ES2102422T3 - Aparato y metodo de transferencia de masas de autocirculacion continua y de varias zonas. - Google Patents

Aparato y metodo de transferencia de masas de autocirculacion continua y de varias zonas.

Info

Publication number
ES2102422T3
ES2102422T3 ES92105345T ES92105345T ES2102422T3 ES 2102422 T3 ES2102422 T3 ES 2102422T3 ES 92105345 T ES92105345 T ES 92105345T ES 92105345 T ES92105345 T ES 92105345T ES 2102422 T3 ES2102422 T3 ES 2102422T3
Authority
ES
Spain
Prior art keywords
mass transfer
liquid
transfer zone
gas
zone
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
ES92105345T
Other languages
English (en)
Inventor
Leslie C Hardison
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.)
Wheelabrator Clean Air Systems Inc
Original Assignee
Wheelabrator Clean Air Systems 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 Wheelabrator Clean Air Systems Inc filed Critical Wheelabrator Clean Air Systems Inc
Application granted granted Critical
Publication of ES2102422T3 publication Critical patent/ES2102422T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/72—Treatment of water, waste water, or sewage by oxidation
    • C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/48—Sulfur compounds
    • B01D53/52—Hydrogen sulfide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/75—Multi-step processes

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Hydrology & Water Resources (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Gas Separation By Absorption (AREA)
  • Treating Waste Gases (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Industrial Gases (AREA)
  • Automatic Analysis And Handling Materials Therefor (AREA)
  • Making Paper Articles (AREA)
  • Branching, Merging, And Special Transfer Between Conveyors (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

AUTOCIRCULACION CONTINUA, APARATO PARA LA TRANSFERENCIA DE MASA A MULTIPLES ZONAS Y METODO. UN APARATO Y METODO PARA PONER EN CONTACTO UN LIQUIDO CON GASES DIFERENTES, SECUENCIALMENTE EN ZONAS SEPARADAS DE TRANSFERENCIA DE MASA QUE SE ENCUENTRAN DENTRO DE UN SOLO RECIPIENTE, ESTANDO LAS ZONAS DE TRANSFERENCIA DE MASA CONECTADAS FUNCIONALMENTE EN COMUNICACION LIQUIDA ENTRE SI, QUE CONSISTE EN PONER EN ESTRECHO CONTACTO EL LIQUIDO CON UN PRIMER GAS DE TRABAJO EN FLUJO PARALELO EN UNA PRIMERA ZONA DE TRANSFERENCIA DE MASA PARA EFECTUAR LA TRANSFERENCIA DE MASA ENTRE EL PRIMER LIQUIDO Y EL GAS DE TRABAJO E INTRODUCIR EL LIQUIDO EN UNA SEGUNDA ZONA DE TRANSFERENCIA DE MASA CON UN SEGUNDO GAS, DISTINTO DEL PRIMER GAS, EN FLUJO PARALELO RESPECTO AL SEGUNDO LIQUIDO, EFECTUANDO ASI UNA TRANSFERENCIA DE MASA ENTRE EL SEGUNDO LIQUIDO Y EL SEGUNDO GAS. LA VELOCIDAD DE FLUJO DEL LIQUIDO DESDE DICHA PRIMERA ZONA DE TRANSFERENCIA DE MASA A LA SEGUNDA ZONA DE TRANSFERENCIA DE MASA Y LA RECIRCULACION A LA PRIMERA ZONA DE TRANSFERENCIA DE MASA DEPENDE DE LA DIFERENCIA DE DENSIDAD DE LOS CONTENIDOS EN LA PORCION DE FASE LIQUIDA DE CADA ZONA DE TRANSFERENCIA DE MASA Y UN LIQUIDO DESCENDENTE SIGUIENTE O UN CANAL DE FLUJO QUE LO CONECTA A LA SIGUIENTE ZONA DE TRANSFERENCIA DE MASA SECUENCIAL, DE MODO QUE DESPUES DE PASAR A TRAVES DE LA ULTIMA ZONA DE TRANSFERENCIA DE MASA, EL LIQUIDO RECIRCULA A LA PRIMERA ZONA DE TRANSFERENCIA DE MASA. EL APARATO Y EL METODO SON TOTALMENTE ADECUADOS PARA LLEVAR A CABO EL PROCESO DE EXTRACCION DEL SULFURO DE HIDROGENO DE LOS GASES MEDIANTE UN CATALIZADOR DE REDUCCION-OXIDACION LIQUIDO REGENERADO CON AIRE , COMO POR EJEMPLO UN HIERRO QUELATADO
ES92105345T 1991-04-08 1992-03-27 Aparato y metodo de transferencia de masas de autocirculacion continua y de varias zonas. Expired - Lifetime ES2102422T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US07/682,598 US5160714A (en) 1991-04-08 1991-04-08 Continuous autocirculation, multiple zone mass transfer apparatus and method

Publications (1)

Publication Number Publication Date
ES2102422T3 true ES2102422T3 (es) 1997-08-01

Family

ID=24740358

Family Applications (1)

Application Number Title Priority Date Filing Date
ES92105345T Expired - Lifetime ES2102422T3 (es) 1991-04-08 1992-03-27 Aparato y metodo de transferencia de masas de autocirculacion continua y de varias zonas.

