AR020500A1 - Columna de burbujeo y su utilizacion - Google Patents

Columna de burbujeo y su utilizacion

Info

Publication number
AR020500A1
AR020500A1 ARP990104772A ARP990104772A AR020500A1 AR 020500 A1 AR020500 A1 AR 020500A1 AR P990104772 A ARP990104772 A AR P990104772A AR P990104772 A ARP990104772 A AR P990104772A AR 020500 A1 AR020500 A1 AR 020500A1
Authority
AR
Argentina
Prior art keywords
gas
liquid
column
reactions
bubble column
Prior art date
Application number
ARP990104772A
Other languages
English (en)
Original Assignee
Degussa Huls Aktiengesellscahft
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=7881934&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=AR020500(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Degussa Huls Aktiengesellscahft filed Critical Degussa Huls Aktiengesellscahft
Publication of AR020500A1 publication Critical patent/AR020500A1/es

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B15/00—Peroxides; Peroxyhydrates; Peroxyacids or salts thereof; Superoxides; Ozonides
    • C01B15/01—Hydrogen peroxide
    • C01B15/022—Preparation from organic compounds
    • C01B15/023—Preparation from organic compounds by the alkyl-anthraquinone process
    • 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
    • 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
    • B01J19/0053—Details of the reactor
    • B01J19/006—Baffles
    • 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
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1836—Heating and cooling 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/44—Fluidisation grids
    • 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
    • B01J2204/00—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices
    • B01J2204/002—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices the feeding side being of particular interest
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/0015—Plates; Cylinders
    • 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
    • B01J2219/00761—Details of the reactor
    • B01J2219/00763—Baffles
    • B01J2219/00765—Baffles attached to the reactor wall

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Extraction Or Liquid Replacement (AREA)

Abstract

La invencion se refiere a una columna de burbujeo con fondos perforados, el rendimiento espacio-tiempo de reacciones gas-líquido puede aumentarseesencialmente si los fondos perforados (5) tienen una distribucion de agujeros esencialmente uniforme,si endo la superficie de seccion transversalde los agujeros individuales de 0,003 a 3 mm2, especialmente de 0,05 a 0,5 mm2, y la superficie abierta del fondo de 2 a 20%, especialmente de 3 a 7%. Lacolumna de burbujeo puede emplearse para llevar acabo r eacciones gas-líquido, tales como reacciones de oxidacion con aire, siendo conducidos el gas y ellíquido unidireccionalmente a través de la columna.
ARP990104772A 1998-09-23 1999-09-22 Columna de burbujeo y su utilizacion AR020500A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19843573A DE19843573A1 (de) 1998-09-23 1998-09-23 Blasensäule und deren Verwendung

Publications (1)

Publication Number Publication Date
AR020500A1 true AR020500A1 (es) 2002-05-15

Family

ID=7881934

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP990104772A AR020500A1 (es) 1998-09-23 1999-09-22 Columna de burbujeo y su utilizacion

Country Status (19)

Country Link
US (1) US6375921B1 (es)
EP (1) EP1123255B1 (es)
JP (1) JP2002526251A (es)
KR (1) KR100640673B1 (es)
AR (1) AR020500A1 (es)
AT (1) ATE227245T1 (es)
AU (1) AU757094B2 (es)
BR (1) BR9913913A (es)
CA (1) CA2345092C (es)
DE (2) DE19843573A1 (es)
ES (1) ES2182567T3 (es)
ID (1) ID28653A (es)
IL (1) IL142158A (es)
NZ (1) NZ510362A (es)
PL (1) PL194793B1 (es)
PT (1) PT1123255E (es)
TR (1) TR200100850T2 (es)
WO (1) WO2000017098A1 (es)
ZA (1) ZA200102386B (es)

