WO2002059231A2 - Azeotrope-like composition of 1,2-dichloro-3,3,3-trifluoropropene and hydrogen fluoride - Google Patents

Azeotrope-like composition of 1,2-dichloro-3,3,3-trifluoropropene and hydrogen fluoride Download PDF

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Publication number
WO2002059231A2
WO2002059231A2 PCT/US2002/001970 US0201970W WO02059231A2 WO 2002059231 A2 WO2002059231 A2 WO 2002059231A2 US 0201970 W US0201970 W US 0201970W WO 02059231 A2 WO02059231 A2 WO 02059231A2
Authority
WO
WIPO (PCT)
Prior art keywords
composition
hydrogen fluoride
azeotrope
trifluoropropene
dichloro
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.)
Ceased
Application number
PCT/US2002/001970
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English (en)
French (fr)
Other versions
WO2002059231A3 (en
Inventor
Hang Thanh Pham
Hsueh Sung Tung
Rajiv Ratna Singh
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
Application filed by Honeywell International Inc filed Critical Honeywell International Inc
Priority to MXPA03006562A priority Critical patent/MXPA03006562A/es
Priority to DE60238175T priority patent/DE60238175D1/de
Priority to AT02707553T priority patent/ATE486915T1/de
Priority to JP2002559520A priority patent/JP4219168B2/ja
Priority to EP02707553A priority patent/EP1354019B1/en
Priority to AU2002241953A priority patent/AU2002241953A1/en
Publication of WO2002059231A2 publication Critical patent/WO2002059231A2/en
Publication of WO2002059231A3 publication Critical patent/WO2002059231A3/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D7/00Compositions of detergents based essentially on non-surface-active compounds
    • C11D7/50Solvents
    • C11D7/5036Azeotropic mixtures containing halogenated solvents
    • C11D7/504Azeotropic mixtures containing halogenated solvents all solvents being halogenated hydrocarbons
    • C11D7/5045Mixtures of (hydro)chlorofluorocarbons
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/38Separation; Purification; Stabilisation; Use of additives
    • C07C17/383Separation; Purification; Stabilisation; Use of additives by distillation
    • C07C17/386Separation; Purification; Stabilisation; Use of additives by distillation with auxiliary compounds
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C21/00Acyclic unsaturated compounds containing halogen atoms
    • C07C21/02Acyclic unsaturated compounds containing halogen atoms containing carbon-to-carbon double bonds
    • C07C21/18Acyclic unsaturated compounds containing halogen atoms containing carbon-to-carbon double bonds containing fluorine
    • 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
    • C09K5/00Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D7/00Compositions of detergents based essentially on non-surface-active compounds
    • C11D7/02Inorganic compounds
    • C11D7/04Water-soluble compounds
    • C11D7/08Acids

