ES2093927T3 - Bandeja de fraccionamiento con tubo de descenso tabicado con flujo paralelo. - Google Patents

Bandeja de fraccionamiento con tubo de descenso tabicado con flujo paralelo.

Info

Publication number
ES2093927T3
ES2093927T3 ES93304057T ES93304057T ES2093927T3 ES 2093927 T3 ES2093927 T3 ES 2093927T3 ES 93304057 T ES93304057 T ES 93304057T ES 93304057 T ES93304057 T ES 93304057T ES 2093927 T3 ES2093927 T3 ES 2093927T3
Authority
ES
Spain
Prior art keywords
downloaded
tube
parallel flow
bucket
liquid flow
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
ES93304057T
Other languages
English (en)
Inventor
Daniel R Monkelbaan
Michael J Resetarits
Robert J Miller
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.)
Honeywell UOP LLC
Original Assignee
UOP LLC
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 UOP LLC filed Critical UOP LLC
Application granted granted Critical
Publication of ES2093927T3 publication Critical patent/ES2093927T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14Fractional distillation or use of a fractionation or rectification column
    • B01D3/16Fractionating columns in which vapour bubbles through liquid
    • B01D3/18Fractionating columns in which vapour bubbles through liquid with horizontal bubble plates
    • B01D3/20Bubble caps; Risers for vapour; Discharge pipes for liquid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14Fractional distillation or use of a fractionation or rectification column
    • B01D3/16Fractionating columns in which vapour bubbles through liquid
    • B01D3/22Fractionating columns in which vapour bubbles through liquid with horizontal sieve plates or grids; Construction of sieve plates or grids

Landscapes

  • Chemical Kinetics & Catalysis (AREA)
  • Chemical & Material Sciences (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Branch Pipes, Bends, And The Like (AREA)
  • Other Air-Conditioning Systems (AREA)
  • Particle Accelerators (AREA)
  • Farming Of Fish And Shellfish (AREA)
  • Feeding And Watering For Cattle Raising And Animal Husbandry (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Vessels And Coating Films For Discharge Lamps (AREA)
  • Treating Waste Gases (AREA)
  • Bathtub Accessories (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Extraction Or Liquid Replacement (AREA)

Abstract

LA EFICIENCIA DE TUBOS DE DESCENSO MULTIPLES DEL TIPO CUBETAS DE FRACCIONAMIENTO SE AUMENTA MEDIANTE EL SUMINISTRO DE PARES DE DEFLECTORES (3) INCLINADOS DESVIADORES DEL LIQUIDO SOBRE CADA TUBO DE DESCENSO (10) CONECTANDO LAS SALIDAS Y LAS ENTRADAS DE LOS TUBOS DE DESCENSO VERTICALMENTE ADYACENTES PARA PROPORCIONAR POR ESTA RAZON UN CAMINO DE FLUJO DE LIQUIDO CIRCULAR RELATIVO AL MOVIMIENTO DEL LIQUIDO SOBRE CADA CUBETA Y PARALELO AL FLUJO DEL LIQUIDO SOBRE UNA BASE DE CUBETA POR CUBETA QUE ACTUA PARA INCREMENTAR LA LONGITUD DE UN CAMINO DEL FLUJO DEL LIQUIDO Y PRODUCIR EL CASO LEWIS II QUE APUNTA AL AUMENTO DE LA EFICIENCIA DEL PLATO.
ES93304057T 1992-04-02 1993-05-24 Bandeja de fraccionamiento con tubo de descenso tabicado con flujo paralelo. Expired - Lifetime ES2093927T3 (es)

Applications Claiming Priority (8)

Application Number Priority Date Filing Date Title
US07/862,472 US5223183A (en) 1992-04-02 1992-04-02 Baffled downcomer fractionation tray
CA002096787A CA2096787A1 (en) 1992-04-02 1993-05-21 Parallel flow baffled downcomer fractionation tray
EP93304057A EP0626185B1 (en) 1992-04-02 1993-05-24 Parallel flow baffled downcomer fractionation tray
AU39808/93A AU659735B2 (en) 1992-04-02 1993-05-25 Parallel flow baffled downcomer fractionation tray
ZA933642A ZA933642B (en) 1992-04-02 1993-05-25 Parallel flow baffled downcomer fractionation tray
NO931891A NO180255C (no) 1992-04-02 1993-05-25 Fraksjoneringsbunn for kontakt mellom damp og væske
CN93108736A CN1037747C (zh) 1992-04-02 1993-05-26 平行流带挡板降液管精馏塔板
JP5126835A JPH0829201B2 (ja) 1992-04-02 1993-05-28 並行流阻止下降管分別トレイ

Publications (1)

Publication Number Publication Date
ES2093927T3 true ES2093927T3 (es) 1997-01-01

Family

ID=27570060

Family Applications (1)

Application Number Title Priority Date Filing Date
ES93304057T Expired - Lifetime ES2093927T3 (es) 1992-04-02 1993-05-24 Bandeja de fraccionamiento con tubo de descenso tabicado con flujo paralelo.

