Priority to US12/890,143 priority patent/US20110037016A1/en
Priority to US13/191,070 priority patent/US9000061B2/en
Priority to US13/191,141 priority patent/US9181410B2/en
Priority to US13/298,452 priority patent/US9175200B2/en
Priority to US13/585,755 priority patent/US8729145B2/en
Priority to US14/282,909 priority patent/US20140336292A1/en
Priority to JP2014191142A priority patent/JP2015017268A/ja
Priority to US14/630,166 priority patent/US20150231527A1/en
Priority to US14/679,802 priority patent/US9701782B2/en
Priority to US14/936,214 priority patent/US20160186917A1/en
Priority to US15/200,268 priority patent/US20160310922A1/en
Priority to JP2016132325A priority patent/JP6307116B2/ja
Priority to US15/439,840 priority patent/US20170158834A1/en
Priority to JP2018040959A priority patent/JP2018127628A/ja
Abandoned legal-status Critical Current

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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
    • C08J9/06Working-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 chemical blowing agent
    • 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
    • C08J9/127Mixtures of organic and inorganic blowing agents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B5/00Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts
    • B32B5/18Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts characterised by features of a layer of foamed material
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F112/00Homopolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
    • C08F112/02Monomers containing only one unsaturated aliphatic radical
    • C08F112/04Monomers containing only one unsaturated aliphatic radical containing one ring
    • C08F112/06Hydrocarbons
    • C08F112/08Styrene
    • 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
    • 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
    • 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
    • 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
    • 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
    • C08J9/146Halogen containing compounds containing carbon, halogen and hydrogen only only fluorine as halogen atoms
    • 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
    • C08J9/147Halogen containing compounds containing carbon and halogen atoms only
    • C08J9/148Halogen containing compounds containing carbon and halogen atoms only perfluorinated
    • 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
    • C08J9/149Mixtures of blowing agents covered by more than one of the groups C08J9/141 - C08J9/143
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K23/00Use of substances as emulsifying, wetting, dispersing, or foam-producing agents
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K3/00Materials not provided for elsewhere
    • C09K3/10Materials in mouldable or extrudable form for sealing or packing joints or covers
    • C09K3/1006Materials in mouldable or extrudable form for sealing or packing joints or covers characterised by the chemical nature of one of its constituents
    • C09K3/1009Fluorinated polymers, e.g. PTFE
    • 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
    • C08J2203/00Foams characterized by the expanding agent
    • C08J2203/06CO2, N2 or noble gases
    • 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
    • C08J2203/00Foams characterized by the expanding agent
    • C08J2203/12Organic compounds only containing carbon, hydrogen and oxygen atoms, e.g. ketone or alcohol
    • 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
    • C08J2203/00Foams characterized by the expanding agent
    • C08J2203/14Saturated hydrocarbons, e.g. butane; Unspecified hydrocarbons
    • 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
    • C08J2203/00Foams characterized by the expanding agent
    • C08J2203/16Unsaturated hydrocarbons
    • C08J2203/162Halogenated unsaturated hydrocarbons, e.g. H2C=CF2
    • 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
    • C08J2207/00Foams characterised by their intended use
    • C08J2207/04Aerosol, e.g. polyurethane foam spray
    • 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
    • C08J2325/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Derivatives of such polymers
    • C08J2325/02Homopolymers or copolymers of hydrocarbons
    • C08J2325/04Homopolymers or copolymers of styrene
    • C08J2325/06Polystyrene
    • 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
    • C08J2375/00Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
    • C08J2375/04Polyurethanes
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    • 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
    • C08J9/122Hydrogen, oxygen, CO2, nitrogen or noble gases
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    • 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
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    • 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
    • C08J9/145Halogen containing compounds containing carbon, halogen and hydrogen only only chlorine as halogen atoms
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/02Halogenated hydrocarbons
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/249921Web or sheet containing structurally defined element or component
    • Y10T428/249953Composite having voids in a component [e.g., porous, cellular, etc.]
    • Y10T428/249987With nonvoid component of specified composition
    • Y10T428/249988Of about the same composition as, and adjacent to, the void-containing component
    • Y10T428/249989Integrally formed skin