Definitions

  • the present invention pertains to azeotropic and azeotrope-like compositions of l,2-dichloro-3,3,3-trifluoropropene (HCFC-1223xd) and hydrogen fluoride.
  • HFC hydrofluorocarbon
  • HFC-245fa 1,1,1,3,3-Pentafluoropropane
  • an intermediate in the production of substantially pure 1,1,1 ,3 ,3 -pentafluoropropane is an azeotropic or azeotrope-like mixture of 1 ,2- dichloro-3,3,3-trifluoropropene (HCFC-1223xd) and hydrogen fluoride.
  • This intermediate once formed, may thereafter be separated into its component parts by extraction techniques.
  • the azeotropic and azeotrope-like compositions find use as anhydrous (non-aqueous) etchants for etching semiconductors in the electronics industry as well as compositions for removing surface oxidation from metals.
  • HCFC-1223xd may be used as a pharmaceutical intermediate.
  • the invention provides an azeotropic composition consisting essentially of l,2-dichloro-3, 3, 3 -trifluoropropene and hydrogen fluoride.
  • the invention further provides an azeotropic or azeotrope-like composition consisting essentially of from about 1 to about 90 weight percent hydrogen fluoride and from about 10 to about 99 weight percent l,2-dichloro-3, 3, 3 -trifluoropropene, which composition has a boiling point of from about 26°C to about 68°C at a pressure of from about 24 psia to about 84 psia.
  • the invention provides a method of forming an azeotropic or azeotrope-like composition, which method comprises blending from about 1 to about 90 weight percent hydrogen fluoride and from about 10 to about 99 weight percent of l,2-dichloro-3, 3, 3 -trifluoropropene, which composition has a boiling point of from about 26°C to about 68°C at a pressure of from about 24 psia to about 84 psia.
  • the invention provides a process for removing l,2-dichloro-3,3,3-trifluoropropene from a mixture of l,2-dichloro-3,3,3- trifluoropropene and at least one impurity, which process comprises adding hydrogen fluoride to the mixture in an amount sufficient to form an azeotropic or azeotrope-like composition of 1 ,2-dichloro-3,3,3-trifluoropropene and hydrogen fluoride, and thereafter separating the azeotropic composition from the impurity.
  • FIG. 1 shows a Vapor-Liquid-Liquid Equilibrium (VLLE) plot for HCFC-1223xd and HF.
  • VLLE Vapor-Liquid-Liquid Equilibrium
  • This binary azeotrope or azeotrope-like composition is then available for separation into its component parts.
  • thermodynamic state of a fluid is defined by its pressure, temperature, liquid composition and vapor composition.
  • the liquid composition and vapor phase are essentially equal at a given temperature and pressure range. In practical terms this means that the components cannot be separated during a phase change.
  • an azeotrope-like composition means that the composition behaves like a true azeotrope in terms of its constant boiling characteristics and tendency not to fractionate upon boiling or evaporation. During boiling or evaporation, the liquid composition changes only slightly, if at all. This is in contrast with non-azeotrope-like compositions in which the liquid and vapor compositions change substantially during evaporation or condensation.
  • One way to determine whether a candidate mixture is azeotrope-like within the meaning of this invention is to distill a sample of it under conditions which would be expected to separate the mixture into its separate components. If the mixture is a non-azeotrope or non-azeotrope-like, the mixture will fractionate, i.e. separate into its various components with the lowest boiling component distilling off first, and so on. If the mixture is azeotrope-like, some finite amount of the first distillation cut will be obtained which contains all of the mixture components and which is constant boiling or behaves like a single substance. Another characteristic of azeotrope-like compositions is that there is a range of compositions containing the same components in varying proportions that are azeotrope-like.
  • compositions are included by the term azeotrope-like as used herein.
  • azeotrope-like As an example, it is well known that at different pressures the composition of a given azeotrope will vary at least slightly as does the boiling point of the composition. Thus an azeotrope of two components represents a unique type of relationship but with a variable composition depending on the temperature and/or pressure. As is well known in the art, the boiling point of an azeotrope will vary with pressure.
  • an azeotrope is a liquid mixture that exhibits a maximum or minimum boiling point relative to the boiling points of surrounding mixture compositions.
  • An azeotrope or an azeotrope-like composition is an admixture of two or more different components which, when in liquid form under given pressure, will boil at a substantially constant temperature, which temperature may be higher or lower than the boiling temperatures of the components and which will provide a vapor composition essentially identical to the liquid composition undergoing boiling.
  • azeotropic compositions are defined to include azeotrope-like compositions which means a composition that behaves like an azeotrope, i.e., has constant-boiling characteristics or a tendency not to fractionate upon boiling or evaporation.
