ES2122956T3 - Columna de proceso. - Google Patents

Columna de proceso.

Info

Publication number
ES2122956T3
ES2122956T3 ES90302258T ES90302258T ES2122956T3 ES 2122956 T3 ES2122956 T3 ES 2122956T3 ES 90302258 T ES90302258 T ES 90302258T ES 90302258 T ES90302258 T ES 90302258T ES 2122956 T3 ES2122956 T3 ES 2122956T3
Authority
ES
Spain
Prior art keywords
tray
zone
steam
liquid contact
down pipe
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
ES90302258T
Other languages
English (en)
Inventor
Michael J Binkley
John T Thorngren
Jorge A Bonilla
Gary W Gage
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.)
Koch Cyprus Ltd
Original Assignee
Koch Cyprus 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
Application filed by Koch Cyprus Ltd filed Critical Koch Cyprus Ltd
Application granted granted Critical
Publication of ES2122956T3 publication Critical patent/ES2122956T3/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
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14—Fractional distillation or use of a fractionation or rectification column
    • B01D3/16—Fractionating columns in which vapour bubbles through liquid
    • B01D3/22—Fractionating columns in which vapour bubbles through liquid with horizontal sieve plates or grids; Construction of sieve plates or grids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14—Fractional distillation or use of a fractionation or rectification column
    • B01D3/16—Fractionating columns in which vapour bubbles through liquid
    • B01D3/18—Fractionating columns in which vapour bubbles through liquid with horizontal bubble plates
    • B01D3/20—Bubble caps; Risers for vapour; Discharge pipes for liquid

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

UN CONJUNTO DE TUBO DE DESCENSO Y BANDEJA PARA TORRES DE CONTACTO DE VAPOR-LIQUIDO. LA ZONA DE LA BANDEJA DEBAJO DE UN TUBO DE DESCENSO SUPERIOR ESTA CONSTRUIDA CON UNA ZONA LEVANTADA, PERFORADA PARA MEJORAR LA EFICIENCIA DE LAS TRANSFERENCIAS DE MASA. LA ZONA LEVANTADA REDUCE PRESION DE FLUIDO PARA FACILITAR EL ASCENSO DE VAPOR A TRAVES DE LA MISMA. UNA SERIE DE PERSIANAS DIRIGE SELECTIVAMENTE EL FLUJO DE VAPOR ASCENDENTE A DENTRO DE LA ZONA DE LIQUIDO DEBAJO DEL TUBO DE DESCENSO PARA GENERAR UN CONTACTO DE VAPOR-LIQUIDO MAS EFICIENTE Y REDUCIDA REPETICION DEL MEZCLADO A TRAVES DE LA BANDEJA.
ES90302258T 1989-03-08 1990-03-02 Columna de proceso. Expired - Lifetime ES2122956T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US07/320,420 US4956127A (en) 1989-03-08 1989-03-08 Downcomer-tray assembly and method

Publications (1)

Publication Number Publication Date
ES2122956T3 true ES2122956T3 (es) 1999-01-01

Family

ID=23246353

Family Applications (1)

Application Number Title Priority Date Filing Date
ES90302258T Expired - Lifetime ES2122956T3 (es) 1989-03-08 1990-03-02 Columna de proceso.

Country Status (11)

Country Link
US (1) US4956127A (es)
EP (1) EP0386961B1 (es)
JP (1) JPH0661403B2 (es)
KR (1) KR0137762B1 (es)
CN (1) CN1033423C (es)
AR (1) AR244099A1 (es)
AU (1) AU638231B2 (es)
BR (1) BR9001086A (es)
CA (1) CA1327305C (es)
DE (1) DE69032706T2 (es)
ES (1) ES2122956T3 (es)

Families Citing this family (61)

