FR3064627B1 - PROCESS FOR PRODUCING 2,3,3,3-TETRAFLUOROPROPENE. - Google Patents

PROCESS FOR PRODUCING 2,3,3,3-TETRAFLUOROPROPENE. Download PDF

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Publication number
FR3064627B1
FR3064627B1 FR1752579A FR1752579A FR3064627B1 FR 3064627 B1 FR3064627 B1 FR 3064627B1 FR 1752579 A FR1752579 A FR 1752579A FR 1752579 A FR1752579 A FR 1752579A FR 3064627 B1 FR3064627 B1 FR 3064627B1
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France
Prior art keywords
stream
tetrafluoropropene
bara
producing
hcl
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FR1752579A
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French (fr)
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FR3064627A1 (en
Inventor
Dominique Deur-Bert
Laurent Wendlinger
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Arkema France SA
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Arkema France SA
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Priority to FR1752579A priority Critical patent/FR3064627B1/en
Priority to PCT/FR2018/050732 priority patent/WO2018178552A1/en
Publication of FR3064627A1 publication Critical patent/FR3064627A1/en
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/093Preparation of halogenated hydrocarbons by replacement by halogens
    • C07C17/20Preparation of halogenated hydrocarbons by replacement by halogens of halogen atoms by other halogen atoms
    • C07C17/202Preparation of halogenated hydrocarbons by replacement by halogens of halogen atoms by other halogen atoms two or more compounds being involved in the reaction
    • C07C17/206Preparation of halogenated hydrocarbons by replacement by halogens of halogen atoms by other halogen atoms two or more compounds being involved in the reaction the other compound being HX
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/25Preparation of halogenated hydrocarbons by splitting-off hydrogen halides from halogenated hydrocarbons
    • 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

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

La présente invention concerne un procédé de production du 2,3,3,3-tetrafluoropropène comprenant les étapes de : a) mise en contact, en phase gazeuse, d'un composé de formule (I) CH(n+2)(X)m-CHp(X)(n+1)-CX(3+p-m) où X représente indépendamment F ou Cl ; n, m, p sont indépendamment les uns des autres 0 ou 1 avec (n+m) = 0 ou 1, (n+p) = 0 ou 1 et (m-p) = 0 ou 1, au moins un X étant Cl, avec de l'acide fluorhydrique pour obtenir un flux de produits comprenant 2,3,3,3-tetrafluoropropène, HCI et HF, b) refroidissement du flux de produits issus du réacteur de l'étape a) à une température de 0°C à 70°C, de préférence à une température de 20°C à 50°C, c) distillation du flux refroidi à l'étape b) pour former un premier courant comprenant 2,3,3,3-tetrafluoropropène et HCI, et un second courant comprenant HF, d) compression du premier courant obtenu à l'étape c) pour former un premier courant comprimé, e) distillation dudit premier courant comprimé obtenu à l'étape d) pour un troisième courant comprenant HCI et un quatrième courant comprenant 2,3,3,3-tetrafluoropropène, f) purification dudit quatrième courant obtenu à l'étape e), caractérisé en ce que l'étape a) est mise en œuvre à une pression inférieure à 10 bara, de préférence à une pression de 2 à 8 bara, en particulier de 3 à 7 bara, plus particulièrement de 5 à 7 bara.The present invention relates to a process for producing 2,3,3,3-tetrafluoropropene comprising the steps of: a) bringing into contact, in the gas phase, a compound of formula (I) CH (n + 2) (X ) m-CHp (X) (n + 1) -CX (3 + pm) where X independently represents F or Cl; n, m, p are independently of each other 0 or 1 with (n + m) = 0 or 1, (n + p) = 0 or 1 and (mp) = 0 or 1, at least one X being Cl, with hydrofluoric acid to obtain a product flow comprising 2,3,3,3-tetrafluoropropene, HCl and HF, b) cooling the product flow from the reactor of step a) to a temperature of 0 ° C. at 70 ° C, preferably at a temperature of 20 ° C to 50 ° C, c) distillation of the stream cooled in step b) to form a first stream comprising 2,3,3,3-tetrafluoropropene and HCl, and a second stream comprising HF, d) compression of the first stream obtained in step c) to form a first compressed stream, e) distillation of said first compressed stream obtained in step d) for a third stream comprising HCI and a fourth stream comprising 2,3,3,3-tetrafluoropropene, f) purification of said fourth stream obtained in step e), characterized in that step a) is carried out at a lower pressure 10 bara, preferably at a pressure of 2 to 8 bara, especially from 3 to 7 bara, more preferably from 5 to 7 bara.