Definitions

  • compositions, methods and systems having utility in numerous applications, including particularly in blowing agents, foamable compositions, foams and articles made with or from foams.
  • the present invention is directed to such compositions which comprise at least one multi-fluorinated olefin and at least one additional component which is either another multi-fluorinated olefin or another compound which is not a multi-fluorinated olefin.
  • Fluorocarbon based fluids have found widespread use in many commercial and industrial applications, including as aerosol propellants and as blowing agents. Because of certain suspected environmental problems, including the relatively high global warming potentials, associated with the use of some of the compositions that have heretofore been used in these applications, it has become increasingly desirable to use fluids having low or even zero ozone depletion potential, such as hydrofluorocarbons (“HFCs”). Thus, the use of fluids that do not contain substantial amounts of chlorofluorocarbons (“CFCs”) or hydrochlorofluorocarbons (“HCFCs”) is desirable. Furthermore, some HFC fluids may have relatively high global warming potentials associated therewith, and it is desirable to use hydrofluorocarbon or other fluorinated fluids having as low global warming potentials as possible while maintaining the desired performance in use properties.
  • HFCs hydrofluorocarbons
  • CFC blowing agent substitutes to be effective without major engineering changes to conventional foam generating systems.
  • blowing agents have included, for example, azo compounds, various volatile organic compounds (VOCs) and chlorofluorocarbons (CFCs).
  • VOCs volatile organic compounds
  • CFCs chlorofluorocarbons
  • the chemical blowing agents typically undergo some form of chemical change, including chemical reaction with the material that forms the polymer matrix (usually at a predetermined temperature/pressure) that causes the release of a gas, such as nitrogen, carbon dioxide, or carbon monoxide.
  • a gas such as nitrogen, carbon dioxide, or carbon monoxide.
  • One of the most frequently used chemical blowing agents is water.
  • the physical blowing agents typically are dissolved in the polymer or polymer precursor material and then expand volumetrically (again at a predetermined temperature/pressure) to contribute to the formation of the foamed structure.
  • Physical blowing agents are frequently used in connection with thermoplastic foams, although chemical blowing agents can be used in place of or in addition to physical blowing agents in connection with thermoplastic foam.
  • chemical blowing agents in connection with the formation of polyvinylchloride-based foams.
  • CFC-11 CCl 3 F
  • HCFCs hydrogen-containing chlorofluoroalkanes
  • CHCl 2 CF 3 HCFC-123
  • CH 2 ClCHClF HCFC-141b
  • ODP Ozone Depletion Potential
  • HFCs non-chlorinated, partially hydrogenated fluorocarbons
  • HFC-245fa foams made with certain of the more modern HFC blowing agents, such as CF 3 CH 2 CF 2 H (“HFC-245fa”) offer improved thermal insulation, due in part to the low thermal conductivity of HFC-245fa vapor, and due in part to the fine cell structure HFC-245fa imparts to the foams.
  • HFC-245fa has been widely used in insulation applications, particularly refrigerator, freezer, refrigerator/freezer and spray foam applications.
  • HFC fluids share the disadvantage of having relatively high global warming potentials, and it is desirable to use hydrofluorocarbon or other fluorinated fluids having as low global warming potentials as possible while maintaining the desired performance in use properties.
  • hydrofluorocarbon or other fluorinated fluids having as low global warming potentials as possible while maintaining the desired performance in use properties.
  • HFCs as blowing agents in foam insulation, particularly rigid foam insulation, has resulted in HFCs being less desirable candidates for blowing agents in commercial foam insulation.
  • Hydrocarbon blowing agents are also known.
  • U.S. Pat. No. 5,182,309 to Hutzen teaches the use of iso- and normal-pentane in various emulsion mixtures.
  • Another example of hydrocarbon blowing agents is cyclopentane, as taught by U.S. Pat. No. 5,096,933—Volkert.
  • many hydrocarbon blowing agents, such as cyclopentane, and isomers of pentane are zero ozone depleting agents and exhibit very low global warming potential, such material are less than fully desirable because foams produced from these blowing agents lack the same degree of thermal insulation efficiency as foams made with, for example, HFC-245fa blowing agent.
  • hydrocarbon blowing agents are extremely flammable, which is undesirable. Also, certain hydrocarbon blowing agents have inadequate miscibility in certain situations with material from which the foam is formed, such as many of the polyester polyols commonly used in polyisocyanurate modified polyurethane foam. The use of these alkanes frequently requires a chemical surfactant to obtain a suitable mixture.
  • nonflammable refers to compounds or compositions which are determined to be nonflammable as determined in accordance with ASTM standard E-681, dated 2002, which is incorporated herein by reference. Unfortunately, many HFC's which might otherwise be desirable for used in foam blowing agent compositions are not nonflammable.
  • fluoroalkane difluoroethane HFC-152a
  • fluoroalkene 1,1,1-trifluorpropene HFO-1243zf
  • HFE-254pc fluorinated ether 1,1,22-tetrafluoroethyl methyl ether
  • HFE-254cb fluorinated ether 1,1,22-tetrafluoroethyl methyl ether
  • bromine-containing halocarbon additives to decrease flammability of certain materials, including foam blowing agents, in U.S. Pat. No. 5,900,185—Tapscott.
  • the additives in this patent are said to be characterized by high efficiency and short atmospheric lifetimes, that is, low ozone depletion potential (ODP) and a low global warming potential (GWP).
  • ODP ozone depletion potential
  • GWP global warming potential
  • blowing agent substitutes it is generally considered desirable for blowing agent substitutes to be effective without major engineering changes to conventional equipment and systems used in foam preparation and formation.
  • compositions and particularly blowing agents, foamable compositons, foamed articles and methods and systems for forming foam, which provide beneficial properties and/or avoid one or more of the disadvantages noted above.
  • This invention relates to compositions, methods and systems having utility in numerous applications, including particularly in connection with compositions, methods, systems and agents relating to polymeric foams.
  • blowing agent compositions comprising one or more C2 to C6 fluoroalkenes, more preferably one or more C3 to C5 fluoroalkenes, and even more preferably one or more compounds having Formula I as follows:
  • X is a C 1 , C 2 , C 3 , C 4 , or C 5 unsaturated, substituted or unsubstituted radical
  • each R is independently Cl, F, Br, I or H
  • z is 1 to 3, it generally being preferred that the fluoroalkene of the present invention has at least four (4) halogen substituents, at least three of which are F and even more preferably none of which are Br.
  • the compound includes no hydrogen.
  • the Br substituent is on an unsaturated carbon, and even more preferably the Br substituent is on a non-terminal unsaturated carbon.
  • One particularly preferred compound in this class is CF 3 CBr ⁇ CF 2 , including all of its isomers
  • the compounds of Formula I are propenes, butenes, pentenes and hexenes having from 3 to 5 fluorine substituents, with other substituents being either present or not present.
  • no R is Br
  • the unsaturated radical contains no Br substituents.
  • tetrafluoropropenes (HFO-1234) and fluorochloroporpenes (such as trifluoro, monochloropropenes (HFCO-1233)) are especially preferred in certain embodiments.
  • pentafluoropropenes are preferred, including particularly those pentafluoropropenes in which there is a hydrogen substituent on the terminal unsaturated carbon, such as CF 3 CF ⁇ CFH (HFO-1225yez), particularly since applicants have discovered that such compounds have a relatively low degree of toxicity in comparison to at least the compound CF 3 CH ⁇ CF 2 (HFO-1225zc).
  • CF 3 CF ⁇ CFH HFO-1225yez
  • fluorochlorobutenes are especially preferred in certain embodiments.
  • HFO-1234 is used herein to refer to all tetrafluoropropenes. Among the tetrafluoropropenes are included 1,1,1,2-tetrafluoropropene (HFO-1234yf) and both cis- and trans-1,1,1,3-tetrafluoropropene (HFO-1234ze).
  • HFO-1234ze is used herein generically to refer to 1,1,1,3-tetrafluoropropene, independent of whether it is the cis- or trans-form.
  • cisHFO-1234ze and “transHFO-1234ze” are used herein to describe the cis- and trans-forms of 1,1,1,3-tetrafluoropropene respectively.
  • HFO-1234ze therefore includes within its scope cisHFO-1234ze, transHFO-1234ze, and all combinations and mixtures of these.
  • HFO-1233 is used herein to refer to all trifluoro, monochloropropenes. Among the trifluoro,monochloropropenes are included 1,1,1,trifluoro-2,chloro-propene (HFCO-1233xf) and both cis- and trans-1,1,1-trifluo-3,chlororopropene (HFCO-1233zd).
  • HFCO-1233zd is used herein generically to refer to 1,1,1-trifluo-3,chloro-propene, independent of whether it is the cis- or trans-form.
  • cisHFCO-1233zd and “transHFCO-1233zd” are used herein to describe the cis- and trans-forms of 1,1,1-trifluo,3-chlororopropene, respectively.
  • HFCO-1233zd therefore includes within its scope cisHFCO-1233zd, transHFCO-1233zd, and all combinations and mixtures of these.
  • HFO-1225 is used herein to refer to all pentafluoropropenes. Among such molecules are included 1,1,1,2,3 pentafluoropropene (HFO-1225yez), both cis- and trans-forms thereof.
  • HFO-1225yez is thus used herein generically to refer to 1,1,1,2,3 pentafluoropropene, independent of whether it is the cis- or trans-form.
  • HFO-1225yez therefore includes within its scope cisHFO-1225yez, transHFO-1225yez, and all combinations and mixtures of these.
  • the present invention provides blowing agent compositions, foamable compositions, foams and/or foamed articles comprising one or more C2 to C6 fluorinated alkenes, and more preferably C3 to C4 fluorinated alkenes, including any one or more of the preferred groups and/or preferred individual fluorinated alkene compounds mentioned herein, and one or more additional compounds selected from the group consisting of hydrocarbons, hydrofluorocarbons (HFCs), ethers, alcohols, aldehydes, ketones, methyl formate, formic acid, water, trans-1,2-dichloroethylene, carbon dioxide and combinations of any two or more of these.
  • HFCs hydrofluorocarbons
  • ethers it is preferred in certain embodiments to use ethers having from one to six carbon atoms.
  • alcohols it is preferred in certain embodiments to use alcohols having from one to four carbon atoms.
  • aldehydes it is preferred in certain embodiments to use aldehydes having from one to four carbon atoms.
  • ketones it is preferred in certain embodiments to use ketones, having from one to four carbon atoms.
  • the present invention provides also methods and systems which utilize the compositions of the present invention, including methods and systems for foam blowing.
  • the present compositions can generally be in the form of blowing agent compositions or foamable compositions.
  • the present invention requires at least one fluoroalkene compound as described herein and optionally but preferably one or more additional components, as described generally above and in more detail below.
  • the preferred embodiments of the present invention are directed to compositions comprising at least one fluoroalkene containing from 2 to 6, preferably 3 to 5 carbon atoms, more preferably 3 to 4 carbon atoms, and in certain embodiments most preferably three carbon atoms, and at least one carbon-carbon double bond.
  • the fluoroalkene compounds of the present invention are sometimes referred to herein for the purpose of convenience as hydrofluoro-olefins or “HFOs” if they contain at least one hydrogen. Although it is contemplated that the HFOs of the present invention may contain two carbon—carbon double bonds, such compounds at the present time are not considered to be preferred.
  • HFOs which also contain at least one chlorine atom, the designation HFCO is sometimes used herein
  • compositions comprise one or more compounds in accordance with Formula I.
  • compositions include one or more compounds of Formula II below:
  • each R is independently Cl, F, Br, I or H
  • R′ is (CR 2 ) n Y
  • n is 0, 1, 2 or 3, preferably 0 or 1, it being generally preferred however that either Br is not present in the compound or when Br is present in the compound there is no hydrogen in the compound.
  • Y is CF 3
  • n is 0 or 1 (most preferably 0) and at least one of the remaining Rs is F, and preferably no R is Br, or when Br is present there is no hydrogen in the compound. It is preferred in certain cases that no R in Formula II is Br.
  • the compound of the present invention comprises a C 3 or C 4 HFO or HFCO, preferably in certain embodiments a C 3 HFO, and more preferably a compound in accordance with Formula I in which X is a halogen substituted C 3 alkylene and z is 3.
  • X is fluorine and/or chlorine substituted C 3 alkylene, with the following C 3 alkylene radicals being preferred in certain embodiments:
  • Such embodiments therefore comprise the following preferred compounds: CF 3 —CH ⁇ CF—CH 3 ; CF 3 —CF ⁇ CH—CH 3 ; CF 3 —CH 2 —CF ⁇ CH 2 ; CF 3 —CH 2 —CH ⁇ CFH; and combinations of these with one another and/or with other compounds in accordance with Formula I or Formula II.
  • the compound of the present invention comprises a C3 or C4 HFCO, preferably a C3 HFCO, and more preferably a compound in accordance with Formula II in which Y is CF 3 , n is 0, at least one R on the unsaturated terminal carbon is H, and at least one of the remaining Rs is Cl.
  • HFCO-1233 is an example of such a preferred compound.
  • compositions of the present invention comprise one or more tetrafluoropropenes, including HFO-1234yf, (cis)HFO-1234ze and (trans)HFO-1234ze, with HFO-1234ze being generally preferred and trans HFO-1234ze being highly preferred in certain embodiments.
  • HFO-1234ze being generally preferred
  • trans HFO-1234ze being highly preferred in certain embodiments.
  • (trans)HFO-1234ze may be preferred for use in certain systems because of its relatively low boiling point ( ⁇ 19° C.), while (cis)HFO-1234ze, with a boiling point of +9° C., may be preferred in other applications.
  • (cis)HFO-1234ze with a boiling point of +9° C.
  • combinations of the cis- and trans-isomers will be acceptable and/or preferred in many embodiments.
  • the terms “HFO-1234ze” and 1,3,3,3-tetrafluoropropene refer to both stereo isomers, and the use of this term is intended to indicate that each of the cis-and trans-forms applies and/or is useful for the stated purpose unless otherwise indicated.
  • HFO-1234 compounds are known materials and are listed in Chemical Abstracts databases.
  • fluoropropenes such as CF 3 CH ⁇ CH 2 by catalytic vapor phase fluorination of various saturated and unsaturated halogen-containing C 3 compounds is described in U.S. Pat. Nos. 2,889,379; 4,798,818 and 4,465,786, each of which is incorporated herein by reference.
  • EP 974,571 discloses the preparation of 1,1,1,3-tetrafluoropropene by contacting 1,1,1,3,3-pentafluoropropane (HFC-245fa) in the vapor phase with a chromium-based catalyst at elevated temperature, or in the liquid phase with an alcoholic solution of KOH, NaOH, Ca(OH) 2 or Mg(OH) 2 .
  • HFC-245fa 1,1,1,3,3-pentafluoropropane
  • compositions may comprise combinations of any two or more compounds within the broad scope of the invention or within any preferred scope of the invention.
  • the present compositions are believed to possess properties that are advantageous for a number of important reasons. For example, applicants believe, based at least in part on mathematical modeling, that the fluoroolefins of the present invention will not have a substantial negative affect on atmospheric chemistry, being negligible contributors to ozone depletion in comparison to some other halogenated species.
  • the preferred compositions of the present invention thus have the advantage of not contributing substantially to ozone depletion.
  • the preferred compositions also do not contribute substantially to global warming compared to many of the hydrofluoroalkanes presently in use.
  • compositions of the present invention have a Global Warming Potential (GWP) of not greater than about 1000, more preferably not greater than about 500, and even more preferably not greater than about 150.
  • GWP of the present compositions is not greater than about 100 and even more preferably not greater than about 75.
  • GWP is measured relative to that of carbon dioxide and over a 100 year time horizon, as defined in “The Scientific Assessment of Ozone Depletion, 2002, a report of the World Meteorological Association's Global Ozone Research and Monitoring Project,” which is incorporated herein by reference.
  • the present compositions also preferably have an Ozone Depletion Potential (ODP) of not greater than 0.05, more preferably not greater than 0.02 and even more preferably about zero.
  • ODP Ozone Depletion Potential
  • “ODP” is as defined in “The Scientific Assessment of Ozone Depletion, 2002, A report of the World Meteorological Association's Global Ozone Research and Monitoring Project,” which is incorporated herein by reference.
  • the amount of the Formula I compounds, particularly HFO-1234 and even more preferably HFO-1234ze, contained in the present compositions can vary widely, depending the particular application, and compositions containing more than trace amounts and less than 100% of the compound are within broad the scope of the present invention.
  • the compositions of the present invention can be azeotropic, azeotrope-like or non-azeotropic.
  • the present compositions, particularly blowing agent compositions comprise Formula I and/or Formula II compounds, preferably HFO-1234 and more preferably HFO-1234ze and/or HFO-1234yf, in amounts from about 1% by weight to about 99% by weight, more preferably from about 5% to about 95% by weight, and even more preferably from 40% to about 90% by weight.
  • blowing agent compositions consist of or consist essentially of one or more compounds in accordance with Formula I hereof.
  • the present invention includes methods and systems which include using one or more of the compounds of the present invention as a blowing agent without the presence of any substantial amount of additional components.
  • one or more compounds or components that are not within the scope of Formula I or Formula II are optionally, but preferably, included in the blowing agent compositions of the present invention.
  • Such optional additional compounds include, but are not limited to, other compounds which also act as blowing agents (hereinafter referred to for convenience but not by way of limitation as co-blowing agents), surfactants, polymer modifiers, toughening agents, colorants, dyes, solubility enhancers, rheology modifiers, plasticizing agents, flammability suppressants, antibacterial agents, viscosity reduction modifiers, fillers, vapor pressure modifiers, nucleating agents, catalysts and the like.