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DE10114982A1 (de) * 2001-03-27 2002-10-02 Degussa Verfahren zur Herstellung von Wasserstoffperoxid
DE10156988A1 (de) * 2001-11-21 2003-05-28 Basf Ag Kolonne mit Dual-Flow-Böden
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US7572936B2 (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
US7568361B2 (en) * 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7563926B2 (en) * 2004-09-02 2009-07-21 Eastman Chemical Company Optimized liquid-phase oxidation
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
US7482482B2 (en) * 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7495125B2 (en) * 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7608733B2 (en) * 2004-09-02 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
KR20070048251A (ko) * 2004-09-02 2007-05-08 이스트만 케미칼 컴파니 최적화된 액상 산화 방법
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7910769B2 (en) * 2004-09-02 2011-03-22 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
US7582793B2 (en) 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) * 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) * 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7361784B2 (en) * 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) * 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) * 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7683210B2 (en) * 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7586000B2 (en) * 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) 2004-09-02 2010-04-06 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
US20060116531A1 (en) * 2004-11-29 2006-06-01 Wonders Alan G Modeling of liquid-phase oxidation
CN101094717A (zh) * 2004-12-31 2007-12-26 国际壳牌研究有限公司 用于固/液/气反应的反应器
AU2011242141B2 (en) * 2005-03-17 2012-05-03 Sasol Technology (Proprietary) Limited Method of operating a three-phase slurry reactor
DE112006000626T5 (de) * 2005-03-17 2008-04-10 Sasol Technology (Proprietary) Ltd. Verfahren zum Betreiben eines Drei-Phasen-Schlammreaktors
RU2391132C2 (ru) * 2005-03-17 2010-06-10 Сэсол Текнолоджи (Проприетери) Лимитед Реактор с псевдоожиженным слоем, трехфазный шламовый реактор и способы обеспечения их функционирования (варианты)
US7884232B2 (en) * 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
ATE540000T1 (de) * 2005-08-31 2012-01-15 Fmc Corp Autoxidative herstellung von wasserstoffperoxid mittels oxidation in einem mikroreaktor
AR057787A1 (es) * 2005-08-31 2007-12-19 Fmc Corp Produccion por auto-oxidacion de peroxido de hidrogeno a traves de hidrogenacion en un microrreactor
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
US7645892B2 (en) * 2006-05-02 2010-01-12 Lyondell Chemical Technology, L.P. Reaction system
US8674145B2 (en) * 2007-11-01 2014-03-18 Illa International, L.L.C. Method for acceleration of cumene oxidation
CN101462927B (zh) * 2007-12-20 2012-04-04 财团法人工业技术研究院 多重区间反应装置
KR101603751B1 (ko) * 2010-02-18 2016-03-16 삼성전자주식회사 명령어 병렬 처리 컴퓨터를 위한 명령어 압축 장치 및 방법
JP2015020940A (ja) * 2013-07-22 2015-02-02 国立大学法人静岡大学 過酸化水素合成方法
CN104418308B (zh) * 2013-08-22 2016-06-22 中国石油化工股份有限公司 一种蒽醌法生产双氧水的氢化工艺
CN104418307B (zh) * 2013-08-22 2016-06-22 中国石油化工股份有限公司 一种蒽醌法生产双氧水多段氢化工艺
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US20160264511A1 (en) * 2015-03-13 2016-09-15 Grupo Petrotemex, S.A. De C.V. Bubble column reactor based digester and method for its use
US11185818B2 (en) * 2016-07-21 2021-11-30 Biogasclean A/S Process and apparatus for removal of hydrogen sulphide from a gas
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FR3086288A1 (fr) * 2018-09-21 2020-03-27 IFP Energies Nouvelles Procede d'oligomerisation d'ethylene dans un reacteur gaz/liquide compartimente
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Also Published As

Publication number Publication date
TR200100850T2 (tr) 2001-08-21
AU757094B2 (en) 2003-01-30
CA2345092A1 (en) 2000-03-30
PL346750A1 (en) 2002-02-25
IL142158A (en) 2004-09-27
JP2002526251A (ja) 2002-08-20
ATE227245T1 (de) 2002-11-15
BR9913913A (pt) 2001-06-19
AU6080799A (en) 2000-04-10
IL142158A0 (en) 2002-03-10
EP1123255B1 (de) 2002-11-06
PL194793B1 (pl) 2007-07-31
DE59903356D1 (de) 2002-12-12
KR100640673B1 (ko) 2006-11-02
ID28653A (id) 2001-06-21
PT1123255E (pt) 2003-03-31
CA2345092C (en) 2009-08-18
NZ510362A (en) 2003-08-29
US6375921B1 (en) 2002-04-23
WO2000017098A1 (de) 2000-03-30
EP1123255A1 (de) 2001-08-16
ZA200102386B (en) 2002-06-24
DE19843573A1 (de) 2000-03-30
ES2182567T3 (es) 2003-03-01
KR20010079901A (ko) 2001-08-22

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