  • the composition of the vapor formed during boiling or evaporation is the same as or substantially the same as the original liquid composition.
  • the liquid composition if it changes at all, changes only to a minimal or negligible extent.
  • the essential features of an azeotrope or an azeotrope-like composition are that at a given pressure, the boiling point of the liquid composition is fixed and that the composition of the vapor above the boiling composition is essentially that of the boiling liquid composition, i.e., essentially no fractionation of the components of the liquid composition takes place.
  • Both the boiling point and the weight percentages of each component of the azeotropic composition may change when the azeotrope or azeotrope-like liquid composition is subjected to boiling at different pressures.
  • an azeotrope or an azeotrope-like composition may be defined in terms of the relationship that exists between its components or in terms of the compositional ranges of the components or in terms of exact weight percentages of each component of the composition characterized by a fixed boiling point at a specified pressure.
  • the present invention provides a composition comprising effective amounts of hydrogen fluoride and HCFC-1223xd to form an azeotropic or azeotrope-like composition.
  • effective amount is meant an amount of each component which, when combined with the other component, results in the formation of an azeotrope or azeotrope-like mixture.
  • inventive compositions preferably are binary azeotropes that consist essentially of combinations of only hydrogen fluoride with HCFC-1223xd.
  • the inventive composition contains from about 1 to about 90 weight percent HF, preferably from about 10 weight percent to about 80 weight percent and most preferably from about 40 weight percent to about 60 weight percent. In the preferred embodiment, the inventive composition contains from about 10 to about 99 weight percent HCFC-1223xd, preferably from about 20 weight percent to about 90 weight percent and most preferably from about 40 weight percent to about 60 weight percent.
  • the composition of the present invention has a boiling point of from about 26°C to about 68°C at a pressure of from about 24 psia to about 84 psia.
  • An azeotropic or azeotrope-like composition having about 55 ⁇ 5 weight percent HF and about 45 ⁇ 5 weight percent HCFC-1223xd has been found to boil at about 26°C and 23 psia.
  • An azeotropic or azeotrope-like composition of about 50 ⁇ 5 weight percent HF and about 50 ⁇ 5 weight percent HCFC-1223xd has been found to boil at about 45°C and 42 psia.
  • HCFC-1223xd may be removed from a mixture containing of HCFC-1223xd and an impurity which may, for example, result from manufacturing steps in the preparation of HCFC-1223xd. This is done by adding hydrogen fluoride to a mixture of HCFC-1223xd and the impurity. Hydrogen fluoride is added to the mixture in an amount sufficient to form an azeotropic composition of HCFC-1223xd and hydrogen fluoride, and thereafter the azeotropic composition is separated from the impurity, for example by distillation, scrubbing, or other art recognized separating means.
  • the impurity itself does not form a close-boiling azeotropic mixture with HCFC-1223xd, hydrogen fluoride or a mixture of HCFC-1223xd and hydrogen fluoride.
  • close-boiling azeotropic mixture means an azeotropic mixture having a boiling point within 10°C of the azeotropic mixture of the invention. The following non-limiting examples serve to illustrate the invention.
  • EXAMPLE 1 50 g of l,2-dichloro-3,3,3-trifluoropropene (HCFC-1223xd) is dissolved in 50 g of HF to form a heterogeneous mixture.
  • the vapor pressure of the mixture at 26°C is 23 psia.
  • EXAMPLE 2 55 g of l,2-dichloro-3, 3, 3 -trifluoropropene is dissolved in 45 g of HF to form a heterogeneous mixture.
  • the vapor pressure of the mixture at 45°C is 42 psia.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Wood Science & Technology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Physics & Mathematics (AREA)
  • Inorganic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Thermal Sciences (AREA)
  • Materials Engineering (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Detergent Compositions (AREA)
  • Weting (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Nitrogen Condensed Heterocyclic Rings (AREA)
  • Plural Heterocyclic Compounds (AREA)
PCT/US2002/001970 2001-01-24 2002-01-17 Azeotrope-like composition of 1,2-dichloro-3,3,3-trifluoropropene and hydrogen fluoride Ceased WO2002059231A2 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
MXPA03006562A MXPA03006562A (es) 2001-01-24 2002-01-17 Composcion tipo azeotropo de 1,2-dicloro-3,3,3-trifluoropropeno y fluoruro de hidrogeno.
DE60238175T DE60238175D1 (de) 2001-01-24 2002-01-17 Azeotrop-ähnliche zusammensetzung von 1,2-dichlor-
AT02707553T ATE486915T1 (de) 2001-01-24 2002-01-17 Azeotrop-ähnliche zusammensetzung von 1,2-dichlor-3,3,3-trifluorpropen und fluorwasserstoff
JP2002559520A JP4219168B2 (ja) 2001-01-24 2002-01-17 1,2−ジクロロ−3,3,3−トリフルオロプロペン及びフッ化水素の共沸様組成物
EP02707553A EP1354019B1 (en) 2001-01-24 2002-01-17 Azeotrope-like composition of 1,2-dichloro-3,3,3-trifluoropropene and hydrogen fluoride
AU2002241953A AU2002241953A1 (en) 2001-01-24 2002-01-17 Azeotrope-like composition of 1,2-dichloro-3,3,3-trifluoropropene and hydrogen fluoride