  • dispersing agents, cell stabilizers, surfactants and other additives may also be incorporated into the blowing agent compositions of the present invention.
  • Certain surfactants are optionally but preferably added to serve as cell stabilizers.
  • DC-193, B-8404, and L-5340 are, generally, polysiloxane polyoxyalkylene block co-polymers such as those disclosed in U.S. Pat. Nos. 2,834,748, 2,917,480, and 2,846,458, each of which is incorporated herein by reference.
  • blowing agent mixture may include flame retardants such as tri(2-chloroethyl)phosphate, tri(2-chloropropyl)phosphate, tri(2,3-dibromopropyl)-phosphate, tri(1,3-dichloropropyl) phosphate, diammonium phosphate, various halogenated aromatic compounds, antimony oxide, aluminum trihydrate, polyvinyl chloride, and the like.
  • flame retardants such as tri(2-chloroethyl)phosphate, tri(2-chloropropyl)phosphate, tri(2,3-dibromopropyl)-phosphate, tri(1,3-dichloropropyl) phosphate, diammonium phosphate, various halogenated aromatic compounds, antimony oxide, aluminum trihydrate, polyvinyl chloride, and the like.
  • nucleating agents all known compounds and materials having nucleating functionality are available for use in the present invention, including particularly talc.
  • compositions that modulate a particular property of the compositions (such as cost for example) may also be included in the present compositions, and the presence of all such compounds and components is within the broad scope of the invention.
  • the preferred embodiments of the present compositions include, in addition to the compounds of Formula I (including particularly HFO-1234ze and/or HFO-1234yf), one or more co-blowing agents.
  • the co-blowing agent in accordance with the present invention can comprise a physical blowing agent, a chemical blowing agent (which preferably in certain embodiments comprises water) or a blowing agent having a combination of physical and chemical blowing agent properties.
  • the blowing agents included in the present compositions, including the compounds of Formula I as well as the co-blowing agent may exhibit properties in addition to those required to be characterized as a blowing agent.
  • blowing agent compositions of the present invention may include components, including the compounds or Formula I described above, which also impart some beneficial property to the blowing agent composition or to the foamable composition to which it is added.
  • the compound of Formula I or for the co-blowing agent may also act as a polymer modifier or as a viscosity reduction modifier.
  • present compositions include at least one ether, preferably which functions as a co-blowing agent in the composition.
  • the ether(s) used in accordance with this aspect of the invention comprise fluorinated ethers (FEs), more preferably one or more hydro-fluorinated ethers (HFEs)), and even more preferably one or more C3 to C5 hydro-fluorinated ethers in accordance with Formula (III) below:
  • a 1-6, more preferably 2-5, and even more preferably 3-5,
  • b 1-12, more preferably 1-6, and even more preferably 3-6,
  • c 1-12, more preferably 1-6, and even more preferably 2-6,
  • e 0-5, more preferably 1-3
  • f 0-5, more preferably 0-2,
  • compositions comprising at least one fluoroalkene as described herein and at least one fluoro-ether, more preferably at least one hydro-fluoroether, containing from 2 to 8, preferably 2 to 7, and even more preferably 2 to 6 carbon atoms, and in certain embodiments most preferably three carbon atoms.
  • the hydro-fluoroether compounds of the present invention are sometimes referred to herein for the purpose of convenience as hydrofluoro-ethers or “HFEs” if they contain at least one hydrogen.
  • the fluoroethers in accordance with the present disclosure and in particular in accordance with above identified Formula (III) are generally effective and exhibit utility in combination with the fluoroalkene compounds in accordance with the teachings contained herein.
  • the fluroethers it is preferred to use in certain embodiments, especially embodiments relating to blowing agent compositions and foam and foaming methods, to utilize hydrofluorethers that are at least difluorinated, more preferbably at least trifluorinated, and even more preferably at least tetra-fluorinated.
  • tetrafluorinated fluorethers having from 3 to 5 carbon atoms, more preferably 3 to 4 carbon atoms, and even more preferably 3 carbon atoms.
  • the compound of the present invention comprises a 1,1,2,2-tetrafluoroethylmethylether (which is sometimes referred to herein as HFE-245pc or HFE-245cb2), including any and all isomeric forms thereof.
  • HFE-245pc 1,1,2,2-tetrafluoroethylmethylether
  • the amount of the Formula III compounds, particularly 1,1,2,2-tetrafluoroethylmethylether contained in the present compositions can vary widely, depending the particular application, and compositions containing more than trace amounts and less than 100% of the compound are within broad the scope of the present invention.
  • the present compositions, particularly blowing agent compositions comprise Formula III compounds, including preferred groups of compounds, in amounts from about 1% by weight to about 99% by weight, more preferably from about 5% to about 95% by weight, and even more preferably from 40% to about 90% by weight.
  • HFE-7100 a material sold under the trade name HFE-7100 by 3M, which is understood to be a mixture of from about 20% to about 80% of methyl nonafluoroisobutyl ether and from about 20% to about 80% methyl nonafluorobutyl ether, may be used to advantage in accordance with certain preferred embodiments of the present invention.
  • a material sold under the trade name HFE-7200 by 3M which is understood to be a mixture of from about 20% to about 80% of ethyl nonafluoroisobutyl ether and from about 20% to about 80% ethyl nonafluorobutyl ether, may be used to advantage in accordance with certain preferred embodiments of the present invention.
  • any one or more of the above-listed HFEs may be used in combination with other compounds as well, including other HFEs not specifically listed herein and/or other compounds with which the designated fluoroether is known to form an azeotrope.
  • each of the following compounds is known to form an azeotrope with trans-dichloroethylene, and it is contemplated that for the purposes of the present invention the use of such azeotropes should be considered to be within the broad scope of the invention:
  • the blowing agent compositions of the present invention include one or more HFCs as co-blowing agents, more preferably one or more C1-C4 HFCs.
  • the present blowing agent compositions may include one or more of difluoromethane (HFC-32), fluoroethane (HFC-161), difluoroethane (HFC-152), trifluoroethane (HFC-143), tetrafluoroethane (HFC-134), pentafluoroethane (HFC-125), pentafluoropropane (HFC-245), hexafluoropropane (HFC-236), heptafluoropropane (HFC-227ea), pentafluorobutane (HFC-365), hexafluorobutane (HFC-356) and all isomers of all such HFC's.
  • HFC isomers are preferred for use as co-blowing agents in the compositions of the present invention:
  • the blowing agent compositions of the present invention include one or more hydrocarbons, more preferably C3-C6 hydrocarbons.
  • the present blowing agent compositions may include in certain preferred embodiments, for example: propane; iso- and normal-butane (each of such butanes being preferred for use as a blowing agent for for thermoplastic foams); iso-, normal-, neo- and/or cyclo-pentane (each of such pentanes being preferable for use as a blowing agent for thermoset foams); iso- and normal-hexane; and heptanes.
  • the blowing agent compositions of the present invention include one or more alcohols, preferably one or more C1-C4 alcohols.
  • the present blowing agent compositions may include one or more of methanol, ethanol, propanol, isopropanol, butanol, iosbutanol, t-butanol.
  • blowing agent compositions of the present invention include one or more aldehydes, particularly Cl-C4 aldehydes, including formaldehyde, acetaldehyde, propanal, butanal and isobutanal.
  • the blowing agent compositions of the present invention include one or more ketones, preferably Cl-C4 ketones.
  • the present blowing agent compositions may include one or more of acetone, methylethylketone, and methylisobutylketone.
  • the relative amount of any of the above noted additional, compounds, which are contemplated for use in certain embodiments as co-blowing agents, as well as any additional components which may be included in present compositions can vary widely within the general broad scope of the present invention according to the particular application for the composition, and all such relative amounts are considered to be within the scope hereof.
  • one particular advantage of at least certain of the compounds of Formula I in accordance with the present invention for example HFO-1234ze, is the relatively low flammability of such compounds.
  • the blowing agent composition of the present invention comprise at least one co-blowing agent and an amount of compound(s) in accordance with Formula I sufficient to produce a blowing agent composition which is overall nonflammable.
  • the relative amounts of the co-blowing agent in comparison to the compound of Formula I will depend, at least in part, upon the flammability of the co-blowing agent.
  • the blowing agent compositions of the present invention may include the compounds of the present invention in widely ranging amounts. It is generally preferred, however, that for preferred compositions for use as blowing agents in accordance with the present invention, compound(s) in accordance with Formula I, and even more preferably Formula II, are present in an amount that is at least about 1% by weight, more preferably at least about 5% by weight, and even more preferably at least about 15% by weight, of the composition.
  • the blowing agent comprises at least about 50% by weight of the present blowing agent compound(s), and in certain embodiments the blowing agent consists essentially of compounds in accordance with the present invention.
  • the use of one or more co-blowing agents is consistent with the novel and basic features of the present invention. For example, it is contemplated that water will be used as either a co-blowing or in combination with other co-blowing agents (such as, for example, pentane, particularly cyclopentane) in a large number of embodiments.
  • the blowing agent compositions of the present invention may comprise, preferably in amounts of at least about 15% by weight of the composition, HFO-1234yf, cisHFO-1234ze, transHFO1234ze or combinations of two or more of these.
  • a co-blowing agent comprising water is included in the compositions, most preferably in compositions directed to the use of thermosetting foams.
  • the blowing agent compositions of the present invention comprise a combination of cisHFO-1234ze and transHFO1234ze in a cis:trans weight ratio of from about 1:99 to about 50:50, more preferably from about 10:90 to about 30:70.
  • a combination of cisHFO-1234ze and transHFO1234ze in a cis:trans weight ratio of from about 1:99 to about 10:90, and preferably from about 1:99 to about 5:95.
  • cisHFO-1234ze and transHFO1234ze in a cis:trans weight ratio of from about 1:99 to about 10:90, and preferably from about 1:99 to about 5:95.
  • the blowing agent composition comprises from about 30% to about 95% by weight, more preferably from about 30% to about 96%, more preferably from about 30% to about 97%, and even more preferably from about 30% to about 98% by weight, and even more preferably from about 30% to about 99% by weight of a compound of Formula I, more preferably a compound of Formula II, and even more preferably one or more HFO-1234 compounds, and from about 5% to about 90% by weight, more preferably from about 5% to about 65% by weight of co-blowing agent, including one or more fluoroethers.
  • the co-blowing agent comprises, and preferably consists essentially of a compound selected from the group consisting of, H 2 O, HFCs, HFEs, hydrocarbons, alcohols (preferably C2, C3 and/or C4 alcohols), CO 2 , and combinations of any two or more of these.
  • foamable compositions generally include one or more components capable of forming foam.
  • foam foaming agent is used to refer to a component, or a combination on components, which are capable of forming a foam structure, preferably a generally cellular foam structure.
  • the foamable compositions of the present invention include such component(s) and a blowing agent compound, preferably a compound of Formula I, in accordance with the present invention.
  • the one or more components capable of forming foam comprise a thermosetting composition capable of forming foam and/or foamable compositions. Examples of thermosetting compositions include isocyanate-based compositions and phenolic-based compositions.
  • polyurethane compositions preferred are polyurethane compositions, polyisocyanurate, and polyurethane/polyisocyanurate.
  • foam types particularly polyurethane foam compositions
  • the present invention provides rigid foam (both closed cell, open cell and any combination thereof), flexible foam, and semiflexible foam, including integral skin foams.
  • reaction and foaming process may be enhanced through the use of various additives such as catalysts and surfactant materials that serve to control and adjust cell size and to stabilize the foam structure during formation.
  • any one or more of the additional components described above with respect to the blowing agent compositions of the present invention could be incorporated into the foamable composition of the present invention.
  • one or more of the present compositions are included as or part of a blowing agent in a foamable composition, or as a part of a two or more part foamable composition, which preferably includes one or more of the components capable of reacting and/or foaming under the proper conditions to form a foam or cellular structure.
  • the one or more components capable of foaming comprise thermoplastic materials, particularly thermoplastic polymers and/or resins.
  • thermoplastic foam components include polyolefins, such as for example monovinyl aromatic compounds of the formula Ar-CHCH2 wherein Ar is an aromatic hydrocarbon radical of the benzene series such as polystyrene (PS).
  • PS polystyrene
  • suitable polyolefin resins in accordance with the invention include the various ethylene resins including the ethylene homopolymers such as polyethylene and ethylene copolymers, polypropylene (PP) and polyethyleneterepthalate (PET).
  • the thermoplastic foamable composition is an extrudable composition.
  • transHFO-1234ze trans-1,1,1,3-tetrafluoropropene
  • additional compound the amount of the transHFO-1234ze may vary widely, including in all cases constituting the balance of the composition after all other components in composition are accounted for.
  • the amount of the transHFO-1234ze in the composition can be in accordance with the following ranges: from about 1 wt % to about 99 wt %; from about 30 wt % to about 99 wt %; from about 50 wt % to about 99 wt %; from about 75 wt % to about 99 wt %; from about 85 wt % to about 99 wt %; from about 75 wt % to about 99 wt %; from about 20 wt % to about 80 wt %; from about 90 wt % to about 99 wt %; from about 95 wt % to about 99 wt %; from about 1 wt % to about 20 wt %; from about 1 wt % to about 40 wt %; from about 1 wt % to about 50 wt %; from about 5 wt % to about 20 wt %; from about 5 wt % to
  • compositions which include as an essential component cis-1,1,1,3-tetrafluoropropene (cisHFO-1234ze) and at least one additional compound.
  • cisHFO-1234ze an essential component cis-1,1,1,3-tetrafluoropropene
  • the amount of the cisHFO-1234ze may vary widely, including in all cases constituting the balance of the composition after all other components in composition are accounted for.
  • the amount of the cisHFO-1234ze in the composition can be in accordance with the following ranges: from about 1 wt % to about 99 wt %; from about 30 wt % to about 99 wt %; from about 50 wt % to about 99 wt %; from about 75 wt % to about 99 wt %; from about 85 wt % to about 99 wt %; from about 75 wt % to about 99 wt %; from about 20 wt % to about 80 wt %; from about 90 wt % to about 99 wt %; from about 95 wt % to about 99 wt %; from about 1 wt % to about 20 wt %; from about 1 wt % to about 40 wt %; from about 1 wt % to about 50 wt %; from about 5 wt % to about 20 wt %; from about
  • compositions which include as an essential component 1,1,1,2,3-pentafluoropropene (HFO-1225ye) and at least one additional compound.
  • HFO-1225ye 1,1,1,2,3-pentafluoropropene
  • the amount of the transHFO-1225ye may vary widely, including in all cases constituting the balance of the composition after all other components in composition are accounted for.
  • the amount of the HFO-1225ye in the composition can be in accordance with the following ranges: from about 1 wt % to about 99 wt %; from about 30 wt % to about 99 wt %; from about 50 wt % to about 99 wt %; from about 75 wt % to about 99 wt %; from about 85 wt % to about 99 wt %; from about 75 wt % to about 99 wt %; from about 20 wt % to about 80 wt %; from about 90 wt % to about 99 wt %; from about 95 wt % to about 99 wt %; from about 1 wt % to about 20 wt %; from about 1 wt % to about 40 wt %; from about 1 wt % to about 50 wt %; from about 5 wt % to about 20 wt %; from about 5 wt % to
  • compositions which include as an essential component CF 3 CH ⁇ CHCl (HFO-1233zd) and at least one additional compound.
  • HFO-1233zd CF 3 CH ⁇ CHCl
  • the amount of the HFO-1233zd may vary widely, including in all cases constituting the balance of the composition after all other components in composition are accounted for.
  • the amount of the HFO-1233zd in the composition can be in accordance with the following ranges: from about 1 wt % to about 99 wt %; from about 30 wt % to about 99 wt %; from about 50 wt % to about 99 wt %; from about 75 wt % to about 99 wt %; from about 85 wt % to about 99 wt %; from about 75 wt % to about 99 wt %; from about 20 wt % to about 80 wt %; from about 90 wt % to about 99 wt %; from about 95 wt % to about 99 wt %; from about 1 wt % to about 20 wt %; from about 1 wt % to about 40 wt %; from about 1 wt % to about 50 wt %; from about 5 wt % to about 20 wt %; from about 5 wt % to
  • the composition comprises H 2 O in an amount of from about 5% by weight to about 50% by weight of the total blowing agent composition, more preferably from about 10% by weight to about 40% by weight, and even more preferably of from about 10% to about 20% by weight of the total blowing agent.
  • the composition comprises CO 2 in an amount of from about 5% by weight to about 60% by weight of the total blowing agent composition, more preferably from about 20% by weight to about 50% by weight, and even more preferably of from about 40% to about 50% by weight of the total blowing agent.
  • the co-blowing agent comprises alcohols, (preferably C2, C3 and/or C4 alcohols)
  • the composition comprises alcohol in an amount of from about 5% by weight to about 40% by weight of the total blowing agent composition, more preferably from about 10% by weight to about 40% by weight, and even more preferably of from about 15% to about 25% by weight of the total blowing agent.
  • the HFC co-blowing agent preferably C2, C3, C4 and/or C5 HFC
  • HFC-152a difluoromethane
  • HFC-245 HFC pentafluoropropane
