BR9806967A - - Google Patents

Info

Publication number
BR9806967A
BR9806967A BR9806967A BR9806967A BR9806967A BR 9806967 A BR9806967 A BR 9806967A BR 9806967 A BR9806967 A BR 9806967A BR 9806967 A BR9806967 A BR 9806967A BR 9806967 A BR9806967 A BR 9806967A
Authority
BR
Brazil
Prior art keywords
reaction
cobalt
oxidation
liquid
butane
Prior art date
Application number
BR9806967A
Other languages
English (en)
Inventor
Derek Alan Colman
Andrew Richard Lucy
Jeremy Bernard Cooper
Original Assignee
Bp Chem Int Ltd
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=10806385&utm_source=***_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=BR9806967(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Bp Chem Int Ltd filed Critical Bp Chem Int Ltd
Publication of BR9806967A publication Critical patent/BR9806967A/pt

Links

Classifications

    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/26—Nozzle-type reactors, i.e. the distribution of the initial reactants within the reactor is effected by their introduction or injection through nozzles
    • 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
    • B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2455—Stationary reactors without moving elements inside provoking a loop type movement of the reactants
    • B01J19/2465—Stationary reactors without moving elements inside provoking a loop type movement of the reactants externally, i.e. the mixture leaving the vessel and subsequently re-entering it
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
    • C07C51/215—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of saturated hydrocarbyl groups
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
    • B01J2219/00103—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor in a heat exchanger separate from the reactor
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00105—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2219/0011—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling involving reactant liquids
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00186—Controlling or regulating processes controlling the composition of the reactive mixture
    • 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
    • Y02P20/582—Recycling of unreacted starting or intermediate materials

Landscapes

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

Abstract

cesso para oxidação da fase líquida do butano para produzir ácido acético pela reação pela reação do oxigênio e butano na presença de um catalisador de cobalto em uma composição de reação líquida em uma zona de reação de oxidação, caracterizado pelo ra na zona de reação, na faixa de 120 a 180° C, enquanto mantém continuamente uma concentração de oxo equivalente a uma pressão parcial de oxigênio maior que 2 bar e uma concentração de catalisador de oxidação de cobalto na composição da reação líquida de pelo menos 0,12% em peso de cobalto e até seu limite de solubilidade na composição de reação líquida.
BR9806967A 1997-01-22 1998-01-20 BR9806967A (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GBGB9701251.2A GB9701251D0 (en) 1997-01-22 1997-01-22 Process
PCT/GB1998/000168 WO1998032725A1 (en) 1997-01-22 1998-01-20 Process for the production of acetic acid

Publications (1)

Publication Number Publication Date
BR9806967A true BR9806967A (pt) 2000-03-21

Family

ID=10806385

Family Applications (1)

Application Number Title Priority Date Filing Date
BR9806967A BR9806967A (pt) 1997-01-22 1998-01-20

Country Status (16)

Country Link
US (1) US6057475A (pt)
EP (1) EP0966422A1 (pt)
JP (1) JP2001508453A (pt)
KR (1) KR20000070341A (pt)
CN (1) CN1250433A (pt)
AR (1) AR011562A1 (pt)
AU (1) AU5672798A (pt)
BR (1) BR9806967A (pt)
CA (1) CA2278012A1 (pt)
GB (1) GB9701251D0 (pt)
ID (1) ID22136A (pt)
NO (1) NO993543L (pt)
TW (1) TW453988B (pt)
WO (1) WO1998032725A1 (pt)
YU (1) YU33699A (pt)
ZA (1) ZA98496B (pt)

Families Citing this family (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6215027B1 (en) * 1998-10-20 2001-04-10 Praxair Technology, Inc. Ballast gas use in liquid phase oxidation
DE10206168A1 (de) * 2002-02-14 2003-08-21 Guehring Joerg Kupplung für mudular aufgebaute Werkzeughalterarme
US7361784B2 (en) * 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) * 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) * 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7683210B2 (en) * 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7495125B2 (en) * 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) * 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7582793B2 (en) * 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US20060047153A1 (en) * 2004-09-02 2006-03-02 Wonders Alan G Optimized liquid-phase oxidation
US7572936B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7563926B2 (en) * 2004-09-02 2009-07-21 Eastman Chemical Company Optimized liquid-phase oxidation
US7608733B2 (en) * 2004-09-02 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7910769B2 (en) * 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7482482B2 (en) * 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7586000B2 (en) * 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
CN101023046B (zh) * 2004-09-02 2019-01-18 奇派特石化有限公司 优化的液相氧化
US7399882B2 (en) * 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) * 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) * 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7371894B2 (en) * 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) * 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7381836B2 (en) * 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
JP2006248951A (ja) * 2005-03-09 2006-09-21 Daicel Chem Ind Ltd 脂肪族飽和カルボン酸の製造法
US7884232B2 (en) * 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7355068B2 (en) * 2006-01-04 2008-04-08 Eastman Chemical Company Oxidation system with internal secondary reactor