FR1752579A 2017-03-28 2017-03-28 PROCESS FOR PRODUCING 2,3,3,3-TETRAFLUOROPROPENE. Active FR3064627B1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
FR1752579A FR3064627B1 (en) 2017-03-28 2017-03-28 PROCESS FOR PRODUCING 2,3,3,3-TETRAFLUOROPROPENE.
PCT/FR2018/050732 WO2018178552A1 (en) 2017-03-28 2018-03-27 Method for the production of 2,3,3,3-tetrafluoropropene

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR1752579A FR3064627B1 (en) 2017-03-28 2017-03-28 PROCESS FOR PRODUCING 2,3,3,3-TETRAFLUOROPROPENE.
FR1752579 2017-03-28

Publications (2)

Publication Number Publication Date
FR3064627A1 FR3064627A1 (en) 2018-10-05
FR3064627B1 true FR3064627B1 (en) 2020-02-21

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FR1752579A Active FR3064627B1 (en) 2017-03-28 2017-03-28 PROCESS FOR PRODUCING 2,3,3,3-TETRAFLUOROPROPENE.

Country Status (2)

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FR (1) FR3064627B1 (en)
WO (1) WO2018178552A1 (en)

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4902838A (en) 1988-12-28 1990-02-20 E. I. Du Pont De Nemours And Company Isomerization of saturated fluorohydrocarbons
DE69909860T2 (en) 1998-02-26 2004-05-27 Central Glass Co., Ltd., Ube Process for the production of fluorinated propanes
FR2808268B1 (en) 2000-04-26 2002-08-30 Atofina IONIC LIQUIDS DERIVED FROM TITANIUM, NIOBIUM, TANTALUM, TIN OR ANTIMONY LEWIS ACIDS AND THEIR APPLICATIONS
EP2546223B1 (en) 2006-01-03 2016-08-10 Honeywell International Inc. Method for producing fluorinated organic compounds
FR2901790A1 (en) 2006-05-30 2007-12-07 Arkema France PROCESS FOR PRODUCING HYDROFLUOROCARBONS
KR101394583B1 (en) 2006-10-03 2014-05-12 멕시켐 아만코 홀딩 에스.에이. 데 씨.브이. Dehydrogenationhalogenation process for the production of C3-C6(hydro)fluoroalkenes
CN103483140B (en) 2006-10-31 2015-09-09 纳幕尔杜邦公司 The preparation method of chloro-3,3, the 3-tri-fluoro-1-propylene of fluoro-propane, propylene halide and 2-and the Azeotrope compositions of HF and the Azeotrope compositions of 1,1,1,2,2-pentafluoropropane and HF
FR2916755B1 (en) 2007-05-31 2009-08-21 Arkema France PROCESS FOR THE PREPARATION OF (HYDRO) (CHLORO) (FLUORO) OLEFINS
FR2929271B1 (en) 2008-03-28 2010-04-16 Arkema France PROCESS FOR THE PREPARATION OF 1,2,3,3,3-PENTAFLUOROPROPENE-1
HUE025859T2 (en) * 2009-12-23 2016-05-30 Arkema France Catalytic gas phase fluorination of 243db to 1234yf
CN103328422A (en) 2011-01-21 2013-09-25 阿克马法国公司 Process for the manufacture of 2,3,3,3- tetrafluoropropene by gas phase fluorination of pentachloropropane
FR2977584B1 (en) * 2011-07-08 2014-12-05 Arkema France PROCESS FOR SEPARATING AND RECOVERING 2,3,3,3-TETRAFLUOROPROPENE AND FLUORHYDRIC ACID
FR2986525B1 (en) * 2012-02-03 2014-02-14 Arkema France PROCESS FOR PRODUCING 2,3,3,3-TETRAFLUOROPROPENE

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Publication number Publication date
FR3064627A1 (en) 2018-10-05
WO2018178552A1 (en) 2018-10-04

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