  • the HFC is preferably C2 - C4 HFC, and even more preferably C3 HFC, with penta-fluorinated C3 HFC, such as HFC-245fa, being highly preferred in certain embodiments.
  • the HFE co-blowing agent preferably C2, C3, C4 and/or C5 HFE
  • HFE-254 is preferably present in the composition in amounts of from of from about 5% by weight to about 80% by weight of the total blowing agent composition, more preferably from about 10% by weight to about 75% by weight, and even more preferably of from about 25% to about 75% by weight of the total blowing agent.
  • the HFE is preferably C2-C4 HFE, and even more preferably a C3 HFC, with tetra-fluorinated C3 HFE being highly preferred in certain embodiments.
  • the HC co-blowing agent (preferably C3, C4 and/or C5 HC) is preferably present in the composition in amounts of from of from about 5% by weight to about 80% by weight of the total blowing agent composition, and even more preferably from about 20% by weight to about 60% by weight of the total blowing agent.
  • the methods of the present invention generally require incorporating a blowing agent in accordance with the present invention into a foamable or foam forming composition and then foaming the composition, preferably by a step or series of steps which include causing volumetric expansion of the blowing agent in accordance with the present invention.
  • the presently used systems and devices for incorporation of blowing agent and for foaming are readily adaptable for use in accordance with the present invention.
  • one advantage of the present invention is the provision of an improved blowing agent which is generally compatible with existing foaming methods and systems.
  • the present invention comprises methods and systems for foaming all types of foams, including thermosetting foams, thermoplastic foams and formed-in-place foams.
  • one aspect of the present invention is the use of the present blowing agents in connection conventional foaming equipment, such as polyurethane foaming equipment, at conventional processing conditions.
  • the present methods therefore include masterbatch type operations, blending type operations, third stream blowing agent addition, and blowing agent addition at the foam head.
  • the preferred methods generally comprise introducing a blowing agent in accordance with the present invention into a thermoplastic material, preferably thermoplastic polymer such as polyolefin, and then subjecting the thermoplastic material to conditions effective to cause foaming.
  • a blowing agent in accordance with the present invention into a thermoplastic material, preferably thermoplastic polymer such as polyolefin
  • the step of introducing the blowing agent into the thermoplastic material may comprise introducing the blowing agent into a screw extruder containing the thermoplastic
  • the step of causing foaming may comprise lowering the pressure on the thermoplastic material and thereby causing expansion of the blowing agent and contributing to the foaming of the material.
  • blowing agent of the present invention does not generally affect the operability of the present invention.
  • the various components of the blowing agent, and even the components of the foamable composition be not be mixed in advance of introduction to the extrusion equipment, or even that the components are not added to the same location in the extrusion equipment.
  • the blowing agent can be introduced either directly or as part of a premix, which is then further added to other parts of the foamable composition.
  • one or more components of the blowing agent at first location in the extruder, which is upstream of the place of addition of one or more other components of the blowing agent, with the expectation that the components will come together in the extruder and/or operate more effectively in this manner.
  • two or more components of the blowing agent are combined in advance and introduced together into the foamable composition, either directly or as part of premix which is then further added to other parts of the foamable composition.
  • One embodiment of the present invention relates to methods of forming foams, and preferably polyurethane and polyisocyanurate foams.
  • the methods generally comprise providing a blowing agent composition of the present inventions, adding (directly or indirectly) the blowing agent composition to a foamable composition, and reacting the foamable composition under the conditions effective to form a foam or cellular structure, as is well known in the art. Any of the methods well known in the art, such as those described in “Polyurethanes Chemistry and Technology,” Volumes I and II, Saunders and Frisch, 1962, John Wiley and Sons, New York, N.Y., which is incorporated herein by reference, may be used or adapted for use in accordance with the foam embodiments of the present invention.
  • such preferred methods comprise preparing polyurethane or polyisocyanurate foams by combining an isocyanate, a polyol or mixture of polyols, a blowing agent or mixture of blowing agents comprising one or more of the present compositions, and other materials such as catalysts, surfactants, and optionally, flame retardants, colorants, or other additives.
  • the foam formulation is pre-blended into two components.
  • the isocyanate and optionally certain surfactants and blowing agents comprise the first component, commonly referred to as the “A” component.
  • the polyol or polyol mixture, surfactant, catalysts, blowing agents, flame retardant, and other isocyanate reactive components comprise the second component, commonly referred to as the “B” component.
  • the present methods and systems also include forming a one component foam, preferably polyurethane foam, containing a blowing agent in accordance with the present invention.
  • a portion of the the blowing agent is contained in the foam forming agent, preferably by being dissolved in a foam forming agent which is liquid at the pressure within the container, a second portion of the blowing agent is present as a separate gas phase.
  • the contained/dissolved blowing agent performs, in large part, to cause the expansion of the foam, and the separate gas phase operates to impart propulsive force to the foam forming agent.
  • Such one component systems are typically and preferably packaged in a container, such as an aerosol type can, and the blowing agent of the present invention thus preferably provides for expansion of the foam and/or the energy to transport the foam/foamable material from the package, and preferably both.
  • such systems and methods comprise charging the package with a fully formulated system (preferably isocyanate/polyol system) and incorporating a gaseous blowing agent in accordance with the present invention into the package, preferably an aerosol type can.
  • the invention also relates to all foams, (incuding but not limited to closed cell foam, open cell foam, rigid foam, flexible foam, integeral skin and the like) prepared from a polymer foam formulation containing a blowing agent comprising the compositions of the invention.
  • foams and particularly thermoset foams such as polyurethane foams, in accordance with the present invention is the ability to achieve, preferably in connection with thermoset foam embodiments, exceptional thermal performance, such as can be measured by the K-factor or lambda, particularly and preferably under low temperature conditions.
  • thermoset foams of the present invention may be used in a wide variety of applications, in certain preferred embodiments the present invention comprises appliance foams in accordance with the present invention, including refrigerator foams, freezer foams, refrigerator/freezer foams, panel foams, and other cold or cryogenic manufacturing applications.
  • the foams in accordance with the present invention provide one or more exceptional features, characteristics and/or properties, including: thermal insulation efficiency (particularly for thermoset foams), dimensional stability, compressive strength, aging of thermal insulation properties, all in addition to the low ozone depletion potential and low global warming potential associated with many of the preferred blowing agents of the present invention.
  • the present invention provides thermoset foam, including such foam formed into foam articles, which exhibit improved thermal conductivity relative to foams made using the same blowing agent (or a commonly used blowing agent HFC-245fa) in the same amount but without the compound of Formula I in accordance with the present invention.
  • the thermoset foams, and preferably polyurethane foams, of the present invention exhibit a K-factor (BTU in/hr ft 2 ° F.) at 40° F. of not greater than about 0.14, more preferably not greater than 0.135, and even more preferably not greater than 0.13. Furthermore, in certain embodiments, it is preferred that the thermoset foams, and preferably the polyurethane foams of the present invention exhibit a K-factor (BTU in/hr ft 2 ° F.) at 75° F. of not greater than about 0.16, more preferably not greater than 0.15, and even more preferably not greater than 0.145.
  • the present foams exhibit improved mechanical properties relative to foams produced with blowing agents outside the scope of the present invention.
  • certain preferred embodiments of the present invention provide foams and foam articles having a compressive strength which is superior to, and preferably at least about 10 relative percent, and even more preferably at least about 15 relative percent greater than a foam produced under substantially identical conditions by utilizing a blowing agent consisting of cyclopentane.
  • the foams produced in accordance with the present invention have compressive strengths that are on a commercial basis comparable to the compressive strength produced by making a foam under substantially the same conditions except wherein the blowing agent consists of HFC-245fa.
  • the foams of the present invention exhibit a compressive strength of at least about 12.5% yield (in the parallel and perpendicular directions), and even more preferably at least about 13% yield in each of said directions.
  • This example illustrates the use of blowing agent in accordance with two preferred embodiments of the present invention, namely the use of HFO-1234ze and HFO-1234yf, and the production of polystyrene foam.
  • a testing apparatus and protocol has been established as an aid to determining whether a specific blowing agent and polymer are capable of producing a foam and the quality of the foam.
  • Ground polymer (Dow Polystyrene 685D) and blowing agent consisting essentially of HFO-1234ze are combined in a vessel.
  • the vessel volume is 200 cm 3 and it is made from two pipe flanges and a section of 2-inch diameter schedule 40 stainless steel pipe 4 inches long.
  • the vessel is placed in an oven, with temperature set at from about 190° F. to about 285° F., preferably for polystyrene at 265° F., and remains there until temperature equilibrium is reached.
  • the pressure in the vessel is then released, quickly producing a foamed polymer.
  • the blowing agent plasticizes the polymer as it dissolves into it.
  • the resulting density of the two foams thus produced using this method are given in Table 1 as the density of the foams produced using trans-HFO-1234ze and HFO-1234yf.
  • the data show that foam polystyrene is obtainable in accordance with the present invention. In this regard it is noted that the bulk density of polystyrene is 1050 kg/m 3 or 65.625 lb/ft 3 at about room temperature.
  • This example demonstrates the performance of HFO-1234ze alone as a blowing agent for polystyrene foam formed in a twin screw type extruder.
  • the apparatus employed in this example is a Leistritz twin screw extruder having the following characteristics:
  • the extruder is divided into 10 sections, each representing a L:D of 4:1.
  • the polystyrene resin was introduced into the first section, the blowing agent was introduced into the sixth section, with the extrudate exiting the tenth section.
  • the extruder operated primarily as a melt/mixing extruder.
  • a subsequent cooling extruder is connected in tandem, for which the design characteristics were:
  • Polystyrene resin namely Nova Chemical—general extrusion grade polystyrene, identified as Nova 1600, is feed to the extruder under the conditions indicated above.
  • the resin has a recommended melt temperature of 375° F.—525° F.
  • the pressure of the extruder at the die is about 1320 pounds per square inch (psi), and the temperature at the die is about 115° C.
  • a blowing agent consisting essentially of transHFO-1234ze is added to the extruder at the location indicated above, with about 0.5% by weight of talc being included, on the basis of the total blowing agent, as a nucleating agent.
  • Foam is produced using the blowing agent at concentrations of 10% by weight, 12% by weight, and 14% by weight, in accordance with the present invention.
  • the density of the foam produced is in the range of about 0.1 grams per cubic centimeter to 0.07 grams per cubic centimeter, with a cell size of about 49 to about 68 microns.
  • the foams, of approximately 30 millimeters diameter are visually of very good quality, very fine cell size, with no visible or apparent blow holes or voids.
  • Example 1B This procedure of Example 1B is repeated except that the foaming agent comprises about 50% by weight transHFO-1234ze and 50% by weight of HFC-245fa and nucleating agent in the concentration indicated in Example 1B.
  • Foamed polystyrene is prepared at blowing agent concentrations of approximately 10% and 12%.
  • the density of the foam produced is about 0.09 grams per cubic centimeter, with a cell size of about 200 microns.
  • the foams, of approximately 30 millimeters diameter, are visually of very good quality, fine cell structure, with no visible or apparent voids.
  • Example 1B This procedure of Example 1B is repeated except that the foaming agent comprises about 80% by weight HFO-1234ze and 20% by weight of HFC-245fa and nucleating agent in the concentration indicated in Example 1B.
  • Foamed polystyrene is prepared at blowing agent concentrations of approximately 10% and 12%.
  • the density of the foam produced is about 0.08 grams per cubic centimeter, with a cell size of about 120 microns.
  • the foams, of approximately 30 millimeters diameter, are visually of very good quality, fine cell structure, with no visible or apparent voids.
  • Example 1B This procedure of Example 1B is repeated except that the foaming agent comprises about 80% by weight HFO-124ze and 20% by weight of HFC-245fa and nucleating agent in the concentration indicated in Example 1B.
  • Foamed polystyrene is prepared at blowing agent concentrations of approximately 10% and 12%.
  • the foams' density was in the range of 0.1 grams per cubic centimeter, and .
  • the foams, of approximately 30 millimeters diameter, are visually of very good quality, fine cell structure, with no visible or apparent voids.
  • Example 1E This procedure of Example 1E is repeated except that the nucleating agent is omitted.
  • the foams' density was in the range of 0.1 grams per cubic centimeter, and the cell size diameter is about 400.
  • the foams of approximately 30 millimeters diameter, are visually of very good quality, fine cell structure, with no visible or apparent voids.
  • This example demonstrates the performance of HFO-1234ze, and isomers thereof, used in combination with hydrocarbon co-blowing agents, and in particular the utility of compositions comprising HFO-1234ze and cyclopentane co-blowing agents in compressive strength performance of polyurethane foams.
  • a commercially available, refrigeration appliance-type polyurethane foam formulation (foam forming agent) is provided.
  • the polyol blend consisted of commercial polyol(s), catalyst(s), and surfactant(s). This formulation is adapted for use in connection with a gaseous blowing agent. Standard commercial polyurethane processing equipment is used for the foam forming process.
  • a gaseous blowing agent combination was formed comprising HFO-1234ze (including isomers thereof) in a concentration of approximately 60 mole percent, and cyclopentane in a concentration of approximately 40 mole percent of the total blowing agent.
  • HFO-1234ze including isomers thereof
  • cyclopentane in a concentration of approximately 40 mole percent of the total blowing agent.
  • Table 2 reports the compressive strength of similar machine-made polyurethane foams using a blowing agent of the present invention in comparison to foams made using a blowing agent consisting of HFC-245fa and a blowing agent consisting of cyclopentane.
  • a polyurethane foam is prepared and is adapted for use as a commercial “appliance type” polyurethane formulation.
  • the same foam formulation described in Example 2 is used in connection with the same standard commercial polyurethane processing equipment is used in the foam forming process.
  • Several systems are prepared, with each system using identical components, systems, and equipment, with the exception of the blowing agent.
  • HFC-134a, HFC-245fa, and cyclopentane are each also tested as the blowing agent.
  • the blowing agent is added in substantially the same molar concentration into the polyol blend.
  • the polyol blend consists of commercial polyol(s), catalyst(s), and surfactant(s).
  • the foams are prepared in accordance with standard commercial manufacturing operations, for example a commercial operation for making foam for refrigeration applications.
  • the prepared foams were evaluated for k-factor, and this information is reported below in Table 3.
  • foams were prepared with HFC-134a, for which commercial data can be referenced.
  • the k-factor data for these foams are shown in Table 3.
  • HFO-1234ze This example demonstrates the k-factor performance of HFO-1234ze, and isomers thereof, when HFO-1234ze blowing agent is substituted into the polyurethane formulation.
  • HFO-1234ze was substituted in an equal molar concentration to that of the benchmark foams.
  • Table 3 data illustrates that HFO-1234ze foams k-factors are considerably better than HFC-134a or cyclopentane foams.
  • blowing agents comprising HFO-1234ze (including isomers thereof) in combination with various HFC co-blowing agents used in connection with the preparation of polyurethane foams.
  • a blowing agent is prepared comprising HFO-1234ze (including isomers thereof) in a concentration of approximately 80 weight percent of the total blowing agent, and HFC-245fa in a concentration of approximately 20 weight percent of the total blowing agent.
  • HFC-134a and cyclopentane were each also tested as the blowing agent.
  • blowing agent was added in substantially the same molar concentration into the polyol blend. Foams are then formed using this blowing agent and the k-factors of the foam are measured. Table 4 below illustrates the k-factor performance of combinations of HFO-1234ze (including isomers thereof) when used in combination with HFC co-blowing agents.
  • Example 5 A further experiment was performed using the same polyol formulation and isocyanate as in Example 5.
  • the foam is prepared by hand mix,
  • the blowing agents consist of a compound in accordance with Formula II, namely, HFCO-1233zd (CF3CH ⁇ CHCI)*in about the same mole percentage of the foamable composition as the blowing agent in Example 5.
  • K-factors are found to be as indicated in Table 6 below.

