ID19133A - Pengisian oksigen langsung kedalam reaktor-reaktor ruang gelembung - Google Patents

Pengisian oksigen langsung kedalam reaktor-reaktor ruang gelembung

Info

Publication number
ID19133A
ID19133A IDP973696A ID973696A ID19133A ID 19133 A ID19133 A ID 19133A ID P973696 A IDP973696 A ID P973696A ID 973696 A ID973696 A ID 973696A ID 19133 A ID19133 A ID 19133A
Authority
ID
Indonesia
Prior art keywords
oxygen directly
filling oxygen
bullet room
reactors
room reactors
Prior art date
Application number
IDP973696A
Other languages
English (en)
Indonesian (id)
Inventor
Jeffrey Paul Kingsley
Roger William Day
Lawrence Malvin Litz
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
Publication of ID19133A publication Critical patent/ID19133A/id

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)
IDP973696A 1996-12-12 1997-11-17 Pengisian oksigen langsung kedalam reaktor-reaktor ruang gelembung ID19133A (id)

Applications Claiming Priority (1)

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

Publications (1)

Publication Number Publication Date
ID19133A true ID19133A (id) 1998-06-18

Family

ID=25076942

Family Applications (1)

Application Number Title Priority Date Filing Date
IDP973696A ID19133A (id) 1996-12-12 1997-11-17 Pengisian oksigen langsung kedalam reaktor-reaktor ruang gelembung

Country Status (12)

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

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DE19843573A1 (de) * 1998-09-23 2000-03-30 Degussa Blasensäule und deren Verwendung
US6451268B1 (en) * 1999-04-16 2002-09-17 Minerals Technologies Inc. Method and apparatus for continuous gas liquid reactions
KR100374785B1 (ko) * 2000-06-29 2003-03-04 학교법인 포항공과대학교 액상 산화 반응기
AU2002210518A1 (en) * 2000-10-19 2002-04-29 Dsm N.V. Aerobic fermentation method
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
US20040000474A1 (en) * 2002-02-22 2004-01-01 Catalytic Distillation Technologies Liquid-continuous column distillation
CA2496577A1 (fr) * 2002-08-28 2004-03-11 Intermune, Inc. Therapie de combinaison pour le traitement de troubles fibrosants
KR101168875B1 (ko) * 2004-03-04 2012-07-30 미쓰비시 가가꾸 가부시키가이샤 쿠멘 하이드로퍼옥사이드의 제조 방법
CN101022897A (zh) 2004-07-21 2007-08-22 皮特尼鲍斯股份有限公司 通过标准级邮件的识别降低投递路线上停站次数的系统和方法
US20070238899A9 (en) * 2004-09-02 2007-10-11 Robert Lin Optimized production of aromatic dicarboxylic acids
US7582793B2 (en) 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7897810B2 (en) * 2004-09-02 2011-03-01 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7507857B2 (en) 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
WO2006028817A2 (fr) * 2004-09-02 2006-03-16 Eastman Chemical Company Oxydation en phase liquide optimisee
US7586000B2 (en) * 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
PL1791800T3 (pl) * 2004-09-02 2018-04-30 Grupo Petrotemex, S.A. De C.V. Zoptymalizowane utlenianie w fazie ciekłej
US7495125B2 (en) * 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7371894B2 (en) * 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
CA2576341A1 (fr) * 2004-09-02 2006-03-23 Eastman Chemical Company Oxydation a phase liquide optimisee
US7399882B2 (en) * 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7381836B2 (en) * 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) * 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7910769B2 (en) * 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) * 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
CN101010278B (zh) * 2004-09-02 2011-02-23 伊士曼化工公司 优化的液相氧化
KR20070048251A (ko) * 2004-09-02 2007-05-08 이스트만 케미칼 컴파니 최적화된 액상 산화 방법
US7683210B2 (en) * 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) * 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7482482B2 (en) * 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7888530B2 (en) * 2004-09-02 2011-02-15 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7563926B2 (en) * 2004-09-02 2009-07-21 Eastman Chemical Company Optimized liquid-phase oxidation
US7572936B2 (en) 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7361784B2 (en) * 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) * 2005-03-08 2009-10-27 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
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
US7816556B2 (en) * 2006-03-01 2010-10-19 Eastman Chemical Company Polycarboxylic acid production system employing enhanced multistage 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
US7772424B2 (en) * 2006-03-01 2010-08-10 Eastman Chemical Company Polycarboxylic acid production system employing enhanced evaporative concentration downstream of oxidative digestion
US7897808B2 (en) * 2006-03-01 2011-03-01 Eastman Chemical Company Versatile oxidation byproduct purge process
US20070208194A1 (en) * 2006-03-01 2007-09-06 Woodruff Thomas E 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
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
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
WO2021069353A1 (fr) 2019-10-09 2021-04-15 Boehringer Ingelheim International Gmbh Bioréacteur ou fermenteur pour la culture de cellules ou de micro-organismes en suspension à l'échelle industrielle

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US3054814A (en) * 1959-09-24 1962-09-18 Standard Oil Co Oxidation of hydrocarbon synthesis liquids
DE1278434B (de) * 1964-09-04 1968-09-26 Vickers Zimmer Ag Verfahren und Vorrichtung zur Herstellung von Gemischen aus Cyclohexanol und Cylclohexanon
CH587915A5 (fr) * 1974-05-28 1977-05-13 Nestle Societe D Assistance Te
DE3001880A1 (de) * 1980-01-19 1981-07-23 Basf Ag, 6700 Ludwigshafen Verfahren zur sicheren zufuehrung von molekularem sauerstoff oder solchen enthaltenden gasen bei der oxidation von kohlenwasserstoffen
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DE4117592A1 (de) * 1991-05-29 1992-12-03 Huels Chemische Werke Ag Reaktor fuer phasenheterogene reaktionen
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Also Published As

Publication number Publication date
PT847800E (pt) 2002-02-28
EP0847800B1 (fr) 2001-08-22
KR19980063918A (ko) 1998-10-07
DE69706268D1 (de) 2001-09-27
BR9706246A (pt) 2000-08-08
MX9709967A (es) 1998-07-31
EP0847800A2 (fr) 1998-06-17
EP0847800A3 (fr) 1998-08-12
CA2224529A1 (fr) 1998-06-12
CN1195577A (zh) 1998-10-14
ES2162183T3 (es) 2001-12-16
JPH10330292A (ja) 1998-12-15
AR009658A1 (es) 2000-04-26
US5994567A (en) 1999-11-30
DE69706268T2 (de) 2002-05-23

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