MX349701B - Proceso para la hidrodecloracion de una alimentacion liquida que comprende acido dicloroacetico. - Google Patents

Proceso para la hidrodecloracion de una alimentacion liquida que comprende acido dicloroacetico.

Info

Publication number
MX349701B
MX349701B MX2014004616A MX2014004616A MX349701B MX 349701 B MX349701 B MX 349701B MX 2014004616 A MX2014004616 A MX 2014004616A MX 2014004616 A MX2014004616 A MX 2014004616A MX 349701 B MX349701 B MX 349701B
Authority
MX
Mexico
Prior art keywords
tubular reactor
vertical tubular
liquid feed
catalyst bed
acid
Prior art date
Application number
MX2014004616A
Other languages
English (en)
Other versions
MX2014004616A (es
Inventor
Rinze Nieuwhof Melle
Kooijman Cornelis
Jan Vos Hendrik
Magnus Tollin Lars
Van Den Berg Jacobus
Johannes Marinus Petrus Van Hal Henricus
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=MX349701(B) "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 MX2014004616A publication Critical patent/MX2014004616A/es
Publication of MX349701B publication Critical patent/MX349701B/es

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
    • 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
    • C07C51/347Preparation 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
    • C07C51/42Separation; 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

El proceso de la presente invención se refiere a un proceso en donde una alimentación líquida que comprende ácido monocloroacético, ácido dicloroacético y, opcionalmente, ácido acético y/o ácido tricloroacético se somete a un paso de hidrodecloración catalítica poniéndola en contacto con una fuente de hidrógeno en presencia de un catalizador heterogéneo para la hidrogenación situado en un lecho de catalizador fijo, en donde la alimentación líquida se alimenta por la parte superior de un reactor tubular vertical a un velocidad de masa superficial de entre 1 y 10 kg/s por metro cuadrado de la sección transversal horizontal del reactor tubular vertical y una velocidad de entre 250 y 3000 kg/h por m3 de dicho lecho de catalizador, en donde la fuente de hidrógeno se alimenta por la parte superior o de fondo del reactor tubular vertical a una velocidad de entre 0.025 a 0.25 Nm3/s por metro cuadrado de la sección transversal horizontal del reactor tubular vertical, para obtener un gradiente de presión axial promedio de por lo menos 2 kPa por metro de dicho lecho de catalizador, y en donde la temperatura en la parte superior del reactor tubular vertical es de entre 100 y 200°C, y en donde la presión en la parte superior del reactor tubular vertical es de entre 0.2 y 1.0 MPa.
MX2014004616A 2011-10-20 2012-10-17 Proceso para la hidrodecloracion de una alimentacion liquida que comprende acido dicloroacetico. MX349701B (es)

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 (2)

Publication Number Publication Date
MX2014004616A MX2014004616A (es) 2014-05-12
MX349701B true MX349701B (es) 2017-08-08

Family

ID=47080485

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2014004616A MX349701B (es) 2011-10-20 2012-10-17 Proceso para la hidrodecloracion de una alimentacion liquida que comprende acido dicloroacetico.

Country Status (16)

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

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BR112017018047B1 (pt) * 2015-03-17 2021-11-23 Akzo Nobel Chemicals International B.V. Processo de purificação de alimentação
AR104892A1 (es) * 2015-06-12 2017-08-23 Akzo Nobel Chemicals Int Bv Proceso para la hidrodecloración de una alimentación que comprende ácido dicloroacético
CN105367410A (zh) * 2015-12-02 2016-03-02 中国天辰工程有限公司 一种生产氯乙酸的加氢精制系统
CN105503574A (zh) * 2015-12-07 2016-04-20 西安凯立新材料股份有限公司 一种催化加氢脱氯生产高纯一氯乙酸的方法
CN106076418A (zh) * 2016-03-14 2016-11-09 郑州航空工业管理学院 一种金属有机骨架复合材料及制备方法
CN108911968B (zh) * 2018-05-24 2021-03-05 西安凯立新材料股份有限公司 一种催化精馏纯化一氯乙酸的方法
CN120398816A (zh) * 2024-01-24 2025-08-01 上海凌凯科技股份有限公司 一种碳酸亚乙烯酯的制备方法