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US12/276,137 2002-10-25 2008-11-21 Foaming agents and compositions containing fluorine sustituted olefins and methods of foaming Abandoned US20090253820A1 (en)

Priority Applications (34)

Application Number Priority Date Filing Date Title
US12/276,137 US20090253820A1 (en) 2006-03-21 2008-11-21 Foaming agents and compositions containing fluorine sustituted olefins and methods of foaming
CN201510437927.6A CN105111492A (zh) 2007-11-25 2008-11-24 含有氟取代的烯烃的发泡剂和组合物以及发泡的方法
MX2010005669A MX2010005669A (es) 2007-11-25 2008-11-24 Agentes espumantes y composiciones que contienen olefinas sustituidas con fluor y metodos para la formacion de la espuma.
CN2008801257097A CN101925644A (zh) 2007-11-25 2008-11-24 含有氟取代的烯烃的发泡剂和组合物以及发泡的方法
KR1020147023257A KR20140119134A (ko) 2007-11-25 2008-11-24 플루오로 치환된 올레핀을 포함하는 발포제 및 조성물 및 발포 방법
CA2706774A CA2706774C (en) 2007-11-25 2008-11-24 Foaming agents and compositions containing fluorine substituted olefins and methods of foaming
EP08851933A EP2215152A4 (en) 2007-11-25 2008-11-24 FOAM COMPOSITES AND COMPOSITIONS WITH FLUORINATED OLEFINES AND FOAM PROCESSING
KR1020177021108A KR20170091757A (ko) 2007-11-25 2008-11-24 플루오로 치환된 올레핀을 포함하는 발포제 및 조성물 및 발포 방법
CN201510436991.2A CN105111491A (zh) 2007-11-25 2008-11-24 含有氟取代的烯烃的发泡剂和组合物以及发泡的方法
CA2997980A CA2997980A1 (en) 2007-11-25 2008-11-24 Foaming agents and compositions containing fluorine substituted olefins and methods of foaming
JP2010535113A JP2011504538A (ja) 2007-11-25 2008-11-24 フッ素置換オレフィンを含有する発泡剤及び組成物ならびに発泡方法
KR1020167023520A KR20160104745A (ko) 2007-11-25 2008-11-24 플루오로 치환된 올레핀을 포함하는 발포제 및 조성물 및 발포 방법
KR20157005312A KR20150038512A (ko) 2007-11-25 2008-11-24 플루오로 치환된 올레핀을 포함하는 발포제 및 조성물 및 발포 방법
KR1020197000987A KR20190007105A (ko) 2007-11-25 2008-11-24 플루오로 치환된 올레핀을 포함하는 발포제 및 조성물 및 발포 방법
PCT/US2008/084512 WO2009067720A2 (en) 2007-11-25 2008-11-24 Foaming agents and compositions containing fluorine substituted olefins and methods of foaming
KR1020107014118A KR20100112562A (ko) 2007-11-25 2008-11-24 플루오로 치환된 올레핀을 포함하는 발포제 및 조성물 및 발포 방법
TW97145587A TW200932807A (en) 2007-11-25 2008-11-25 Foaming agents and compositions containing fluorine substituted olefins and methods of foaming
TW104134781A TWI612085B (zh) 2007-11-25 2008-11-25 熱固性發泡體、包含其之澆注面板、提供該發泡體之方法及可發泡組合物
US12/351,807 US9499729B2 (en) 2006-06-26 2009-01-09 Compositions and methods containing fluorine substituted olefins
US13/394,289 US8962707B2 (en) 2003-10-27 2010-09-08 Monochlorotrifluoropropene compounds and compositions and methods using same
US12/890,143 US20110037016A1 (en) 2003-10-27 2010-09-24 Fluoropropene compounds and compositions and methods using same
US13/191,070 US9000061B2 (en) 2006-03-21 2011-07-26 Foams and articles made from foams containing 1-chloro-3,3,3-trifluoropropene (HFCO-1233zd)
US13/191,141 US9181410B2 (en) 2002-10-25 2011-07-26 Systems for efficient heating and/or cooling and having low climate change impact
US13/298,452 US9175200B2 (en) 2008-10-28 2011-11-17 Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US13/585,755 US8729145B2 (en) 2006-03-21 2012-08-14 Foaming agents and compositions containing fluorine substituted olefins and methods of foaming
US14/282,909 US20140336292A1 (en) 2006-03-21 2014-05-20 Foaming Agents And Compositions Containing Fluorine Substituted Olefins And Methods Of Foaming
JP2014191142A JP2015017268A (ja) 2007-11-25 2014-09-19 フッ素置換オレフィンを含有する発泡剤及び組成物ならびに発泡方法
US14/630,166 US20150231527A1 (en) 2003-10-27 2015-02-24 Monochlorotrifluoropropene compounds and compositions and methods using same
US14/679,802 US9701782B2 (en) 2006-03-21 2015-04-06 Foams and articles made from foams containing 1-chloro-3,3,3-trifluoropropene (HFCO-1233zd)
US14/936,214 US20160186917A1 (en) 2003-10-27 2015-11-09 Systems For Efficient Heating And/Or Cooling And Having Low Climate Change Impact
US15/200,268 US20160310922A1 (en) 2003-10-27 2016-07-01 Fluoropropene compounds and compositions and methods using same
JP2016132325A JP6307116B2 (ja) 2007-11-25 2016-07-04 フッ素置換オレフィンを含有する発泡剤及び組成物ならびに発泡方法
US15/439,840 US20170158834A1 (en) 2006-06-26 2017-02-22 Foams and articles made from foams containing hcfo or hfo blowing agents
JP2018040959A JP2018127628A (ja) 2007-11-25 2018-03-07 フッ素置換オレフィンを含有する発泡剤及び組成物ならびに発泡方法

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US78473106P 2006-03-21 2006-03-21
US11/474,887 US9796848B2 (en) 2002-10-25 2006-06-26 Foaming agents and compositions containing fluorine substituted olefins and methods of foaming
PCT/US2007/064570 WO2007109748A2 (en) 2006-03-21 2007-03-21 Foaming agents containing fluorine substituted unsaturated olefins
US98997707P 2007-11-25 2007-11-25
US12/276,137 US20090253820A1 (en) 2006-03-21 2008-11-21 Foaming agents and compositions containing fluorine sustituted olefins and methods of foaming

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US11/474,887 Continuation-In-Part US9796848B2 (en) 2002-10-25 2006-06-26 Foaming agents and compositions containing fluorine substituted olefins and methods of foaming
US11/475,605 Continuation-In-Part US9005467B2 (en) 2002-10-25 2006-06-26 Methods of replacing heat transfer fluids
PCT/US2007/064570 Continuation WO2007109748A2 (en) 2002-10-25 2007-03-21 Foaming agents containing fluorine substituted unsaturated olefins
US12/426,948 Continuation-In-Part US8033120B2 (en) 2002-10-25 2009-04-20 Compositions and methods containing fluorine substituted olefins

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US11/475,605 Continuation-In-Part US9005467B2 (en) 2002-10-25 2006-06-26 Methods of replacing heat transfer fluids
US12/259,694 Continuation-In-Part US7935268B2 (en) 2008-10-28 2008-10-28 Azeotrope-like compositions comprising trans-1-chloro-3,3,3-trifluoropropene
US12/351,807 Continuation US9499729B2 (en) 2003-10-27 2009-01-09 Compositions and methods containing fluorine substituted olefins
US13/191,141 Continuation-In-Part US9181410B2 (en) 2002-10-25 2011-07-26 Systems for efficient heating and/or cooling and having low climate change impact
US13/191,070 Continuation-In-Part US9000061B2 (en) 2006-03-21 2011-07-26 Foams and articles made from foams containing 1-chloro-3,3,3-trifluoropropene (HFCO-1233zd)
US13/298,452 Continuation-In-Part US9175200B2 (en) 2008-10-28 2011-11-17 Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US13/585,755 Continuation US8729145B2 (en) 2006-03-21 2012-08-14 Foaming agents and compositions containing fluorine substituted olefins and methods of foaming

