ES2162183T3 - Inyeccion directa de oxigeno en reactores de columna de burbujas. - Google Patents

Inyeccion directa de oxigeno en reactores de columna de burbujas.

Info

Publication number
ES2162183T3
ES2162183T3 ES97121683T ES97121683T ES2162183T3 ES 2162183 T3 ES2162183 T3 ES 2162183T3 ES 97121683 T ES97121683 T ES 97121683T ES 97121683 T ES97121683 T ES 97121683T ES 2162183 T3 ES2162183 T3 ES 2162183T3
Authority
ES
Spain
Prior art keywords
oxygen
bubble column
direct injection
column reactors
gas containing
Prior art date
Legal status (The legal status 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 status listed.)
Expired - Lifetime
Application number
ES97121683T
Other languages
English (en)
Inventor
Jeffrey Paul Kingsley
Roger William Day
Lawrence Marvin Litz
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Praxair Technology Inc
Original Assignee
Praxair Technology Inc
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
Application filed by Praxair Technology Inc filed Critical Praxair Technology Inc
Application granted granted Critical
Publication of ES2162183T3 publication Critical patent/ES2162183T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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
    • 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
    • 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
    • B01J10/002—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor carried out in foam, aerosol or bubbles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • 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
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C407/00—Preparation of peroxy compounds
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C409/00—Peroxy compounds
    • C07C409/02—Peroxy compounds the —O—O— group being bound between a carbon atom, not further substituted by oxygen atoms, and hydrogen, i.e. hydroperoxides
    • C07C409/04—Peroxy compounds the —O—O— group being bound between a carbon atom, not further substituted by oxygen atoms, and hydrogen, i.e. hydroperoxides the carbon atom being acyclic
    • C07C409/08—Compounds containing six-membered aromatic rings
    • C07C409/10—Cumene hydroperoxide
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/27—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation
    • C07C45/32—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen
    • C07C45/33—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

LA INVENCION SE REFIERE A UN PROCEDIMIENTO DE OXIDACION EN FASE LIQUIDA, EN EL QUE UN PRIMER GAS QUE CONTIENE OXIGENO SE INYECTA EN LA ZONA INFERIOR DEL RECIPIENTE DE UN REACTOR DE COLUMNA DE BURBUJEO, QUE CONTIENE UN LIQUIDO ORGANICO OXIDABLE. UN SEGUNDO GAS QUE CONTIENE OXIGENO SE INYECTA EN EL INTERIOR DEL REACTOR A UN PUNTO O PUNTOS EN LOS QUE EL LIQUIDO ESTA PRACTICAMENTE EMPOBRECIDO EN OXIGENO DISUELTO ANTES DE DICHA INYECCION. EL OXIGENO PROCEDENTE TANTO DEL PRIMER COMO DEL SEGUNDO GAS QUE CONTIENE OXIGENO SE UTILIZA PARA OXIDAR EL LIQUIDO ORGANICO.
ES97121683T 1996-12-12 1997-12-09 Inyeccion directa de oxigeno en reactores de columna de burbujas. Expired - Lifetime ES2162183T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US76660396A 1996-12-12 1996-12-12

Publications (1)

Publication Number Publication Date
ES2162183T3 true ES2162183T3 (es) 2001-12-16

Family

ID=25076942

Family Applications (1)

Application Number Title Priority Date Filing Date
ES97121683T Expired - Lifetime ES2162183T3 (es) 1996-12-12 1997-12-09 Inyeccion directa de oxigeno en reactores de columna de burbujas.

Country Status (12)

Country Link
US (1) US5994567A (es)
EP (1) EP0847800B1 (es)
JP (1) JPH10330292A (es)
KR (1) KR19980063918A (es)
CN (1) CN1195577A (es)
AR (1) AR009658A1 (es)
BR (1) BR9706246A (es)
CA (1) CA2224529A1 (es)
DE (1) DE69706268T2 (es)
ES (1) ES2162183T3 (es)
ID (1) ID19133A (es)
PT (1) PT847800E (es)