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB721914A (en) * 1951-06-30 1955-01-12 Celanese Corp Oxidation of hydrocarbons
GB1020797A (en) * 1964-03-12 1966-02-23 Tekkosha Kabushiki Kaisha Improvements in the production of monocarboxylic lower fatty acids
US3483250A (en) * 1966-07-08 1969-12-09 Halcon International Inc Oxidation of n-butane
BE749000A (fr) * 1969-05-01 1970-09-16 Gulf Research & Dev Cy Procede pour la conversion de butane en acide
US3644512A (en) * 1969-10-10 1972-02-22 Gulf Research Development Co Process for converting butane to acetic acid
US4032570A (en) * 1971-11-08 1977-06-28 Gulf Research & Development Company Process for converting butane to acetic acid
US3923882A (en) * 1974-04-17 1975-12-02 Union Carbide Corp Production of acetic acid
GB1528771A (en) * 1975-07-21 1978-10-18 Bp Chem Int Ltd Cobalt-catalysed oxidation of c3 to c7 saturated aliphatic hydrocarbons to acetic acid
GB1531247A (en) * 1975-11-03 1978-11-08 Bp Chem Int Ltd Cobalt-catalysed oxidation of hydrocarbons
US4111986A (en) * 1977-04-19 1978-09-05 Standard Oil Company (Indiana) Butane oxidation to acetic acid
US4158740A (en) * 1978-03-20 1979-06-19 Gulf Research & Development Company Oxidation of butane to acetic acid
NO800968L (no) * 1979-04-06 1980-10-07 Bp Chem Int Ltd Kontinuerlig prosess for fremstilling av oksygenholdige organiske forbindelser inneholdende en vesentlig andel eddiksyre
US4337356A (en) * 1980-03-20 1982-06-29 Union Carbide Corporation Catalytic liquid-phase oxidation of butane
CA1224486A (en) * 1983-05-23 1987-07-21 David J. Schreck Liquid phase oxidation of alkanes
US4900480A (en) * 1986-10-21 1990-02-13 Union Carbide Corporation Gas-liquid mixing
JPH06116217A (ja) * 1992-10-02 1994-04-26 Kuraray Co Ltd （±）−シス−４−アミノシクロペント−２−エンカルボン酸誘導体の光学分割法
US5371283A (en) * 1993-12-22 1994-12-06 Praxair Technology, Inc. Terephthalic acid production

Also Published As

Publication number Publication date
AU5672798A (en) 1998-08-18
US6057475A (en) 2000-05-02
YU33699A (sh) 2001-03-07
TW453988B (en) 2001-09-11
JP2001508453A (ja) 2001-06-26
EP0966422A1 (en) 1999-12-29
AR011562A1 (es) 2000-08-30
CN1250433A (zh) 2000-04-12
ZA98496B (en) 1999-07-21
WO1998032725A1 (en) 1998-07-30
NO993543L (no) 1999-09-21
GB9701251D0 (en) 1997-03-12
KR20000070341A (ko) 2000-11-25
ID22136A (id) 1999-09-09
NO993543D0 (no) 1999-07-19
CA2278012A1 (en) 1998-07-30

Similar Documents

Publication Publication Date Title
BR9806967A (pt)
ES2153138T3 (es) Procedimiento para hacer reaccionar monoxido de carbono con un reactante carbonilable y/o un ester derivado del mismo.
Stanley et al. Copper stress underlies the fundamental change in intracellular location of methane mono-oxygenase in methane-oxidizing organisms: studies in batch and continuous cultures
BR9810625A (pt) Terpolìmeros de propileno e processo para sua produção
BRPI0416168A (pt) processo em contracorrente em estágio contìnuo de oxidação catalìtica, mistura de produto e composição
BR0109070A (pt) Processo e aparelho para preparar anidrido maleico
ATE261925T1 (de) Schwefel-enthaltender promoter für oxidative dehydrierungsverfahren von kohlenwasserstoffen
DE69510404T2 (de) Öle mit niedrigem Gehalt an gesättigter Fettsäure
GB1276792A (en) Acetone purification process
BR0011843A (pt) Preparação e medição de componentes misturados com co2
GB1315052A (en) Preparation of cycloalkanones and cycloalkanols
BR9914569A (pt) Processo para a oxidação de um composto orgânico contendo pelo menos uma ligação dupla c-c
BR9914612A (pt) Preparação de acroleìna e/ou ácido acrìlico a partir do propano.
KR890001918A (ko) 메타크롤레인의 후산화 방지 방법
KR960034156A (ko) 유기 화합물의 연속적인 불균일하게 촉매 작용된 기체상 부분 산화 방법
BR9914611A (pt) Processo para a preparação de acroleìna e/ou ácido acrìlico a partir do propano.
BR9908543A (pt) Processo contìnuo para preparar uma poliamida, e, poliamida
BR9916139A (pt) Processo para a produção de acetato de vinila
KR960004335A (ko) 트리옥산의 제조방법
ES2040033T3 (es) Procedimiento para preparar un catalizador util en la dimerizacion de butadieno.
BR0005515A (pt) Processo de partida para a produção em fase gasosa de polibutadieno
ES2159161T3 (es) Procedimiento para producir acido prusico y catalizador.
Malviya et al. Observations on the oxidoreduction of the two cytochromes b in cytochrome c-deficient mitochondria and submitochondrial particles
BR9607990A (pt) Conversão em fase lìquida de uma fonte de dióxido de enxofre a ácido sulfúrico.
BR9809222A (pt) Método para preparação de ácido formilfosfÈnico

Legal Events

Date Code Title Description
B08F Application fees: application dismissed [chapter 8.6 patent gazette]

Free format text: REFERENTE A 6A,7A,8A E 9A ANUIDADES.

B08K Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette]

Free format text: REFERENTE AO DESPACHO 8.6 PUBLICADO NA RPI 1888 DE 13/03/2007.