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US5120474A (en) * 1989-03-08 1992-06-09 Glitsch, Inc. Valve-tray assembly
US5164125A (en) * 1989-03-08 1992-11-17 Glitsch, Inc. Method and apparatus for downcomer-tray operation
US5277847A (en) * 1989-03-08 1994-01-11 Glitsch, Inc. Method and apparatus for catalyst-downcomer-tray operation
US5106544A (en) * 1990-01-31 1992-04-21 Glitsch, Inc. Method of and apparatus for vapor distribution
US5080836A (en) * 1990-11-27 1992-01-14 Glitsch, Inc. Tower packing with small and large louvers
US5057250A (en) * 1990-11-27 1991-10-15 Glitsch, Inc. Tower packing with small louvers
US5185106A (en) * 1990-11-27 1993-02-09 Glitsch, Inc. Tower packing with small louvers and mixing method
CA2035701C (en) * 1991-02-05 1999-01-19 Karl T. Chuang Active liquid distributor containing, packed column
US5192465A (en) * 1991-02-05 1993-03-09 Glitsch, Inc. Method of and apparatus for liquid distribution
US5118449A (en) * 1991-05-13 1992-06-02 Glitsch, Inc. Method of and apparatus for cartridge tray sealing
US5192466A (en) * 1991-10-09 1993-03-09 Glitsch, Inc. Method of and apparatus for flow promotion
US5601797A (en) * 1992-08-10 1997-02-11 Glitsch, Inc. Liquid-phase catalyst-assembly for chemical process tower
US5213719A (en) * 1992-09-28 1993-05-25 Chuang Karl T Gas-liquid contacting device
US5454989A (en) * 1994-03-23 1995-10-03 Nutter; Dale E. Vapor-liquid contact apparatus
US5516465A (en) * 1993-08-04 1996-05-14 Koch Engineering Company, Inc. Method and apparatus for vapor distribution in mass transfer and heat exchange columns
US5605654A (en) * 1993-08-04 1997-02-25 Koch Engineering Company, Inc. Method and apparatus to improve vapor distribution in mass transfer and heat exchange columns
US5632933A (en) * 1993-08-04 1997-05-27 Koch Engineering Company, Inc. Method and apparatus using guide vanes for vapor distribution in mass transfer and heat exchange columns
GB2321417B (en) * 1994-03-23 1998-10-21 Nutter Dale E Vapour-liquid contact apparatus
US5480595A (en) * 1994-04-28 1996-01-02 Koch Engineering Chemical, Inc. Vapor-liquid contact tray and downcomer assembly and method employing same
US5632935A (en) * 1994-04-28 1997-05-27 Koch Engineering Company, Inc. Vapor-liquid contact tray and downcomer assembly and method employing same
JP2715059B2 (ja) * 1994-05-06 1998-02-16 韓国電力公社 排煙と脱硫を行なう方法およびその装置
US5453222A (en) 1994-09-15 1995-09-26 Glitsch, Inc. Contact tray apparatus and method
CN1068235C (zh) * 1994-10-07 2001-07-11 环球油品公司 高汽容量复式降液管分馏塔盘装置
US5547617A (en) * 1995-03-31 1996-08-20 Glitsch, Inc. Apparatus for increasing effective active area
AU694850B2 (en) * 1995-03-31 1998-07-30 Koch (Cyprus) Limited Multi-downcomer high performance tray assembly
US5618473A (en) * 1995-05-09 1997-04-08 Norton Chemical Process Products Corporation Fractionation trays
US5788894A (en) * 1996-04-05 1998-08-04 Koch Engineering Company, Inc. High capacity vapor-liquid contact tray
US5895608A (en) * 1996-10-30 1999-04-20 Koch Enterprises, Inc. Downcomer for chemical process tower and method of forming the same
JP3926563B2 (ja) * 1997-11-19 2007-06-06 エクソンモービル オイル コーポレイション 二次羽根を備えた蒸気／液体接触サイクロン