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US7048262B2 (en) * 2001-11-01 2006-05-23 Praxair Technology, Inc. Method and apparatus for injecting oxygen into fermentation processes
DE10206168A1 (de) * 2002-02-14 2003-08-21 Guehring Joerg Kupplung für mudular aufgebaute Werkzeughalterarme
JP2003238529A (ja) * 2002-02-15 2003-08-27 Sumitomo Chem Co Ltd 酸化反応方法
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US20060110358A1 (en) * 2002-08-28 2006-05-25 Hsu Henry H Combination therapy for treatment of fibrotic disorders
KR101168875B1 (ko) * 2004-03-04 2012-07-30 미쓰비시 가가꾸 가부시키가이샤 쿠멘 하이드로퍼옥사이드의 제조 방법
JP2008507398A (ja) * 2004-07-21 2008-03-13 ピットニイ ボウズ インコーポレイテッド 標準クラスの郵便物の識別による配達ルート上の停止の回数を低減するシステム及び方法
US7507857B2 (en) 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
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US7390921B2 (en) * 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US20070238899A9 (en) * 2004-09-02 2007-10-11 Robert Lin Optimized production of aromatic dicarboxylic acids
US7589231B2 (en) * 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
PL1786751T3 (pl) * 2004-09-02 2015-12-31 Grupo Petrotemex Sa De Cv Optymalne utlenianie w fazie ciekłej
US7495125B2 (en) * 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7482482B2 (en) * 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) * 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
PT1786753E (pt) * 2004-09-02 2015-12-01 Grupo Petrotemex Sa De Cv Oxidação em fase líquida otimizada
US7608732B2 (en) * 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
WO2006028817A2 (en) * 2004-09-02 2006-03-16 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7381836B2 (en) * 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
PT1791800T (pt) * 2004-09-02 2018-02-02 Grupo Petrotemex Sa De Cv Oxidação em fase líquida optimizada
US7683210B2 (en) * 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7910769B2 (en) * 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7361784B2 (en) * 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7572936B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7586000B2 (en) * 2004-09-02 2009-09-08 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
US7888530B2 (en) * 2004-09-02 2011-02-15 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7741515B2 (en) 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
JP2008511645A (ja) * 2004-09-02 2008-04-17 イーストマン ケミカル カンパニー 最適化液相酸化
US7959879B2 (en) * 2004-09-02 2011-06-14 Grupo Petrotemex, S.A. De C.V. Optimized production of aromatic dicarboxylic acids
US7371894B2 (en) * 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
US7563926B2 (en) * 2004-09-02 2009-07-21 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) * 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7884232B2 (en) 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7569722B2 (en) * 2005-08-11 2009-08-04 Eastman Chemical Company Process for removal of benzoic acid from an oxidizer purge stream
US7355068B2 (en) * 2006-01-04 2008-04-08 Eastman Chemical Company Oxidation system with internal secondary reactor
US7358389B2 (en) * 2006-01-04 2008-04-15 Eastman Chemical Company Oxidation system employing internal structure for enhanced hydrodynamics
US20070203359A1 (en) * 2006-03-01 2007-08-30 Philip Edward Gibson Versatile oxidation byproduct purge process
US20070208194A1 (en) * 2006-03-01 2007-09-06 Woodruff Thomas E Oxidation system with sidedraw secondary reactor
US7897808B2 (en) * 2006-03-01 2011-03-01 Eastman Chemical Company Versatile oxidation byproduct purge process
US7816556B2 (en) * 2006-03-01 2010-10-19 Eastman Chemical Company Polycarboxylic acid production system employing enhanced multistage oxidative digestion
US7772424B2 (en) * 2006-03-01 2010-08-10 Eastman Chemical Company Polycarboxylic acid production system employing enhanced evaporative concentration downstream of oxidative digestion
US7880032B2 (en) * 2006-03-01 2011-02-01 Eastman Chemical Company Versatile oxidation byproduct purge process
US7863481B2 (en) * 2006-03-01 2011-01-04 Eastman Chemical Company Versatile oxidation byproduct purge process
US7420082B2 (en) * 2006-03-01 2008-09-02 Eastman Chemical Company Polycarboxylic acid production system employing hot liquor removal downstream of oxidative digestion
US7501537B2 (en) * 2006-03-01 2009-03-10 Eastman Chemical Company Polycarboxylic acid production system employing oxidative digestion with reduced or eliminated upstream liquor exchange
US8936767B2 (en) 2010-01-29 2015-01-20 Grupo Petrotemex. S.A. de C.V. Oxidation system with sidedraw secondary reactor
US8790601B2 (en) * 2010-01-29 2014-07-29 Grupo Petrotemex, S.A. De C.V. Oxidation system with sidedraw secondary reactor
US8968686B2 (en) 2010-01-29 2015-03-03 Grupo Petrotemex, S.A. De C.V. Oxidation system with sidedraw secondary reactor
CN102266739B (zh) * 2011-06-20 2013-06-19 广东佳德环保科技有限公司 一种利用微泡实现氧及自由基液相高效传质的工艺
US10076739B1 (en) * 2014-07-22 2018-09-18 Precision Combustion, Inc. Chemical reactor for use with overly reactive chemicals
RU2566504C1 (ru) * 2014-08-08 2015-10-27 Общество с ограниченной ответственностью "Научно-производственное объединение ЕВРОХИМ" Способ окисления алкилароматических углеводородов и реактор для его осуществления
CN114502711A (zh) 2019-10-09 2022-05-13 勃林格殷格翰国际公司 以工业规模培养悬浮细胞或微生物的生物反应器或发酵器

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Also Published As

Publication number Publication date
CA2224529A1 (en) 1998-06-12
PT847800E (pt) 2002-02-28
DE69706268D1 (de) 2001-09-27
KR19980063918A (ko) 1998-10-07
EP0847800A3 (en) 1998-08-12
EP0847800A2 (en) 1998-06-17
DE69706268T2 (de) 2002-05-23
AR009658A1 (es) 2000-04-26
ID19133A (id) 1998-06-18
CN1195577A (zh) 1998-10-14
US5994567A (en) 1999-11-30
BR9706246A (pt) 2000-08-08
JPH10330292A (ja) 1998-12-15
MX9709967A (es) 1998-07-31
EP0847800B1 (en) 2001-08-22

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