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Cited By (56)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090305876A1 (en) * 2006-06-26 2009-12-10 Honeywell International, Inc. Compositions and Methods Containing Fluorine Substituted Olefins
US20100102272A1 (en) * 2008-10-28 2010-04-29 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US20100102273A1 (en) * 2008-10-28 2010-04-29 Honeywell International Inc. Azeotrope-like compositions comprising trans-1-chloro-3,3,3-trifluoropropene
US20100154444A1 (en) * 2005-06-24 2010-06-24 Honeywell International Inc. Trans-Chloro-3,3,3-Trifluoropropene For Use In Chiller Applications
US20100216904A1 (en) * 2009-02-24 2010-08-26 E. I. Du Pont De Nemours And Company Foam-forming compositions containing mixtures of 2-chloro-3,3,3-trifluoropropene and at least one hydrofluoroolefin and their uses in the preparation of polyisocyanate-based foams
US20110023507A1 (en) * 2009-07-29 2011-02-03 Honeywell International Inc. Compositions and methods for refrigeration
US20110084228A1 (en) * 2008-06-11 2011-04-14 Arkema France Hydrofluoroolefin compositions
US20110095224A1 (en) * 2008-06-11 2011-04-28 Wissam Rached Hydrofluoroolefin compositions
US20110162410A1 (en) * 2007-10-12 2011-07-07 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
US20110195890A1 (en) * 2008-10-15 2011-08-11 Laurent Abbas Cleaning compositions
GB2477835A (en) * 2010-02-16 2011-08-17 Ineos Fluor Holdings Ltd Heat transfer compositions
CN102250586A (zh) * 2010-05-20 2011-11-23 墨西哥化学阿玛科股份有限公司 传热组合物
US20110309288A1 (en) * 2009-01-22 2011-12-22 Arkema Inc. Azeotrope and azeotrope-like compositions of e-1-chloro-3,3,3-trifluoropropene and isopropanol
WO2011144906A3 (en) * 2010-05-20 2012-03-01 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
US20120119136A1 (en) * 2010-11-12 2012-05-17 Honeywell International Inc. Low gwp heat transfer compositions
US20120128964A1 (en) * 2010-11-19 2012-05-24 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US20120240477A1 (en) * 2009-12-22 2012-09-27 Ei Du Pont De Nemours And Company Compositions comprising 2,3,3,3-tetrafluoropropene, 1,1,2,3-tetra-chloropropene, 2-chloro-3,3,3-trifluoropropene, or 2-chloro-1,1,1,2-tetrafluoropropane
US8333901B2 (en) 2007-10-12 2012-12-18 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
US20120329893A1 (en) * 2010-03-09 2012-12-27 Arkema France Hydrochlorofluoroolefin blowing agent compositions
US20130149452A1 (en) * 2011-12-09 2013-06-13 Honeywell International, Inc. Foams and articles made from foams containing 1-chloro-3,3,3-trifluoropropene (1233zd)
US20130197115A1 (en) * 2011-08-01 2013-08-01 Basf Se Hfo/water-blown rigid foam systems
US8512591B2 (en) 2007-10-12 2013-08-20 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
US8522606B2 (en) 2010-12-22 2013-09-03 Nuovo Pignone S.P.A. Similitude testing of compressor performance
US8580137B2 (en) * 2009-01-22 2013-11-12 Arkema Inc. Trans-1,2-dichloroethylene with flash point elevated by 1-chloro-3,3,3-trifluoropropene
US8703006B2 (en) 2008-10-28 2014-04-22 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US8808569B2 (en) 2009-09-11 2014-08-19 Arkema France Use of ternary compositions
WO2014164587A1 (en) * 2013-03-13 2014-10-09 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US8912369B2 (en) 2012-06-29 2014-12-16 Central Glass Company, Limited Method for production of 1-chloro-3,3,3-trifluoropropene
US20140378559A1 (en) * 2011-12-19 2014-12-25 Honeywell International Inc. Compositions of 1,1,1,3,3-pentafluoropropane and cyclopentane
US8962707B2 (en) 2003-10-27 2015-02-24 Honeywell International Inc. Monochlorotrifluoropropene compounds and compositions and methods using same
US9000061B2 (en) 2006-03-21 2015-04-07 Honeywell International Inc. Foams and articles made from foams containing 1-chloro-3,3,3-trifluoropropene (HFCO-1233zd)
US9011711B2 (en) 2009-09-11 2015-04-21 Arkema France Heat transfer fluid replacing R-410A
AU2013204022B2 (en) * 2010-05-20 2015-05-14 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
AU2014203085B2 (en) * 2010-05-20 2015-08-20 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
US9150768B2 (en) 2008-10-28 2015-10-06 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US9175203B2 (en) 2009-09-11 2015-11-03 Arkema France Ternary compositions for low-capacity refrigeration
US9175202B2 (en) 2010-02-16 2015-11-03 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
US9174897B2 (en) 2012-06-28 2015-11-03 Central Glass Company, Limited Method for purifying trans-1,3,3,3-tetrafluoropropene
US9267064B2 (en) 2009-09-11 2016-02-23 Arkema France Ternary compositions for high-capacity refrigeration
US9353302B2 (en) 2010-08-13 2016-05-31 Carrier Corporation Fluorinated hydrocarbon composition
US20160169575A1 (en) * 2014-12-12 2016-06-16 Honeywell International Inc. Abs liners and cooling cabinets containing same
US9683157B2 (en) 2009-09-11 2017-06-20 Arkema France Heat transfer method
US9816057B2 (en) 2014-10-24 2017-11-14 Edo Shellef Nonflammable composition containing 1,2-dichloroethylene
US9926244B2 (en) 2008-10-28 2018-03-27 Honeywell International Inc. Process for drying HCFO-1233zd
US10035938B2 (en) 2009-09-11 2018-07-31 Arkema France Heat transfer fluid replacing R-134a
US10077221B2 (en) 2013-03-20 2018-09-18 Arkema France Composition comprising HF and E-3,3,3-trifluoro-1-chloropropene
US10266736B2 (en) 2010-06-25 2019-04-23 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
US10330364B2 (en) 2014-06-26 2019-06-25 Hudson Technologies, Inc. System and method for retrofitting a refrigeration system from HCFC to HFC refrigerant
US10335623B2 (en) 2011-05-19 2019-07-02 Arkema Inc. Non-flammable compositions of chloro-trifluoropropene
US10669465B2 (en) 2016-09-19 2020-06-02 Arkema France Composition comprising 1-chloro-3,3,3-trifluoropropene
US10858561B2 (en) 2008-10-16 2020-12-08 Arkema France Heat transfer method
US11104833B2 (en) * 2016-12-26 2021-08-31 Zhejiang Quhua Fluor-Chemistry Co Ltd Hydrofluoroolefins-containing refrigerant composition
US11130893B2 (en) 2008-10-08 2021-09-28 Arkema France Heat transfer fluid
US20220163162A1 (en) * 2019-04-02 2022-05-26 Basf Se Insulated pipe containing polyurethane foam which is foamed by an environmentally friendly foaming agent and has a low degree of brittleness
WO2022213067A1 (en) * 2021-03-30 2022-10-06 Honeywell International Inc. Blowing agents comprising z-1-chloro-2,3,3,3-tetrafluoropentene (hcfo-1224yd(z))
US11753516B2 (en) 2021-10-08 2023-09-12 Covestro Llc HFO-containing compositions and methods of producing foams

Families Citing this family (35)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090253820A1 (en) * 2006-03-21 2009-10-08 Honeywell International Inc. Foaming agents and compositions containing fluorine sustituted olefins and methods of foaming
US20110037016A1 (en) * 2003-10-27 2011-02-17 Honeywell International Inc. Fluoropropene compounds and compositions and methods using same
JP5416087B2 (ja) 2007-03-29 2014-02-12 アーケマ・インコーポレイテッド ヒドロフルオロプロペンおよびヒドロクロロフルオロオレフィンの発泡剤組成物
EP3473691A1 (en) 2008-07-30 2019-04-24 Honeywell International Inc. Compositions containing difluoromethane and fluorine substituted olefins
CN102177118A (zh) 2008-10-10 2011-09-07 纳幕尔杜邦公司 包含2,3,3,3-四氟丙烯、2-氯-2,3,3,3-四氟丙醇、乙酸2-氯-2,3,3,3-四氟丙酯或(2-氯-2,3,3,3-四氟丙氧基)氯化锌的组合物
DE102009028061A1 (de) 2009-07-29 2011-02-10 Evonik Goldschmidt Gmbh Verfahren zur Herstellung von Polyurethanschaum
CN102574756B (zh) * 2009-08-17 2014-09-17 阿科玛股份有限公司 1-氯-3,3,3-三氟丙烯和HFC-245eb的共沸混合物以及类共沸混合物的组合物
CA2778518C (en) * 2009-10-23 2017-11-28 Arkema Inc. Tetrafluorobutene blowing agent compositions for polyurethane foams
FR2955590B1 (fr) * 2010-01-22 2012-03-23 Arkema France Compositions de nettoyage a base d'hydrochlorofluoroolefine
GB201002619D0 (en) * 2010-02-16 2010-03-31 Ineos Fluor Holdings Ltd Heat transfer compositions
CN107090090B (zh) * 2010-04-28 2022-05-17 阿科玛股份有限公司 改善含有卤化烯烃发泡剂的聚氨酯多元醇共混物的稳定性的方法
US8747691B2 (en) * 2010-05-06 2014-06-10 Honeywell International Inc. Azeotrope-like compositions of tetrafluoropropene and water
US20120046372A1 (en) * 2010-08-18 2012-02-23 Honeywell International Inc. Blowing agents, foamable compositions and foams
MX354274B (es) 2011-08-01 2018-02-21 Basf Se Sistemas de espuma rígida soplados con hidrofluoroolefina/agua.
JP5937386B2 (ja) * 2012-03-16 2016-06-22 株式会社ジェイエスピー ポリスチレン系樹脂押出発泡断熱板の製造方法
CN104540888A (zh) 2012-08-15 2015-04-22 纳幕尔杜邦公司 2,3,3,4,4,4-六氟-1-丁烯和1,1,1,2,3,3-六氟丙烷的共沸和类共沸组合物及其用途
KR20180039771A (ko) 2014-01-24 2018-04-18 아사히 가세이 겐자이 가부시키가이샤 페놀 수지 발포체 및 그 제조 방법
KR101991603B1 (ko) * 2015-03-24 2019-06-20 아사히 가세이 겐자이 가부시키가이샤 페놀 수지 발포체 및 그 제조 방법
WO2016152988A1 (ja) * 2015-03-24 2016-09-29 積水化学工業株式会社 フェノール樹脂発泡体及びフェノール樹脂発泡体の製造方法
US20180044494A1 (en) 2015-03-24 2018-02-15 Asahi Kasei Construction Materials Corporation Phenolic resin foam and method of producing same
FR3037964B1 (fr) * 2015-06-24 2019-12-20 Saint-Gobain Isover Mousses polyester thermodurcies et procede de fabrication
CN105017553A (zh) * 2015-07-14 2015-11-04 关志强 一种保温聚氨酯塑料的发泡剂
JP6512580B2 (ja) * 2015-10-30 2019-05-15 株式会社ジェイエスピー ポリスチレン系樹脂発泡板の製造方法
JP6541555B2 (ja) * 2015-11-25 2019-07-10 株式会社ジェイエスピー ポリスチレン系樹脂発泡板の製造方法
JP6921106B2 (ja) * 2016-03-24 2021-08-18 ザ ケマーズ カンパニー エフシー リミテッド ライアビリティ カンパニー Z−1233zdの共沸及び共沸様組成物
JP6250094B2 (ja) * 2016-05-12 2017-12-20 株式会社ジェイエスピー ポリスチレン系樹脂押出発泡断熱板の製造方法
CN106750488B (zh) * 2016-12-26 2019-05-17 浙江衢化氟化学有限公司 一种低碳环保型发泡剂组合物
JP6485493B2 (ja) * 2017-06-16 2019-03-20 ダイキン工業株式会社 ペンタフルオロプロパンと水とを含む共沸又は共沸様組成物、並びにペンタフルオロプロパンの製造方法
CN108384515A (zh) * 2018-02-27 2018-08-10 湖北绿冷高科节能技术有限公司 一种替代r22的制冷剂
WO2019232038A1 (en) * 2018-05-29 2019-12-05 Owens Corning Intellectual Capital, Llc Blowing agent compositions for insulating foams
WO2020132309A1 (en) * 2018-12-21 2020-06-25 Honeywell International Inc. Solvent compositions containing 1,2,2-trifluoro-1-trifluoromethylcyclobutane (tfmcb)
EP3935122B1 (en) * 2019-03-04 2024-05-08 The Chemours Company FC, LLC Heat transfer compositions comprising r-1225ye(e)
CN110105520B (zh) * 2019-05-05 2021-09-21 深圳市盈石科技有限公司 一种保温硬质聚氨酯泡沫及其制备方法
WO2023204283A1 (ja) * 2022-04-22 2023-10-26 旭化成建材株式会社 フェノール樹脂発泡体およびその積層板
CN114940738B (zh) * 2022-06-02 2024-02-27 万华化学(宁波)容威聚氨酯有限公司 一种聚氨酯组合物、聚氨酯泡沫及其制备方法与应用

Citations (46)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2834748A (en) * 1954-03-22 1958-05-13 Union Carbide Corp Siloxane-oxyalkylene block copolymers
US2846458A (en) * 1956-05-23 1958-08-05 Dow Corning Organosiloxane ethers
US2889379A (en) * 1957-02-06 1959-06-02 Dow Chemical Co Preparation of 3, 3, 3-trifluoropropene
US2917480A (en) * 1954-06-10 1959-12-15 Union Carbide Corp Siloxane oxyalkylene block copolymers
US2931840A (en) * 1958-11-25 1960-04-05 Du Pont Process for preparing 2, 3, 3, 3-tetrafluoropropene
US2996555A (en) * 1959-06-25 1961-08-15 Dow Chemical Co Preparation of 2, 3, 3, 3-tetrafluoropropene
US3085918A (en) * 1959-05-22 1963-04-16 Ici Ltd Cleaning process
US3723318A (en) * 1971-11-26 1973-03-27 Dow Corning Propellants and refrigerants based on trifluoropropene
US3884828A (en) * 1970-10-15 1975-05-20 Dow Corning Propellants and refrigerants based on trifluoropropene
US4465786A (en) * 1982-09-27 1984-08-14 General Electric Company Catalyst composition for the preparation of 3,3,3-trifluoropropene
US4788352A (en) * 1986-07-21 1988-11-29 Shell Oil Company Trifluoroalkenes and a method for their preparation
US4798818A (en) * 1987-11-27 1989-01-17 Dow Corning Corporation Catalyst composition and process for its preparation
US4945119A (en) * 1989-05-10 1990-07-31 The Dow Chemical Company Foaming system for rigid urethane and isocyanurate foams
US4944890A (en) * 1989-05-23 1990-07-31 E. I. Du Pont De Nemours And Company Compositions and process of using in refrigeration
US5137932A (en) * 1989-12-07 1992-08-11 Hoechst Aktiengesellschaft Process for producing foams
US5250208A (en) * 1992-04-02 1993-10-05 E. I. Du Pont De Nemours And Company Ternary azeotropic compositions
US5532419A (en) * 1994-05-16 1996-07-02 Alliedsignal Inc. Processes for the preparation of fluorinated olefins and hydrofluorocarbons using fluorinated olefin
US5574192A (en) * 1994-07-11 1996-11-12 Alliedsignal Inc. Process for the manufacture of 1,1,1,3,3-pentafluoropropane
US5578137A (en) * 1993-08-31 1996-11-26 E. I. Du Pont De Nemours And Company Azeotropic or azeotrope-like compositions including 1,1,1,2,3,4,4,5,5,5-decafluoropentane
US5616275A (en) * 1993-03-29 1997-04-01 E. I. Du Pont De Nemours And Company Azeotrope(like) mixtures of two hexafluoropropane stereoisomers
US5674451A (en) * 1993-03-05 1997-10-07 Ikon Corporation Methods and compositions for sterilization of articles
US5679875A (en) * 1992-06-05 1997-10-21 Daikin Industries, Ltd. Method for manufacturing 1,1,1,2,3-pentafluoropropene 1,1,1,2,3-pentafluoropropane
US5714083A (en) * 1995-01-30 1998-02-03 Turner; Donald E. A non-flammable refrigerant fluid containing hexa fluoropropane and hydrocarbons
US5736063A (en) * 1991-03-18 1998-04-07 Alliedsignal Inc. Non-azeotropic refrigerant compositions containing carbon dioxide
US5744052A (en) * 1994-07-14 1998-04-28 E. I. Du Pont De Nemours And Company Azeotrope-like compositions containing difluoromethane, pentafluoroethane, and carbon dioxide
US5788886A (en) * 1997-05-05 1998-08-04 E. I. Du Pont De Nemours And Company Pentafluoropropane compositions
US5900185A (en) * 1996-09-27 1999-05-04 University Of New Mexico Tropodegradable bromine-containing halocarbon additives to decrease flammability of refrigerants, foam blowing agents, solvents, aerosol propellants, and sterilants
US6041621A (en) * 1998-12-30 2000-03-28 Praxair Technology, Inc. Single circuit cryogenic liquefaction of industrial gas
US6111150A (en) * 1996-06-20 2000-08-29 Central Glass Company, Limited Method for producing 1,1,1,3,3,-pentafluoropropane
US6124510A (en) * 1998-07-21 2000-09-26 Elf Atochem North America, Inc. 1234ze preparation
US6258292B1 (en) * 1996-08-08 2001-07-10 Donald E. Turner Alternative refrigerant including hexafluoropropylene
US6274779B1 (en) * 1998-03-03 2001-08-14 Daniel Christopher Merkel Purified 1,1,1,3,3,3-hexafluoropropane and method for making same
US6300378B1 (en) * 1996-09-27 2001-10-09 University Of New Mexico Tropodegradable bromine-containing halocarbon additives to decrease flammability of refrigerants foam blowing agents solvents aerosol propellants and sterilants
US6327866B1 (en) * 1998-12-30 2001-12-11 Praxair Technology, Inc. Food freezing method using a multicomponent refrigerant
US6516837B2 (en) * 2000-09-27 2003-02-11 Honeywell International Inc. Method of introducing refrigerants into refrigeration systems
US20030127115A1 (en) * 1999-10-29 2003-07-10 Thomas Raymond Hilton Percival Cleaning processes using hydrofluorocarbon and/or hydrochlorofluorocarbon compounds
US20040256594A1 (en) * 2002-10-25 2004-12-23 Honeywell International, Inc. Compositions containing fluorine substituted olefins
US6858571B2 (en) * 2002-10-25 2005-02-22 Honeywell International Inc. Pentafluoropropene-based compositions
US20050054741A1 (en) * 2002-01-30 2005-03-10 Solvay Fluor Und Derivate Gmbh Mixtures containing 1,1,1,3,3-pentafluorobutane and 1,1,1,2,3,3,3-heptafluoropropane
US20050233934A1 (en) * 2004-04-16 2005-10-20 Honeywell International, Inc. Azeotrope-like compositions of tetrafluoropropene and trifluoroiodomethane
US6972271B2 (en) * 2000-07-17 2005-12-06 Honeywell International Inc. Supported catalyst systems
US20060022166A1 (en) * 2004-04-16 2006-02-02 Honeywell International Inc. Azeotrope-like compositions of tetrafluoropropene and pentafluoropropene
US20060043331A1 (en) * 2004-04-29 2006-03-02 Honeywell International, Inc. Compositions comprising tetrafluoeopropene & carbon dioxide
US20060142173A1 (en) * 2003-11-04 2006-06-29 Honeywell International Inc. Solvent compositions containing chlorofluoroolefins or fluoroolefins
US20060243944A1 (en) * 2005-03-04 2006-11-02 Minor Barbara H Compositions comprising a fluoroolefin
US20070007488A1 (en) * 2003-10-27 2007-01-11 Honeywell International, Inc. Compositions containing fluorine substituted olefins