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US09/768,415 US6475971B2 (en) 2001-01-24 2001-01-24 Azeotrope-like composition of 1,2-dichloro-3,3,3-trifluoropropene and hydrogen fluoride composition
US09/768,415 2001-01-24

Publications (2)

Publication Number Publication Date
WO2002059231A2 true WO2002059231A2 (en) 2002-08-01
WO2002059231A3 WO2002059231A3 (en) 2002-09-26

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PCT/US2002/001970 Ceased WO2002059231A2 (en) 2001-01-24 2002-01-17 Azeotrope-like composition of 1,2-dichloro-3,3,3-trifluoropropene and hydrogen fluoride

Country Status (10)

Country Link
US (1) US6475971B2 (enExample)
EP (1) EP1354019B1 (enExample)
JP (1) JP4219168B2 (enExample)
CN (1) CN100406534C (enExample)
AT (1) ATE486915T1 (enExample)
AU (1) AU2002241953A1 (enExample)
DE (1) DE60238175D1 (enExample)
ES (1) ES2353736T3 (enExample)
MX (1) MXPA03006562A (enExample)
WO (1) WO2002059231A2 (enExample)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004099109A1 (en) * 2003-05-06 2004-11-18 Honeywell International Inc. Azeotrope-like compositions of 1-chloro-1,3,3,3-tetrafluoropropane and 1,2-dichloro-3,3,3-trifluoropropene
WO2005044969A1 (en) * 2003-11-04 2005-05-19 Honeywell International Inc. Solvent compositions containing chlorofluoroolefins or hydrochiloroolefins
WO2005103188A1 (en) * 2004-04-16 2005-11-03 Honeywell International Inc. Azeotrope-like compositions of tetrafluoropropene and pentafluoropropene
US7098176B2 (en) 2004-04-16 2006-08-29 Honeywell International Inc. Azeotrope-like compositions of tetrafluoropropene and pentafluoropropene
US7605117B2 (en) 2004-04-16 2009-10-20 Honeywell International Inc. Methods of replacing refrigerant
GB2546845A (en) * 2016-09-05 2017-08-02 Mexichem Fluor Sa De Cv Composition

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7074751B2 (en) * 2004-04-16 2006-07-11 Honeywell International Inc. Azeotrope-like compositions of tetrafluoropropene and trifluoroiodomethane
US8546624B2 (en) * 2008-03-06 2013-10-01 Honeywell International Inc. Azeotrope-like composition of 2-chloro-3,3,3-trifluoropropene (HCFC-1233xf) and hydrogen fluoride (HF)
EP2098499B2 (en) 2008-03-06 2017-11-22 Honeywell International Inc. Azeotrope-like composition of 2-chloro-3,3,3-trifluoropropene (HCFC-1233xf) and hydrogen fluoride (HF)
US8114308B2 (en) * 2010-03-30 2012-02-14 Honeywell International Inc. Azeotrope-like composition of 2,3-dichloro-3,3-difluoropropene (HCFO-1232xf) and hydrogen fluoride (HF)
US8883707B2 (en) 2010-06-30 2014-11-11 Honeywell International Inc. Azeotrope-like composition of PF5 and HF
US8378158B2 (en) * 2010-12-03 2013-02-19 Honeywell International Inc. Azeotrope-like compositions of (Z)-1-chloro-3,3,3-trifluoropropene and hydrogen fluoride
US8519200B1 (en) * 2012-02-23 2013-08-27 Honeywell International Inc. Azeotropic compositions of 1,1,3,3-tetrachloro-1-fluoropropane and hydrogen fluoride
US8999909B2 (en) * 2012-02-23 2015-04-07 Honeywell International Inc. Azeotropic compositions of 1,1,1,3,3-pentachloropropane and hydrogen fluoride
JP6432306B2 (ja) * 2014-11-21 2018-12-05 セントラル硝子株式会社 含フッ素オレフィンを構成成分とする共沸様組成物
GB2540428B (en) * 2015-07-17 2017-09-13 Mexichem Fluor Sa De Cv Process for preparing 3,3,3-trifluoropropene
KR101769206B1 (ko) 2015-10-01 2017-08-17 (주)후성 하이드로클로로플루오로올레핀류의 공비 조성물 또는 유사 공비 조성물을 포함하는 발포제 및 이를 포함하는 폴리올 프리믹스 조성물
JP6749768B2 (ja) * 2016-02-10 2020-09-02 三菱重工サーマルシステムズ株式会社 熱源機およびその運転方法
US10029964B2 (en) 2016-08-30 2018-07-24 Honeywell International Inc. Azeotropic or azeotrope-like compositions of 3,3,3-trifluoropropyne and water
US9950974B2 (en) 2016-08-31 2018-04-24 Honeywell International Inc. Azeotropic or azeotrope-like compositions of 1,3,3-trichloro-3-fluoro-1-ene (HCFO-1231zd) and hydrogen fluoride (HF)
US9950973B2 (en) 2016-08-31 2018-04-24 Honeywell International Inc. Azeotropic or azeotrope-like compositions of 1,3-dichloro-3,3-difluoroprop-1-ene (HCFO-1232zd) and hydrogen fluoride (HF)
CN110945099B (zh) 2017-07-27 2024-07-05 科慕埃弗西有限公司 包含氟化氢和氟碳化合物的共沸组合物