CN1055253C (zh) * 1998-06-11 2000-08-09 华东理工大学 一种液体停留时间均布的塔盘
US6250611B1 (en) 1999-10-07 2001-06-26 Sulzer Chemtech Usa, Inc. Vapor-liquid contact apparatus
US6575438B2 (en) 2001-06-13 2003-06-10 Sulzer Chemtech Usa, Inc. Stepped downcomer apparatus and vapor-liquid contact apparatus with same
US7770873B2 (en) * 2003-02-06 2010-08-10 Sulzer Chemtech Ag Tray apparatus, column with same and method of assembling and using
ES2305830T3 (es) * 2003-08-13 2008-11-01 Shell Internationale Research Maatschappij B.V. Bandeja de contacto gas-liquido.
US7270316B2 (en) * 2004-06-09 2007-09-18 Joseph Michael Burch Distillation column tray configuration
US7204477B2 (en) * 2005-06-01 2007-04-17 Uop Llc Parallel flow fractionation tray
US8540218B2 (en) 2007-04-27 2013-09-24 Gtc Technology Us Llc Fluid dispersion unit assembly and method
US8070142B2 (en) * 2008-01-24 2011-12-06 Amt International, Inc. Downcomer distributor
US8517354B1 (en) 2008-03-20 2013-08-27 Gtc Technology Us Llc Fluid dispersion unit with directional component vector
US8517352B1 (en) 2008-04-04 2013-08-27 Gtc Technology Us Llc Liquid distributor
US9463397B2 (en) 2008-04-04 2016-10-11 Gtc Technology Us Llc System and method for liquid distribution
US8678357B2 (en) 2010-05-17 2014-03-25 Gtc Technology Us, Llc Fluid contactor-diffuser tray assembly
US8353980B2 (en) * 2008-12-05 2013-01-15 Marsulex Environmental Technologies Corporation Flue gas scrubbing apparatus and process
US8480062B2 (en) * 2009-05-15 2013-07-09 Gtc Technology Us, Llc Activated hinge-joint
US9072986B2 (en) 2011-02-23 2015-07-07 Gtc Technology Us Llc Method and apparatus for securing fractionation trays
US9597650B2 (en) 2011-04-18 2017-03-21 Gtc Technology Us Llc System for improved reactant mixing and distribution
US9079121B2 (en) * 2011-12-02 2015-07-14 Celanese International Corporation Distillation column having enlarged downcomers and method of downcomer enlargement
CN103239883B (zh) * 2012-02-08 2015-10-28 中国石油天然气股份有限公司 以等停留时间法设计多溢流塔板的方法
CN103432764B (zh) * 2013-08-05 2015-05-13 北京泽华化学工程有限公司 多降液管塔盘和具有其的板式塔
CN106457058B (zh) * 2014-01-31 2019-06-21 Lat水务有限公司 具有破碎板的逆流液化气蒸发和冷凝设备
CN104907769A (zh) * 2015-05-23 2015-09-16 嘉兴市中达金属制品有限公司 一种塔盘加工工艺
US10258936B2 (en) 2015-07-08 2019-04-16 Koch-Glitsch, Lp Contact tray for a mass transfer column
BR112018016529B1 (pt) * 2016-02-18 2023-04-25 Koch-Glitsch, Lp Sistema de suporte de parede cordal para bandejas de fluxo cruzado em uma coluna de transferência de massa e método envolvendo o mesmo
USD816188S1 (en) 2016-06-07 2018-04-24 Koch-Glitsch, Lp Tray valve cover
USD816189S1 (en) 2016-06-07 2018-04-24 Koch-Glitsch, Lp Tray valve
CN107720758A (zh) * 2017-11-13 2018-02-23 浙江工业大学上虞研究院有限公司 化工用生产系统
CN107673360A (zh) * 2017-11-13 2018-02-09 浙江工业大学上虞研究院有限公司 用于制备三氯氢硅的化工设备
CN107854859B (zh) * 2017-11-17 2023-06-27 洪湖市兴达石化设备制造有限公司 多用途降液结构
WO2020031077A1 (en) * 2018-08-06 2020-02-13 Koch-Glitsch, Lp Multi-pass contact tray for a mass transfer column comprising fixed and movable valves and method involving same
US11148069B2 (en) 2019-12-09 2021-10-19 Uop Llc Multiple downcomer trays
US11738284B2 (en) 2021-04-16 2023-08-29 Uop Llc Distillation trays