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 (de) 1958-07-22 1960-01-14 Knapsack-Griesheim Aktiengesellschaft, Knapsack bei Köln Verfahren zum partiellen Dehalogenieren von Di- und Trihalogenessigsäure
NL109769C (es) 1962-05-25 1964-10-15
NL6812630A (es) * 1967-09-19 1969-03-21
DE1816931B2 (de) * 1968-12-24 1973-08-23 Verfahren zur reinigung eines bei der chlorierung von essigsaeure unter bildung von monochloressigsaeure anfallenden rohproduktes
DE2323777C2 (de) * 1973-05-11 1975-01-16 Farbwerke Hoechst Ag, Vormals Meister Lucius & Bruening, 6000 Frankfurt Verfahren zur kontinuierlichen Reinigung von roher Monochloressigsäure
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 (fr) 1983-07-05 1990-02-02 Rhone Poulenc Spec Chim Alliages de neodyme et leur procede de fabrication
FR2645531B1 (fr) 1989-04-07 1991-06-07 Atochem Procede et catalyseur de deshalogenation d'acides carboxyliques alphahalogenes
FR2682616B1 (fr) * 1991-10-18 1993-12-10 Atochem Catalyseurs de deshalogenation d'acides carboxyliques alphahalogenes.
ES2095589T3 (es) * 1992-02-19 1997-02-16 Atochem Elf Sa Catalizador de deshalogenacion de acidos carboxilicos alfahalogenados y su utilizacion para purificar el acido monocloroacetico.
DE4327872A1 (de) 1992-08-26 1994-03-03 Hoechst Ag Verfahren zum Abtrennen von Monochloressigsäure durch Rektifikation
US5449501A (en) 1994-03-29 1995-09-12 Uop Apparatus and process for catalytic distillation
ES2156134T3 (es) * 1994-12-02 2001-06-16 Salzgitter Anlagenbau Gmbh Procedimiento para la obtencion de acido monocloracetico.
JP3133672B2 (ja) * 1995-02-16 2001-02-13 株式会社ジャパンエナジー 粒子散布装置
KR100203995B1 (ko) 1995-02-16 1999-06-15 나가시마 카쭈시게, 노미야마 아키히코 입자충전방법 및 장치
FR2740123B1 (fr) 1995-10-20 1998-01-02 Total Raffinage Distribution Procede et dispositif pour la distribution uniforme d'un solide sous forme divisee dans une enceinte
JP2003144921A (ja) 2001-11-08 2003-05-20 Daicel Chem Ind Ltd 脱ハロゲン化触媒及び高純度モノクロロ酢酸の製造法
ATE469876T1 (de) 2001-12-04 2010-06-15 Akzo Nobel Nv Verfahren zur herstellung von monochloressigsäure
RU2301331C1 (ru) 2005-11-18 2007-06-20 Общество с ограниченной ответственностью Научно-производственное предприятие "НКГЕО" Герметичное соединение генератора со скважинным прибором
EP1900719A1 (en) 2006-09-01 2008-03-19 BUSS ChemTech AG Manufacture of substantially pure monochloroacetic acid
RU2318796C1 (ru) * 2006-10-18 2008-03-10 Общество с ограниченной ответственностью "Синтез-2" Способ очистки монохлоруксусной кислоты
US7987879B2 (en) 2007-03-07 2011-08-02 Cat Tech, Inc. Methods and apparatus for dense particle loading
JP4659056B2 (ja) 2008-03-04 2011-03-30 ダイセル化学工業株式会社 脱ハロゲン化触媒の製造方法
RU2391331C2 (ru) 2008-08-13 2010-06-10 Общество с ограниченной ответственностью "Синтез-2" Способ получения монохлоруксусной кислоты
CN102001930B (zh) * 2010-10-15 2014-08-27 中国天辰工程有限公司 一氯乙酸生产中催化氢解提纯一氯乙酸的方法及其用途

