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MX370246B - Metodo para la produccion de acido acetico. - Google Patents

Metodo para la produccion de acido acetico.

Info

Publication number
MX370246B
MX370246B MX2019004920A MX2019004920A MX370246B MX 370246 B MX370246 B MX 370246B MX 2019004920 A MX2019004920 A MX 2019004920A MX 2019004920 A MX2019004920 A MX 2019004920A MX 370246 B MX370246 B MX 370246B
Authority
MX
Mexico
Prior art keywords
acetic acid
vaporization tank
vortex breaker
production method
catalyst
Prior art date
Application number
MX2019004920A
Other languages
English (en)
Other versions
MX2019004920A (es
Inventor
Shimizu Masahiko
Original Assignee
Daicel Corp
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=60421720&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=MX370246(B) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Daicel Corp filed Critical Daicel Corp
Publication of MX2019004920A publication Critical patent/MX2019004920A/es
Publication of MX370246B publication Critical patent/MX370246B/es

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/10—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide
    • C07C51/12—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide on an oxygen-containing group in organic compounds, e.g. alcohols
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/06—Halogens; Compounds thereof
    • B01J27/08—Halides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/1616—Coordination complexes, e.g. organometallic complexes, immobilised on an inorganic support, e.g. ship-in-a-bottle type catalysts
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42—Separation; Purification; Stabilisation; Use of additives
    • C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
    • C07C51/44—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C53/00—Saturated compounds having only one carboxyl group bound to an acyclic carbon atom or hydrogen
    • C07C53/08—Acetic acid
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/584—Recycling of catalysts

Landscapes

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

Abstract

Se proporciona un metodo para producir acido acetico, que suprime la precipitacion y la acumulacion de catalizadores en un evaporador, puede reciclar eficientemente catalizadores a un recipiente de reaccion y puede contribuir al mantenimiento y mejora en la productividad de acido acetico y asegurar la operacion de seguridad; en el metodo, el evaporador tiene una estructura de prevencion de precipitacion y acumulacion de catalizadores: (a) estructura en la que el angulo de inclinacion ? de la superficie de la pared interior de una porcion de conexion cilindrica conica truncada invertida es de 5o a 85o; y/o (b) estructura en la que un dispositivo antirremolino que comprende un cuerpo principal del dispositivo antirremolino similar a placa y una pata se dispone de tal manera que el cuerpo principal del dispositivo antirremolino cubre directamente encima de la porcion de conexion de una parte inferior del evaporador a una linea de reciclado de corriente de liquido residual y la velocidad lineal r de la corriente de liquido residual que pasa a traves de un espacio entre el cuerpo principal del dispositivo antirremolino y la parte inferior del evaporador es superior a 10 m/h.
MX2019004920A 2016-10-28 2017-05-25 Metodo para la produccion de acido acetico. MX370246B (es)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2016211922 2016-10-28
JP2017039388 2017-03-02
PCT/JP2017/019572 WO2018078924A1 (ja) 2016-10-28 2017-05-25 酢酸の製造方法

Publications (2)

Publication Number Publication Date
MX2019004920A MX2019004920A (es) 2019-06-20
MX370246B true MX370246B (es) 2019-12-04

Family

ID=60421720

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2019004920A MX370246B (es) 2016-10-28 2017-05-25 Metodo para la produccion de acido acetico.

Country Status (11)

Country Link
EP (1) EP3333147B1 (es)
JP (1) JP6491750B2 (es)
KR (1) KR102257562B1 (es)
CN (1) CN110214132A (es)
BR (1) BR112019008340A2 (es)
ES (1) ES2744537T3 (es)
MX (1) MX370246B (es)
MY (1) MY186617A (es)
PH (1) PH12019550075A1 (es)
TW (1) TWI697476B (es)
WO (1) WO2018078924A1 (es)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
MX370246B (es) 2016-10-28 2019-12-04 Daicel Corp Metodo para la produccion de acido acetico.
WO2019220522A1 (ja) * 2018-05-15 2019-11-21 株式会社ダイセル 酢酸の製造方法
CN110325503B (zh) * 2018-05-29 2023-05-02 株式会社大赛璐 乙酸的制备方法
US10737996B2 (en) 2018-05-29 2020-08-11 Daicel Corporation Method for producing acetic acid
JP6588656B1 (ja) * 2018-05-29 2019-10-09 株式会社ダイセル 酢酸の製造方法
WO2019229856A1 (ja) * 2018-05-29 2019-12-05 株式会社ダイセル 酢酸の製造方法
WO2019229857A1 (ja) * 2018-05-29 2019-12-05 株式会社ダイセル 酢酸の製造方法
US12060322B2 (en) * 2018-07-02 2024-08-13 Daicel Corporation Method for producing acetic acid
EP3611154B1 (en) 2018-07-02 2021-09-08 Daicel Corporation Method for producing acetic acid
US11884617B2 (en) 2018-07-02 2024-01-30 Daicel Corporation Method for producing acetic acid
EP3611153B1 (en) * 2018-07-02 2021-06-16 Daicel Corporation Method for producing acetic acid