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US2693949A (en) * 1950-10-19 1954-11-09 Koch Eng Co Inc Apparatus for contacting gases and liquids
US2757915A (en) * 1951-08-23 1956-08-07 Koch Eng Co Inc Gas-liquid contact apparatus
US2762692A (en) * 1953-03-04 1956-09-11 Exxon Research Engineering Co Apparatus for solid-liquid contacting
US3282576A (en) * 1962-09-06 1966-11-01 Union Carbide Corp Apparatus for improved liquidvapor contact
BE674013A (es) * 1965-01-22
GB1143772A (es) * 1965-03-15
US3959419A (en) * 1973-09-06 1976-05-25 Fritz W. Glitsch & Sons, Inc. Vapor-liquid contact method
SU510247A1 (ru) * 1974-03-20 1976-04-15 Предприятие П/Я Р-6273 Тепло-массообменна тарелка
FR2267812A1 (en) * 1974-04-19 1975-11-14 Vicarb Sa Sieve plate for vapour-liq. contacting - constructed of slotted or perforated graphite
SU602203A1 (ru) * 1975-05-26 1978-04-15 Центральное конструкторское бюро нефтеаппаратуры Тарелка дл тепломассообменных аппаратов
US4499035A (en) * 1977-03-17 1985-02-12 Union Carbide Corporation Gas-liquid contacting tray with improved inlet bubbling means
JPS5527045A (en) * 1978-08-15 1980-02-26 Mitsubishi Heavy Ind Ltd Plate structure in gas liquid contact equipment
US4374000A (en) * 1981-02-02 1983-02-15 Cosden Technology, Inc. Method for controlling the formation of polymer accumulations during distillation of a vinylaromatic monomer
SU997706A1 (ru) * 1981-08-07 1983-02-23 Казахский Химико-Технологический Институт Массообменна тарелка
CA1211364A (en) * 1982-04-15 1986-09-16 Jeremy B. Bentham Apparatus for contacting a liquid with a gas
US4601788A (en) * 1982-07-12 1986-07-22 Shell Oil Company Apparatus for fractionation reboiling
CA1197172A (en) * 1982-11-24 1985-11-26 Karl T. Chuang Gas-liquid contacting apparatus
JPS5995903A (ja) * 1982-11-24 1984-06-02 Nippon Kayaku Co Ltd バツフル・トレイ塔
US4597916A (en) * 1983-06-21 1986-07-01 Glitsch, Inc. Method of and apparatus for intermediate lamella vapor liquid contact
US4604247A (en) * 1983-06-21 1986-08-05 Glitsch, Inc. Tower packing material and method
GB8406634D0 (en) * 1984-03-14 1984-04-18 Shell Int Research Gas/liquid contacting apparatus
GB8413336D0 (en) * 1984-05-24 1984-06-27 Shell Int Research Gas/liquid contacting apparatus

Also Published As

Publication number Publication date
EP0386961B1 (en) 1998-10-21
AR244099A1 (es) 1993-10-29
AU638231B2 (en) 1993-06-24
KR900014025A (ko) 1990-10-22
DE69032706T2 (de) 1999-03-11
US4956127A (en) 1990-09-11
EP0386961A3 (en) 1990-11-07
AU5064390A (en) 1990-09-13
KR0137762B1 (ko) 1998-04-27
CA1327305C (en) 1994-03-01
CN1033423C (zh) 1996-12-04
CN1045357A (zh) 1990-09-19
BR9001086A (pt) 1991-02-26
DE69032706D1 (de) 1998-11-26
JPH02277501A (ja) 1990-11-14
EP0386961A2 (en) 1990-09-12
JPH0661403B2 (ja) 1994-08-17

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