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0760387B2 (ja) * 1987-11-12 1995-06-28 松下電器産業株式会社 情報処理装置
JPH05179043A (ja) * 1991-11-18 1993-07-20 Daikin Ind Ltd フルオロブテンからなる発泡剤およびプラスチック発泡体の製造方法
US20060234944A1 (en) * 2001-10-23 2006-10-19 Oklahoma Medical Reseach Foundation Beta-secretase inhibitors and methods of use
US9796848B2 (en) * 2002-10-25 2017-10-24 Honeywell International Inc. Foaming agents and compositions containing fluorine substituted olefins and methods of foaming
US20090253820A1 (en) * 2006-03-21 2009-10-08 Honeywell International Inc. Foaming agents and compositions containing fluorine sustituted olefins and methods of foaming
DE10341394A1 (de) * 2003-09-05 2005-04-28 Pierburg Gmbh Stellvorrichtung
US7524805B2 (en) * 2004-04-29 2009-04-28 Honeywell International Inc. Azeotrope-like compositions of tetrafluoropropene and hydrofluorocarbons
EP1740521B1 (en) * 2004-04-29 2015-05-20 Honeywell International Inc. Processes for synthesis of 1,3,3,3-tetrafluoropropene
US20060143944A1 (en) * 2005-01-06 2006-07-06 Collins Matthew K Surfing footwear with leash anchor
TW201815923A (zh) * 2005-06-24 2018-05-01 美商哈尼威爾國際公司 含有經氟取代之烯烴之發泡劑及組合物,及發泡方法
CA2646990C (en) * 2006-03-21 2018-02-20 Honeywell International Inc. Foaming agents containing fluorine substituted unsaturated olefins
FR2899234B1 (fr) * 2006-03-31 2017-02-17 Arkema Composition d'agent d'expansion
JP5416087B2 (ja) * 2007-03-29 2014-02-12 アーケマ・インコーポレイテッド ヒドロフルオロプロペンおよびヒドロクロロフルオロオレフィンの発泡剤組成物
ES2376290T5 (es) * 2007-03-29 2020-03-19 Arkema Inc Uso de composiciones de agente expansionante a base de hidrofluorolefinas e hidroclorofluorolefinas para el espumado de material termoplástico

Patent Citations (47)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2834748A (en) * 1954-03-22 1958-05-13 Union Carbide Corp Siloxane-oxyalkylene block copolymers
US2917480A (en) * 1954-06-10 1959-12-15 Union Carbide Corp Siloxane oxyalkylene block copolymers
US2846458A (en) * 1956-05-23 1958-08-05 Dow Corning Organosiloxane ethers
US2889379A (en) * 1957-02-06 1959-06-02 Dow Chemical Co Preparation of 3, 3, 3-trifluoropropene
US2931840A (en) * 1958-11-25 1960-04-05 Du Pont Process for preparing 2, 3, 3, 3-tetrafluoropropene
US3085918A (en) * 1959-05-22 1963-04-16 Ici Ltd Cleaning process
US2996555A (en) * 1959-06-25 1961-08-15 Dow Chemical Co Preparation of 2, 3, 3, 3-tetrafluoropropene
US3884828A (en) * 1970-10-15 1975-05-20 Dow Corning Propellants and refrigerants based on trifluoropropene
US3723318A (en) * 1971-11-26 1973-03-27 Dow Corning Propellants and refrigerants based on trifluoropropene
US4465786A (en) * 1982-09-27 1984-08-14 General Electric Company Catalyst composition for the preparation of 3,3,3-trifluoropropene
US4788352A (en) * 1986-07-21 1988-11-29 Shell Oil Company Trifluoroalkenes and a method for their preparation
US4798818A (en) * 1987-11-27 1989-01-17 Dow Corning Corporation Catalyst composition and process for its preparation
US4945119A (en) * 1989-05-10 1990-07-31 The Dow Chemical Company Foaming system for rigid urethane and isocyanurate foams
US4944890A (en) * 1989-05-23 1990-07-31 E. I. Du Pont De Nemours And Company Compositions and process of using in refrigeration
US5137932A (en) * 1989-12-07 1992-08-11 Hoechst Aktiengesellschaft Process for producing foams
US5736063A (en) * 1991-03-18 1998-04-07 Alliedsignal Inc. Non-azeotropic refrigerant compositions containing carbon dioxide
US5250208A (en) * 1992-04-02 1993-10-05 E. I. Du Pont De Nemours And Company Ternary azeotropic compositions
US5679875A (en) * 1992-06-05 1997-10-21 Daikin Industries, Ltd. Method for manufacturing 1,1,1,2,3-pentafluoropropene 1,1,1,2,3-pentafluoropropane
US5674451A (en) * 1993-03-05 1997-10-07 Ikon Corporation Methods and compositions for sterilization of articles
US5616275A (en) * 1993-03-29 1997-04-01 E. I. Du Pont De Nemours And Company Azeotrope(like) mixtures of two hexafluoropropane stereoisomers
US5578137A (en) * 1993-08-31 1996-11-26 E. I. Du Pont De Nemours And Company Azeotropic or azeotrope-like compositions including 1,1,1,2,3,4,4,5,5,5-decafluoropentane
US5532419A (en) * 1994-05-16 1996-07-02 Alliedsignal Inc. Processes for the preparation of fluorinated olefins and hydrofluorocarbons using fluorinated olefin
US5574192A (en) * 1994-07-11 1996-11-12 Alliedsignal Inc. Process for the manufacture of 1,1,1,3,3-pentafluoropropane
US5744052A (en) * 1994-07-14 1998-04-28 E. I. Du Pont De Nemours And Company Azeotrope-like compositions containing difluoromethane, pentafluoroethane, and carbon dioxide
US5714083A (en) * 1995-01-30 1998-02-03 Turner; Donald E. A non-flammable refrigerant fluid containing hexa fluoropropane and hydrocarbons
US6111150A (en) * 1996-06-20 2000-08-29 Central Glass Company, Limited Method for producing 1,1,1,3,3,-pentafluoropropane
US6258292B1 (en) * 1996-08-08 2001-07-10 Donald E. Turner Alternative refrigerant including hexafluoropropylene
US5900185A (en) * 1996-09-27 1999-05-04 University Of New Mexico Tropodegradable bromine-containing halocarbon additives to decrease flammability of refrigerants, foam blowing agents, solvents, aerosol propellants, and sterilants
US6300378B1 (en) * 1996-09-27 2001-10-09 University Of New Mexico Tropodegradable bromine-containing halocarbon additives to decrease flammability of refrigerants foam blowing agents solvents aerosol propellants and sterilants
US5788886A (en) * 1997-05-05 1998-08-04 E. I. Du Pont De Nemours And Company Pentafluoropropane compositions
US6274779B1 (en) * 1998-03-03 2001-08-14 Daniel Christopher Merkel Purified 1,1,1,3,3,3-hexafluoropropane and method for making same
US6124510A (en) * 1998-07-21 2000-09-26 Elf Atochem North America, Inc. 1234ze preparation
US6041621A (en) * 1998-12-30 2000-03-28 Praxair Technology, Inc. Single circuit cryogenic liquefaction of industrial gas
US6327866B1 (en) * 1998-12-30 2001-12-11 Praxair Technology, Inc. Food freezing method using a multicomponent refrigerant
US20030127115A1 (en) * 1999-10-29 2003-07-10 Thomas Raymond Hilton Percival Cleaning processes using hydrofluorocarbon and/or hydrochlorofluorocarbon compounds
US6972271B2 (en) * 2000-07-17 2005-12-06 Honeywell International Inc. Supported catalyst systems
US6516837B2 (en) * 2000-09-27 2003-02-11 Honeywell International Inc. Method of introducing refrigerants into refrigeration systems
US20050054741A1 (en) * 2002-01-30 2005-03-10 Solvay Fluor Und Derivate Gmbh Mixtures containing 1,1,1,3,3-pentafluorobutane and 1,1,1,2,3,3,3-heptafluoropropane
US20040256594A1 (en) * 2002-10-25 2004-12-23 Honeywell International, Inc. Compositions containing fluorine substituted olefins
US6858571B2 (en) * 2002-10-25 2005-02-22 Honeywell International Inc. Pentafluoropropene-based compositions
US7279451B2 (en) * 2002-10-25 2007-10-09 Honeywell International Inc. Compositions containing fluorine substituted olefins
US20070007488A1 (en) * 2003-10-27 2007-01-11 Honeywell International, Inc. Compositions containing fluorine substituted olefins
US20060142173A1 (en) * 2003-11-04 2006-06-29 Honeywell International Inc. Solvent compositions containing chlorofluoroolefins or fluoroolefins
US20050233934A1 (en) * 2004-04-16 2005-10-20 Honeywell International, Inc. Azeotrope-like compositions of tetrafluoropropene and trifluoroiodomethane
US20060022166A1 (en) * 2004-04-16 2006-02-02 Honeywell International Inc. Azeotrope-like compositions of tetrafluoropropene and pentafluoropropene
US20060043331A1 (en) * 2004-04-29 2006-03-02 Honeywell International, Inc. Compositions comprising tetrafluoeopropene & carbon dioxide
US20060243944A1 (en) * 2005-03-04 2006-11-02 Minor Barbara H Compositions comprising a fluoroolefin

