IN2014CN03586A - - Google Patents

Info

Publication number
IN2014CN03586A
IN2014CN03586A IN3586CHN2014A IN2014CN03586A IN 2014CN03586 A IN2014CN03586 A IN 2014CN03586A IN 3586CHN2014 A IN3586CHN2014 A IN 3586CHN2014A IN 2014CN03586 A IN2014CN03586 A IN 2014CN03586A
Authority
IN
India
Prior art keywords
tubular reactor
vertical tubular
catalyst bed
acid
per
Prior art date
Application number
Inventor
Melle Rinze Nieuwhof
Cornelis Kooijman
Hendrik Jan Vos
Lars Magnus Tollin
Berg Jacobus Van Den
Henricus Johannes Marinus Petrus Van Hal
Original Assignee
Akzo Nobel Chemicals Int Bv
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=47080485&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=IN2014CN03586(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Akzo Nobel Chemicals Int Bv filed Critical Akzo Nobel Chemicals Int Bv
Publication of IN2014CN03586A publication Critical patent/IN2014CN03586A/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/347Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/347Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups
    • C07C51/377Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups by splitting-off hydrogen or functional groups; by hydrogenolysis of functional groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/487Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C53/00Saturated compounds having only one carboxyl group bound to an acyclic carbon atom or hydrogen
    • C07C53/15Saturated compounds having only one carboxyl group bound to an acyclic carbon atom or hydrogen containing halogen
    • C07C53/16Halogenated acetic acids

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

The process of the present invention pertains to a process wherein a liquid feed comprising monochloroacetic acid dichloroacetic acid and optionally acetic acid and/or trichloroacetic acid is subjected to a catalytic hydrodechlorination step by contacting it with a source of hydrogen in the presence of a solid heterogeneous hydrogenation catalyst situated in a fixed catalyst bed wherein the liquid feed is fed to the top of avertical tubular reactor at a superficial mass velocity of between and 10 kg/s per square meter of the horizontal cross section of the vertical tubular reactor and a rate of between 250 and 3 000 kg/hr per m of said catalyst bed wherein the source of hydrogen is fed to the top or bottom of the vertical tubular reactor at a rate of between 0.025 to 0.25 Nm/s per square meter of the horizontal cross section of the vertical tubular reactor so as to obtain an average axial pressure gradient of at least 2 kPa per meter of said catalyst bed and wherein the temperature in the top of the vertical tubular reactor is between 100 and 200°C and wherein the pressure in the top of the vertical tubular reactor is between 0.2and 1.0 MPa.
IN3586CHN2014 2011-10-20 2012-10-17 IN2014CN03586A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP11185953 2011-10-20
PCT/EP2012/070524 WO2013057126A1 (en) 2011-10-20 2012-10-17 Process for the hydrodechlorination of a liquid feed comprising dichloroacetic acid

Publications (1)

Publication Number Publication Date
IN2014CN03586A true IN2014CN03586A (en) 2015-10-09

Family

ID=47080485

Family Applications (1)

Application Number Title Priority Date Filing Date
IN3586CHN2014 IN2014CN03586A (en) 2011-10-20 2012-10-17

Country Status (16)

Country Link
US (1) US9505693B2 (en)
EP (1) EP2748139B1 (en)
JP (1) JP5870199B2 (en)
CN (2) CN105646190A (en)
AR (1) AR088477A1 (en)
AU (1) AU2012324958B2 (en)
BR (1) BR112014008599B1 (en)
CO (1) CO6950504A2 (en)
DK (1) DK2748139T3 (en)
ES (1) ES2625050T3 (en)
IN (1) IN2014CN03586A (en)
MX (1) MX349701B (en)
PL (1) PL2748139T3 (en)
RU (1) RU2608630C2 (en)
WO (1) WO2013057126A1 (en)
ZA (1) ZA201402210B (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6815325B2 (en) 2015-03-17 2021-01-20 ヌーリオン ケミカルズ インターナショナル ベスローテン フェノーツハップNouryon Chemicals International B.V. Process for purification of monochloroacetic acid
AR104892A1 (en) * 2015-06-12 2017-08-23 Akzo Nobel Chemicals Int Bv PROCESS FOR HYDRODECLORATION OF A FOOD THAT INCLUDES DICHLOROACETIC ACID
CN105367410A (en) * 2015-12-02 2016-03-02 中国天辰工程有限公司 Hydrogenation refining system for producing chloroacetic acid
CN105503574A (en) * 2015-12-07 2016-04-20 西安凯立新材料股份有限公司 Hydrodechlorination method for producing high-purity monochloro acetic acid
CN106076418A (en) * 2016-03-14 2016-11-09 郑州航空工业管理学院 A kind of metallic organic framework composite and preparation method
CN108911968B (en) * 2018-05-24 2021-03-05 西安凯立新材料股份有限公司 Method for purifying monochloroacetic acid by catalytic rectification