Country Status (8)

Country Link
US (1) US5160714A (es)
EP (1) EP0508243B1 (es)
JP (1) JP2506597B2 (es)
AT (1) ATE152633T1 (es)
CA (1) CA2065549C (es)
DE (1) DE69219514T2 (es)
ES (1) ES2102422T3 (es)
GR (1) GR3024065T3 (es)

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US5545358A (en) * 1995-04-20 1996-08-13 Hallsten Corporation Tank cover structure with aeration distribution
US6158269A (en) * 1995-07-13 2000-12-12 Bayer Corporation Method and apparatus for aspirating and dispensing sample fluids
US5750881A (en) * 1995-07-13 1998-05-12 Chiron Diagnostics Corporation Method and apparatus for aspirating and dispensing sample fluids
US5641006A (en) * 1995-07-13 1997-06-24 Chiron Diagnostics Corporation Liquid supply apparatus and method of operation
US5766519A (en) * 1995-11-13 1998-06-16 Erickson; Donald C. Locally cocurrent globally crosscurrent pressure equalized absorber and process
US5698171A (en) * 1996-01-10 1997-12-16 Quaker Chemical Corporation Regenerative method for removing sulfides from gas streams
DE19629500C1 (de) * 1996-07-22 1998-04-16 Thermoselect Ag Multiwäscher und Verfahren zur Totalreinigung von Gasen
US5885538A (en) * 1997-07-02 1999-03-23 Quaker Chemical Corporation Method and composition for the regeneration of an aminal compound
US6270063B1 (en) * 1998-07-27 2001-08-07 Texas Instruments Incorporated Ozone diffuser for deionized water
EP1074295A1 (de) * 1999-08-04 2001-02-07 Sulzer Chemtech AG Umlaufreaktor für Fluide unterschiedlicher Dichte
US7491856B2 (en) 2007-06-27 2009-02-17 H R D Corporation Method of making alkylene glycols
US7749481B2 (en) * 2007-06-27 2010-07-06 H R D Corporation System and process for gas sweetening
US8304584B2 (en) 2007-06-27 2012-11-06 H R D Corporation Method of making alkylene glycols
JP5175077B2 (ja) * 2007-11-01 2013-04-03 新日鉄住金エンジニアリング株式会社 液相酸化湿式脱硫装置
JP5754877B2 (ja) * 2009-03-31 2015-07-29 三菱日立パワーシステムズ株式会社 酸化槽、海水処理装置及び海水脱硫システム
US7951353B1 (en) 2010-06-07 2011-05-31 Merichem Company Flow control method and apparatus for a continuous multiple zone mass transfer
US8815083B2 (en) 2012-11-29 2014-08-26 Merichem Company Treating sulfur containing hydrocarbons recovered from hydrocarbonaceous deposits
AU2014318458B2 (en) 2013-09-16 2018-02-01 Savannah River Nuclear Solutions, Llc Mass transfer apparatus and method for separation of gases
CN108911274A (zh) * 2018-09-03 2018-11-30 湖南先瑞环境技术有限公司 一种重金属反应器及包括该重金属反应器的重金属废水处理方法

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CH611255A5 (es) * 1976-06-18 1979-05-31 Bertrams Ag Hch
US2142406A (en) * 1934-12-27 1939-01-03 Ici Ltd Apparatus for the wet purification of gases
DE2001284A1 (de) * 1969-01-16 1970-11-19 Foster Wheeler Corp Beseitigung von Verunreinigungen durch Schwefelwasserstoff- und Schwefeldioxydgase
US3638708A (en) * 1969-06-11 1972-02-01 Marathon Engineering Inc Methods of multiple stage evaporation from heat sources other than steam
BE759284A (fr) * 1969-11-24 1971-05-24 Shell Int Research Procede et appareil pour la mise en contact d'un liquide avec des particules solides
JPS5136715B2 (es) * 1971-11-02 1976-10-09
GB1460029A (en) * 1972-12-21 1976-12-31 Perstorp Ab Continuous process for the production of phenolic urea and mela mine resins and apparatus therefor
US4009251A (en) * 1973-08-27 1977-02-22 Rhodia, Inc. Process for the removal of hydrogen sulfide from gaseous streams by catalytic oxidation of hydrogen sulfide to sulfur while inhibiting the formation of sulfur oxides
US3876537A (en) * 1973-10-31 1975-04-08 Industrial Resources Method of insolubilizing demineralizer and cooling tower blowdown wastes
US4083944A (en) * 1976-12-17 1978-04-11 Arthur G. Mckee & Company Regenerative process for flue gas desulfurization
JPS6051373B2 (ja) * 1977-09-02 1985-11-13 日本電気株式会社 連続式反応装置
US4482524A (en) * 1978-01-31 1984-11-13 Ari Technologies, Inc. Autocirculation apparatus
US4238462A (en) * 1978-01-31 1980-12-09 Air Resources, Inc. Autocirculation process and apparatus
EP0011517A3 (fr) * 1978-10-06 1980-07-23 Rhone-Poulenc Industries Procédé et appareillage pour l'élimination de l'hydrogène sulfuré des courants gazeux
DE2847443A1 (de) * 1978-11-02 1980-05-22 Blenke Heinz Verfahren und vorrichtung zur durchfuehrung (bio-)chemischer reaktionen und verfahrenstechnischer grundoperationen in fluiden systemen
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Also Published As

Publication number Publication date
JPH06170159A (ja) 1994-06-21
DE69219514D1 (de) 1997-06-12
GR3024065T3 (en) 1997-10-31
JP2506597B2 (ja) 1996-06-12
CA2065549C (en) 1999-05-04
ATE152633T1 (de) 1997-05-15
EP0508243A1 (en) 1992-10-14
US5160714A (en) 1992-11-03
EP0508243B1 (en) 1997-05-07
DE69219514T2 (de) 1997-10-09
CA2065549A1 (en) 1992-10-09

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