Also Published As

Publication number Publication date
EP2748139B1 (en) 2017-04-26
CN105646190A (zh) 2016-06-08
CN103649039A (zh) 2014-03-19
MX2014004616A (es) 2014-05-12
US20140357892A1 (en) 2014-12-04
WO2013057126A1 (en) 2013-04-25
ZA201402210B (en) 2015-04-29
AR088477A1 (es) 2014-06-11
RU2014118948A (ru) 2015-11-27
EP2748139A1 (en) 2014-07-02
ES2625050T3 (es) 2017-07-18
AU2012324958B2 (en) 2016-03-17
BR112014008599B1 (pt) 2019-11-05
AU2012324958A1 (en) 2014-03-20
DK2748139T3 (en) 2017-08-07
JP2014530834A (ja) 2014-11-20
CN103649039B (zh) 2016-01-20
PL2748139T3 (pl) 2017-08-31
JP5870199B2 (ja) 2016-02-24
BR112014008599A2 (pt) 2017-04-25
CO6950504A2 (es) 2014-05-20
IN2014CN03586A (es) 2015-10-09
US9505693B2 (en) 2016-11-29
RU2608630C2 (ru) 2017-01-23

Similar Documents

Publication Publication Date Title
MX2014004616A (es) Proceso para la hidrodecloracion de una alimentacion liquida que comprende acido dicloroacetico.
CL2011001612A1 (es) Proceso de produccion de acetato de vinilo que comprende: contactar una corriente de alimentacion de acido acetico e hidrogeno a temperatura elevada con catalizador de hidrogenacion, enriquecer la corriente con acetato de etilo,contactar la corriente con un catalizador de cracking, y separar el acetato de vinilo
MX2011011738A (es) Produccion de ester de vinilo a partir de acetileno y carboxilico usando catalizador homogeneo.
MX2012013920A (es) Reactor de terminacion para la purificacion de etanol.
NZ592785A (en) Integrated process for the production of vinyl acetate from acetic acid via ethylene
MX2012004842A (es) Proceso para hacer etanol a partir de acido acetico utilizando catalizadores acidos.
MY156559A (en) Process for preparing toluenediamine by hydrogenation of dinitrotoluene
PH12014500727A1 (en) Production of adipic acid and derivatives from carbohydrate-containing materials
MY162490A (en) One-step method for butadiene production
MY168081A (en) Ethyl acetate production
MX2014004617A (es) Proceso para la purificacion de una alimentacion liquida que comprende mca y dca.
IN2014DN10247A (es)
UA100016C2 (en) Process for the production of methyl acetate
WO2009137427A3 (en) A process for the start-up of an epoxidation process, a process for the production of ethylene oxide, a 1,2-diol, a 1,2-diol ether, a 1,2-carbonate, or an alkanolamine
DE602008004976D1 (de) Verfahren zur Herstellung von 1,2-Propylenglykol unter Verwendung von Glycerin
WO2011140460A3 (en) Process for producing ethanol by hydrogenation of a purified acetic acid feed stream
MY150056A (en) Method for producing hydrogenolysis product of polyhydric alcohol
MX350643B (es) Procedimiento para la produccion de acetato de vinilo.
MX350908B (es) Hidrogenacion catalitica de fluoroolefinas, composiciones de paladio soportado sobre alfa-alumina y su uso como catalizadores de hidrogenacion.
AU2016232404B2 (en) Process for the purification of monochloroacetic acid
AU2013409375A1 (en) Method for preparing polyoxymethylene dimethyl ether carbonyl compound and methyl methoxyacetate
NZ601367A (en) Processes for producing denatured ethanol
MX2011011739A (es) Produccion de ester de vinilo a partir de acetileno y acido carboxilico usando catalizador heterogeneo.
WO2014154751A3 (de) Verfahren zur herstellung von vinylacetat
MY184173A (en) Method for producing ethylene glycol from oxalate through the fluidized bed catalytic reaction

Legal Events

Date Code Title Description
FG Grant or registration