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US3845121A (en) 1971-11-10 1974-10-29 Monsanto Co Process for separating carbonylation products from reaction mixture without catalyst decomposition
JPS5710301A (en) 1980-06-18 1982-01-19 Daicel Chem Ind Ltd Concentrating device
US4733006A (en) 1980-12-29 1988-03-22 Monsanto Company Carbonylation process with an alkali metal acetate as catalyst stabilizer
US5144068A (en) 1984-05-03 1992-09-01 Hoechst Celanese Corporation Methanol carbonylation process
CA1299195C (en) 1986-06-16 1992-04-21 G. Paull Torrence Addition of hydrogen to carbon monoxide feed gas in producing acetic acid by carbonylation of methanol
CA2035426A1 (en) 1990-02-09 1991-08-10 David W. Smith Catalytic carbonylation process
US5374774A (en) 1994-03-11 1994-12-20 Hoechst Celanese Corporation Control system for an acetic acid manufacturing process
IN192600B (es) 1996-10-18 2004-05-08 Hoechst Celanese Corp
US6632329B1 (en) 1999-10-29 2003-10-14 Nippon Shokubai Co., Ltd. Distillation apparatus and distilling method
JP5069827B2 (ja) 2001-02-28 2012-11-07 株式会社ダイセル 反応制御方法および制御装置
US6599348B2 (en) 2001-06-01 2003-07-29 Celanese International Corporation Methods for reducing entrainment of solids and liquids
US7223886B2 (en) 2004-03-02 2007-05-29 Celanese International Corporation Removal of permanganate reducing compounds from methanol carbonylation process stream
US7855306B2 (en) 2005-04-28 2010-12-21 Celanese International Corporation Process for the production of acetic acid
CN1757627A (zh) * 2005-06-30 2006-04-12 西南化工研究设计院 甲醇低压液相羰基合成醋酸工艺中反应热平衡调节方法
KR20080061390A (ko) 2005-10-03 2008-07-02 다이셀 가가꾸 고교 가부시끼가이샤 아세트산의 제조 방법
CA2655086A1 (en) 2006-06-13 2007-12-21 Shell Internationale Research Maatschappij B.V. Glycol separation and purification
CN200984467Y (zh) * 2006-12-14 2007-12-05 上海太平洋化工(集团)公司焦化设计院 一种用于羰基合成醋酐及醋酸工艺中的闪蒸器
US7989659B2 (en) 2007-05-17 2011-08-02 Celanese International Corporation Method and apparatus for making acetic acid with improved light ends column productivity
CN201415064Y (zh) * 2009-04-03 2010-03-03 北京泽华化学工程有限公司 一种用于化工生产中的闪蒸器
RU2527035C2 (ru) * 2009-04-24 2014-08-27 Инвиста Текнолоджиз С.А.Р.Л. Способы, процессы и системы для обработки и очистки сырой терефталевой кислоты и ассоциированные потоки процесса
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CN103249705B (zh) * 2010-10-06 2015-11-25 株式会社大赛璐 乙酸的制造方法
BR112013014801B1 (pt) * 2010-12-15 2019-04-02 Daicel Corporation Processo para produzir ácido acétido, método para inibir a corrosão de um reator de carbonilação em um processo de produção de ácido acético,e processo ou método.
JP6007108B2 (ja) * 2010-12-24 2016-10-12 株式会社ダイセル 酢酸の製造方法
US9079121B2 (en) * 2011-12-02 2015-07-14 Celanese International Corporation Distillation column having enlarged downcomers and method of downcomer enlargement
CN104080764B (zh) 2011-12-16 2016-09-14 国际人造丝公司 催化剂稳定性增强的乙酸制备方法
US9193657B2 (en) 2012-08-17 2015-11-24 Celanese International Corporation Catalyst stability in carbonylation processes
AR094541A1 (es) * 2013-01-25 2015-08-12 Daicel Corp Procedimiento para producir ácido carboxílico
EP3177588A1 (en) * 2014-08-05 2017-06-14 BP Chemicals Limited Process
JP2016211922A (ja) 2015-05-01 2016-12-15 Ckd株式会社 三次元計測装置
JP6421987B2 (ja) 2015-08-20 2018-11-14 豊田合成株式会社 オープニングトリムウエザストリップ
MX370246B (es) 2016-10-28 2019-12-04 Daicel Corp Metodo para la produccion de acido acetico.

Also Published As

Publication number Publication date
MX2019004920A (es) 2019-06-20
TWI697476B (zh) 2020-07-01
EP3333147A1 (en) 2018-06-13
EP3333147A4 (en) 2018-06-13
JP6491750B2 (ja) 2019-03-27
EP3333147B1 (en) 2019-07-10
WO2018078924A1 (ja) 2018-05-03
KR102257562B1 (ko) 2021-05-31
TW201829364A (zh) 2018-08-16
JPWO2018078924A1 (ja) 2018-10-25
MY186617A (en) 2021-07-30
PH12019550075A1 (en) 2020-01-20
KR20190069546A (ko) 2019-06-19
CN110214132A (zh) 2019-09-06
ES2744537T3 (es) 2020-02-25
BR112019008340A2 (pt) 2019-08-06

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