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Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006525374A (ja) * 2003-05-06 2006-11-09 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−1、3、3、3−テトラフルオロプロパン及び1、2−ジクロロ−3、3、3−トリフルオロプロペンの共沸類組成物
WO2004099109A1 (en) * 2003-05-06 2004-11-18 Honeywell International Inc. Azeotrope-like compositions of 1-chloro-1,3,3,3-tetrafluoropropane and 1,2-dichloro-3,3,3-trifluoropropene
US9095737B2 (en) 2003-11-04 2015-08-04 Honeywell International Inc. Compositions containing chlorofluoroolefins or fluoroolefins
US7674756B2 (en) 2003-11-04 2010-03-09 Honeywell International Inc. Solvent compositions containing chlorofluoroolefins or fluoroolefins
US7985299B2 (en) 2003-11-04 2011-07-26 Honeywell International Inc. Solvent compositions containing chlorofloroolefins or fluoroolefins
US8618040B2 (en) 2003-11-04 2013-12-31 Honeywell International Inc. Solvent compositions containing chlorofluoroolefins or fluoroolefins
WO2005044969A1 (en) * 2003-11-04 2005-05-19 Honeywell International Inc. Solvent compositions containing chlorofluoroolefins or hydrochiloroolefins
US9586071B2 (en) 2003-11-04 2017-03-07 Honeywell International Inc. Compositions containing chlorofluoroolefins or fluoroolefins
US10066140B2 (en) 2003-11-04 2018-09-04 Honeywell International Inc. Compositions containing chlorofluoroolefins or fluoroolefins
US7098176B2 (en) 2004-04-16 2006-08-29 Honeywell International Inc. Azeotrope-like compositions of tetrafluoropropene and pentafluoropropene
WO2005103188A1 (en) * 2004-04-16 2005-11-03 Honeywell International Inc. Azeotrope-like compositions of tetrafluoropropene and pentafluoropropene
US7605117B2 (en) 2004-04-16 2009-10-20 Honeywell International Inc. Methods of replacing refrigerant
EP3275963A1 (en) * 2004-04-16 2018-01-31 Honeywell International Inc. Azeotrope-like compositions of tetrafluoropropene and pentafluoropropene
GB2546845A (en) * 2016-09-05 2017-08-02 Mexichem Fluor Sa De Cv Composition

Also Published As

Publication number Publication date
CN100406534C (zh) 2008-07-30
ES2353736T3 (es) 2011-03-04
US20020137645A1 (en) 2002-09-26
EP1354019A2 (en) 2003-10-22
US6475971B2 (en) 2002-11-05
ATE486915T1 (de) 2010-11-15
JP2004529087A (ja) 2004-09-24
CN1487986A (zh) 2004-04-07
JP4219168B2 (ja) 2009-02-04
AU2002241953A1 (en) 2002-08-06
EP1354019B1 (en) 2010-11-03
WO2002059231A3 (en) 2002-09-26
MXPA03006562A (es) 2004-05-05
DE60238175D1 (de) 2010-12-16

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