Family Cites Families (29)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2539238A (en) 1949-08-20 1951-01-23 Monsanto Chemicals Process for the production of monochloroacetic acid
US2671803A (en) 1951-03-12 1954-03-09 Knapsack Ag Dehalogenation of halogeno acetic acids by hydrogenation
US2863917A (en) 1954-03-31 1958-12-09 Hooker Chemical Corp Method for reducing dichloroacetic acid in the presence of monochloro-acetic acid
DE1072980B (en) 1958-07-22 1960-01-14 Knapsack-Griesheim Aktiengesellschaft, Knapsack bei Köln Process for the partial dehalogenation of di- and trihaloacetic acid
NL109769C (en) 1962-05-25 1964-10-15
NL6812630A (en) * 1967-09-19 1969-03-21
DE1816931B2 (en) 1968-12-24 1973-08-23 PROCESS FOR THE PURIFICATION OF A RAW PRODUCT ARISING FROM THE CHLORINATION OF ACETIC ACID WITH THE FORMATION OF MONOCHLOROACETIC ACID
DE2323777C2 (en) 1973-05-11 1975-01-16 Farbwerke Hoechst Ag, Vormals Meister Lucius & Bruening, 6000 Frankfurt Process for the continuous purification of crude monochloroacetic acid
US4051019A (en) 1974-04-22 1977-09-27 Uop Inc. Method for loading finely divided particulate matter into a vessel
US4159785A (en) 1976-06-01 1979-07-03 Uop Inc. Method for loading particulate matter in a vessel
FR2551769B2 (en) 1983-07-05 1990-02-02 Rhone Poulenc Spec Chim NEODYM ALLOYS AND THEIR MANUFACTURING METHOD
FR2645531B1 (en) 1989-04-07 1991-06-07 Atochem PROCESS AND CATALYST FOR DEHALOGENATION OF ALPHAHALOGENIC CARBOXYLIC ACIDS
FR2682616B1 (en) 1991-10-18 1993-12-10 Atochem CATALYSTS FOR DEHALOGENATION OF ALPHAHALOGENIC CARBOXYLIC ACIDS.
EP0557169B1 (en) 1992-02-19 1996-12-27 Elf Atochem S.A. Catalyst for the dehalogenation of alpha-halogenated carboxylic acids and the use thereof for purifying monochloroacetic acid
DE4327872A1 (en) 1992-08-26 1994-03-03 Hoechst Ag Sepn of mono:chloro:acetic acid from an acetic acid chlorination mixt - by rectification in column with ordered carbon-contg. packing
US5449501A (en) 1994-03-29 1995-09-12 Uop Apparatus and process for catalytic distillation
ATE199537T1 (en) 1994-12-02 2001-03-15 Salzgitter Anlagenbau Gmbh METHOD FOR PRODUCING MONOCHLOROACETIC ACID
US5731994A (en) 1995-02-16 1998-03-24 Japan Energy Corporation Method of packing particles into vessels and apparatus therefor
JP3133672B2 (en) * 1995-02-16 2001-02-13 株式会社ジャパンエナジー Particle scattering device
FR2740123B1 (en) 1995-10-20 1998-01-02 Total Raffinage Distribution METHOD AND DEVICE FOR THE UNIFORM DISTRIBUTION OF A SOLID IN DIVIDED FORM IN AN ENCLOSURE
JP2003144921A (en) 2001-11-08 2003-05-20 Daicel Chem Ind Ltd Dehalogenation catalyst and method for manufacturing high purity monochloroacetic acid
DE60236617D1 (en) 2001-12-04 2010-07-15 Akzo Nobel Nv PROCESS FOR THE PREPARATION OF MONOCLOROACTIC ACID
RU2301331C1 (en) 2005-11-18 2007-06-20 Общество с ограниченной ответственностью Научно-производственное предприятие "НКГЕО" Method for hermetically connecting generator to well equipment
EP1900719A1 (en) 2006-09-01 2008-03-19 BUSS ChemTech AG Manufacture of substantially pure monochloroacetic acid
RU2318796C1 (en) 2006-10-18 2008-03-10 Общество с ограниченной ответственностью "Синтез-2" Method for purification of monochloroacetic acid
US7987879B2 (en) 2007-03-07 2011-08-02 Cat Tech, Inc. Methods and apparatus for dense particle loading
JP4659056B2 (en) 2008-03-04 2011-03-30 ダイセル化学工業株式会社 Method for producing dehalogenation catalyst
RU2391331C2 (en) 2008-08-13 2010-06-10 Общество с ограниченной ответственностью "Синтез-2" Method of obtaining monochloracetic acid
CN102001930B (en) * 2010-10-15 2014-08-27 中国天辰工程有限公司 Method for purifying chloroacetic acid by catalytic hydrogenolysis in chloroacetic acid production and application thereof

Also Published As

Publication number Publication date
US20140357892A1 (en) 2014-12-04
RU2014118948A (en) 2015-11-27
AU2012324958B2 (en) 2016-03-17
JP2014530834A (en) 2014-11-20
EP2748139B1 (en) 2017-04-26
ES2625050T3 (en) 2017-07-18
AR088477A1 (en) 2014-06-11
DK2748139T3 (en) 2017-08-07
WO2013057126A1 (en) 2013-04-25
MX349701B (en) 2017-08-08
JP5870199B2 (en) 2016-02-24
MX2014004616A (en) 2014-05-12
PL2748139T3 (en) 2017-08-31
BR112014008599A2 (en) 2017-04-25
BR112014008599B1 (en) 2019-11-05
CN103649039B (en) 2016-01-20
RU2608630C2 (en) 2017-01-23
CO6950504A2 (en) 2014-05-20
AU2012324958A1 (en) 2014-03-20
US9505693B2 (en) 2016-11-29
CN105646190A (en) 2016-06-08
EP2748139A1 (en) 2014-07-02
CN103649039A (en) 2014-03-19
ZA201402210B (en) 2015-04-29

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