Cited By (115)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8962707B2 (en) 2003-10-27 2015-02-24 Honeywell International Inc. Monochlorotrifluoropropene compounds and compositions and methods using same
US9347695B2 (en) * 2005-06-24 2016-05-24 Honeywell International Inc. Trans-chloro-3,3,3-trifluoropropene for use in chiller applications
US20100154444A1 (en) * 2005-06-24 2010-06-24 Honeywell International Inc. Trans-Chloro-3,3,3-Trifluoropropene For Use In Chiller Applications
US20140069129A1 (en) * 2005-06-24 2014-03-13 Honeywell International Inc. Trans-chloro-3,3,3-trifluoropropene for use in chiller applications
US8574451B2 (en) 2005-06-24 2013-11-05 Honeywell International Inc. Trans-chloro-3,3,3-trifluoropropene for use in chiller applications
US9000061B2 (en) 2006-03-21 2015-04-07 Honeywell International Inc. Foams and articles made from foams containing 1-chloro-3,3,3-trifluoropropene (HFCO-1233zd)
US9499729B2 (en) * 2006-06-26 2016-11-22 Honeywell International Inc. Compositions and methods containing fluorine substituted olefins
US20090305876A1 (en) * 2006-06-26 2009-12-10 Honeywell International, Inc. Compositions and Methods Containing Fluorine Substituted Olefins
US8333901B2 (en) 2007-10-12 2012-12-18 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
US20110162410A1 (en) * 2007-10-12 2011-07-07 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
US8512591B2 (en) 2007-10-12 2013-08-20 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
US8999190B2 (en) 2007-10-12 2015-04-07 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
US8628681B2 (en) * 2007-10-12 2014-01-14 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
US8070977B2 (en) * 2008-06-11 2011-12-06 Arkema France Hydrofluoroolefin compositions
US8246850B2 (en) 2008-06-11 2012-08-21 Arkema France Hydrofluoroolefin compositions
US8075798B2 (en) * 2008-06-11 2011-12-13 Arkema France Hydrofluoroolefin compositions
US20110095224A1 (en) * 2008-06-11 2011-04-28 Wissam Rached Hydrofluoroolefin compositions
US20110084228A1 (en) * 2008-06-11 2011-04-14 Arkema France Hydrofluoroolefin compositions
US8252198B2 (en) 2008-06-11 2012-08-28 Arkema France Hydrofluoroolefin compositions
US11130893B2 (en) 2008-10-08 2021-09-28 Arkema France Heat transfer fluid
US8053403B2 (en) * 2008-10-15 2011-11-08 Arkema France Cleaning compositions
US20110195890A1 (en) * 2008-10-15 2011-08-11 Laurent Abbas Cleaning compositions
US10858561B2 (en) 2008-10-16 2020-12-08 Arkema France Heat transfer method
US9150768B2 (en) 2008-10-28 2015-10-06 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US8946312B2 (en) 2008-10-28 2015-02-03 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US7935268B2 (en) * 2008-10-28 2011-05-03 Honeywell International Inc. Azeotrope-like compositions comprising trans-1-chloro-3,3,3-trifluoropropene
US20100102272A1 (en) * 2008-10-28 2010-04-29 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US9175200B2 (en) 2008-10-28 2015-11-03 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US8703006B2 (en) 2008-10-28 2014-04-22 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US9926244B2 (en) 2008-10-28 2018-03-27 Honeywell International Inc. Process for drying HCFO-1233zd
US20100102273A1 (en) * 2008-10-28 2010-04-29 Honeywell International Inc. Azeotrope-like compositions comprising trans-1-chloro-3,3,3-trifluoropropene
US8163196B2 (en) * 2008-10-28 2012-04-24 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US8580137B2 (en) * 2009-01-22 2013-11-12 Arkema Inc. Trans-1,2-dichloroethylene with flash point elevated by 1-chloro-3,3,3-trifluoropropene
US20110309288A1 (en) * 2009-01-22 2011-12-22 Arkema Inc. Azeotrope and azeotrope-like compositions of e-1-chloro-3,3,3-trifluoropropene and isopropanol
US20100216904A1 (en) * 2009-02-24 2010-08-26 E. I. Du Pont De Nemours And Company Foam-forming compositions containing mixtures of 2-chloro-3,3,3-trifluoropropene and at least one hydrofluoroolefin and their uses in the preparation of polyisocyanate-based foams
US20110023507A1 (en) * 2009-07-29 2011-02-03 Honeywell International Inc. Compositions and methods for refrigeration
US8974688B2 (en) * 2009-07-29 2015-03-10 Honeywell International Inc. Compositions and methods for refrigeration
US8808569B2 (en) 2009-09-11 2014-08-19 Arkema France Use of ternary compositions
US9683157B2 (en) 2009-09-11 2017-06-20 Arkema France Heat transfer method
US9505968B2 (en) 2009-09-11 2016-11-29 Arkema France Ternary compositions for low-capacity refrigeration
US9175203B2 (en) 2009-09-11 2015-11-03 Arkema France Ternary compositions for low-capacity refrigeration
US9127191B2 (en) 2009-09-11 2015-09-08 Arkema France Use of ternary compositions
US10035938B2 (en) 2009-09-11 2018-07-31 Arkema France Heat transfer fluid replacing R-134a
US9267064B2 (en) 2009-09-11 2016-02-23 Arkema France Ternary compositions for high-capacity refrigeration
US9663697B2 (en) 2009-09-11 2017-05-30 Arkema France Use of ternary compositions
US9399726B2 (en) 2009-09-11 2016-07-26 Arkema France Use of ternary compositions
US9011711B2 (en) 2009-09-11 2015-04-21 Arkema France Heat transfer fluid replacing R-410A
US9308408B2 (en) 2009-12-22 2016-04-12 The Chemours Company Fc, Llc Compositions comprising 2,3,3,3-tetrafluoropropene, 1,1,2,3-tetra-chloropropene, 2-chloro-3,3,3-trifluoropropene, or 2-chloro-1,1,1,2-tetrafluoropropane
US9051500B2 (en) * 2009-12-22 2015-06-09 E I Du Pont De Nemours And Company Compositions comprising 2,3,3,3-tetrafluoropropene, 1,1,2,3-tetra-chloropropene, 2-chloro-3,3,3-trifluoropropene, or 2-chloro-1,1,1,2-tetrafluoropropane
US10688329B2 (en) 2009-12-22 2020-06-23 The Chemours Company Fc, Llc Compositions comprising 2,3,3,3-tetrafluoropropene, 1,1,2,3-tetra-chloropropene, 2-chloro-3,3,3-trifluoropropene, or 2-chloro-1,1,1,2-tetrafluoropropane
US9943717B2 (en) 2009-12-22 2018-04-17 The Chemours Company Fc, Llc Compositions comprising 2,3,3,3-tetrafluoropropene, 1,1,2,3-tetra-chloropropene, 2-chloro-3,3,3-trifluoropropene, or 2-chloro-1,1,1,2-tetrafluoropropane
US12023536B2 (en) 2009-12-22 2024-07-02 The Chemours Company Fc, Llc Compositions comprising 2,3,3,3-tetrafluoropropene, 1,1,2,3 tetrachloropropene, 2-chloro-3,3,3-trifluoropropene, or 2-chloro-1,1,1,2-tetrafluoropropane
US11331525B2 (en) 2009-12-22 2022-05-17 The Chemours Company Fc, Llc Compositions comprising 2,3,3,3-tetrafluoropropene, 1,1,2,3-tetra-chloropropene, 2-chloro-3,3,3-trifluoropropene, or 2-chloro-1,1,1,2-tetrafluoropropane
US20120240477A1 (en) * 2009-12-22 2012-09-27 Ei Du Pont De Nemours And Company Compositions comprising 2,3,3,3-tetrafluoropropene, 1,1,2,3-tetra-chloropropene, 2-chloro-3,3,3-trifluoropropene, or 2-chloro-1,1,1,2-tetrafluoropropane
US11596824B2 (en) 2009-12-22 2023-03-07 The Chemours Company Fc, Llc Compositions comprising 2,3,3,3-tetrafluoropropene, 1,1,2,3-tetra-chloropropene, 2-chloro-3,3,3-trifluoropropene, or 2-chloro-1,1,1,2-tetrafluoropropane
GB2477835A (en) * 2010-02-16 2011-08-17 Ineos Fluor Holdings Ltd Heat transfer compositions
CN104277766A (zh) * 2010-02-16 2015-01-14 墨西哥化学阿玛科股份有限公司 传热组合物
US9175202B2 (en) 2010-02-16 2015-11-03 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
GB2477835B (en) * 2010-02-16 2012-01-04 Mexichem Amanco Holding Sa Heat transfer compositions
US8926856B2 (en) 2010-02-16 2015-01-06 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
US20120329893A1 (en) * 2010-03-09 2012-12-27 Arkema France Hydrochlorofluoroolefin blowing agent compositions
CN102939351A (zh) * 2010-05-20 2013-02-20 墨西哥化学阿玛科股份有限公司 传热组合物
WO2011144907A3 (en) * 2010-05-20 2012-03-08 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
US8808570B2 (en) 2010-05-20 2014-08-19 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
WO2011144905A3 (en) * 2010-05-20 2012-03-08 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
CN102250586A (zh) * 2010-05-20 2011-11-23 墨西哥化学阿玛科股份有限公司 传热组合物
AU2011254381B2 (en) * 2010-05-20 2014-03-06 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
AU2011254380B2 (en) * 2010-05-20 2014-02-20 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
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AU2014203085C1 (en) * 2010-05-20 2016-01-07 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
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US9309450B2 (en) 2010-05-20 2016-04-12 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
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US10844260B2 (en) 2010-06-25 2020-11-24 Mexichem Amanco Holding S.A. De C.V. Heat transfer compositions
US9353302B2 (en) 2010-08-13 2016-05-31 Carrier Corporation Fluorinated hydrocarbon composition
US20120119136A1 (en) * 2010-11-12 2012-05-17 Honeywell International Inc. Low gwp heat transfer compositions
US20140264148A1 (en) * 2010-11-19 2014-09-18 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US8734671B2 (en) * 2010-11-19 2014-05-27 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
CN107033848A (zh) * 2010-11-19 2017-08-11 霍尼韦尔国际公司 包含1‑氯‑3,3,3‑三氟丙烯的类共沸物组合物
US20120128964A1 (en) * 2010-11-19 2012-05-24 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US9410024B2 (en) * 2010-11-19 2016-08-09 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
KR20130116293A (ko) * 2010-11-19 2013-10-23 허니웰 인터내셔널 인코포레이티드 1-클로로-3,3,3-트리플루오로프로펜을 포함하는 유사-공비 조성물
JP2013543050A (ja) * 2010-11-19 2013-11-28 ハネウェル・インターナショナル・インコーポレーテッド 1−クロロ−3,3,3−トリフルオロプロペンを含む共沸混合物様の組成物
US8522606B2 (en) 2010-12-22 2013-09-03 Nuovo Pignone S.P.A. Similitude testing of compressor performance
US10335623B2 (en) 2011-05-19 2019-07-02 Arkema Inc. Non-flammable compositions of chloro-trifluoropropene
US9896558B2 (en) * 2011-08-01 2018-02-20 Basf Se HFO/water-blown rigid foam systems
US20130197115A1 (en) * 2011-08-01 2013-08-01 Basf Se Hfo/water-blown rigid foam systems
US20130149452A1 (en) * 2011-12-09 2013-06-13 Honeywell International, Inc. Foams and articles made from foams containing 1-chloro-3,3,3-trifluoropropene (1233zd)
US20140378559A1 (en) * 2011-12-19 2014-12-25 Honeywell International Inc. Compositions of 1,1,1,3,3-pentafluoropropane and cyclopentane
US9174897B2 (en) 2012-06-28 2015-11-03 Central Glass Company, Limited Method for purifying trans-1,3,3,3-tetrafluoropropene
US8912369B2 (en) 2012-06-29 2014-12-16 Central Glass Company, Limited Method for production of 1-chloro-3,3,3-trifluoropropene
WO2014164587A1 (en) * 2013-03-13 2014-10-09 Honeywell International Inc. Azeotrope-like compositions comprising 1-chloro-3,3,3-trifluoropropene
US10077221B2 (en) 2013-03-20 2018-09-18 Arkema France Composition comprising HF and E-3,3,3-trifluoro-1-chloropropene
US10343963B2 (en) 2013-03-20 2019-07-09 Arkema France Composition comprising HF and E-3,3,3-trifluoro-1-chloropropene
US10330364B2 (en) 2014-06-26 2019-06-25 Hudson Technologies, Inc. System and method for retrofitting a refrigeration system from HCFC to HFC refrigerant
US9816057B2 (en) 2014-10-24 2017-11-14 Edo Shellef Nonflammable composition containing 1,2-dichloroethylene
US20160169575A1 (en) * 2014-12-12 2016-06-16 Honeywell International Inc. Abs liners and cooling cabinets containing same
US10669465B2 (en) 2016-09-19 2020-06-02 Arkema France Composition comprising 1-chloro-3,3,3-trifluoropropene
US11104833B2 (en) * 2016-12-26 2021-08-31 Zhejiang Quhua Fluor-Chemistry Co Ltd Hydrofluoroolefins-containing refrigerant composition
US20220163162A1 (en) * 2019-04-02 2022-05-26 Basf Se Insulated pipe containing polyurethane foam which is foamed by an environmentally friendly foaming agent and has a low degree of brittleness
US11982395B2 (en) * 2019-04-02 2024-05-14 Basf Se Insulated pipe containing polyurethane foam which is foamed by an environmentally friendly foaming agent and has a low degree of brittleness
WO2022213067A1 (en) * 2021-03-30 2022-10-06 Honeywell International Inc. Blowing agents comprising z-1-chloro-2,3,3,3-tetrafluoropentene (hcfo-1224yd(z))
US11753516B2 (en) 2021-10-08 2023-09-12 Covestro Llc HFO-containing compositions and methods of producing foams

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