Country Status (12)

Country Link
US (1) US5223183A (es)
EP (1) EP0626185B1 (es)
JP (1) JPH0829201B2 (es)
CN (1) CN1037747C (es)
AT (1) ATE144908T1 (es)
AU (1) AU659735B2 (es)
CA (1) CA2096787A1 (es)
DE (1) DE69305840T2 (es)
DK (1) DK0626185T3 (es)
ES (1) ES2093927T3 (es)
NO (1) NO180255C (es)
ZA (1) ZA933642B (es)

Families Citing this family (39)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5318732A (en) * 1992-12-29 1994-06-07 Uop Capacity-enhanced multiple downcomer fractionation trays
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
US6116583A (en) * 1999-03-31 2000-09-12 Uop Llc Nestable fractionation tray antipenetration pans
BR0108415B1 (pt) * 2000-02-16 2010-06-15 bandeja de contato gás-lìquido com múltiplos tubos de descida, e, coluna de contato gás-lìquido.
US6460834B2 (en) * 2000-02-16 2002-10-08 Shell Oil Company Gas/liquid contact tray
AU2001231751A1 (en) * 2000-02-16 2001-08-27 Shell Internationale Research Maatschappij B.V. Gas-liquid tray
US6588735B2 (en) 2000-02-16 2003-07-08 Shell Oil Company Gas-liquid tray
US6494440B2 (en) * 2000-02-16 2002-12-17 Shell Oil Company Gas-liquid contacting tray
US6911652B2 (en) * 2000-03-22 2005-06-28 Jonathan A. Walkenstein Low light imaging device
US6390454B1 (en) * 2000-06-02 2002-05-21 Uop Llc Multiple downcomer fractionation trays with liquid distribution devices on ends of downcomers
US6479620B1 (en) * 2001-06-01 2002-11-12 E. I. Du Pont De Nemours And Company Process for converting caprolactam to nylon 6
US6736378B2 (en) * 2001-06-18 2004-05-18 Koch-Glitsch, Lp Contact tray having tray supported downcomers
ATE530236T1 (de) * 2003-04-07 2011-11-15 Koch Glitsch Lp Kombinierte flüssigkeitssammler und mischer für stoffaustauschkolonne
US7510173B2 (en) 2003-12-22 2009-03-31 Shell-Oil Company Gas-liquid contacting tray
US7234691B2 (en) * 2005-05-20 2007-06-26 Air Products And Chemicals, Inc. Radial-crossflow distillation trays for divided wall column applications
US7204477B2 (en) * 2005-06-01 2007-04-17 Uop Llc Parallel flow fractionation tray
FR2909894B1 (fr) 2006-12-14 2010-12-17 Inst Francais Du Petrole Systeme deflecteur pour plateaux de colonnes
US8074972B2 (en) * 2008-06-18 2011-12-13 Uop Llc Device for gas-liquid contacting
US8246016B2 (en) * 2008-07-18 2012-08-21 Uop Llc Downcomer for a gas-liquid contacting device
US8235362B2 (en) * 2009-03-31 2012-08-07 Uop Llc Fluid distribution to parallel flow vapor-liquid contacting trays
US8268049B2 (en) 2010-03-31 2012-09-18 Uop Llc Vapor-liquid contacting apparatuses having a secondary absorption zone with vortex contacting stages
US9199206B2 (en) 2010-05-11 2015-12-01 Sulzer Chemtech Ag Contact tray for a mass transfer column
US8944419B2 (en) * 2010-05-11 2015-02-03 Sulzer Chemtech Ag Contact tray for a mass transfer column
CN101905089B (zh) * 2010-06-09 2012-02-15 石家庄工大化工设备有限公司 一种液体并流复合塔
US8608833B2 (en) 2010-06-09 2013-12-17 Uop Llc Selective absorption of gas components in co-current contacting apparatuses
US8944418B2 (en) * 2011-05-16 2015-02-03 Koch-Glitsch, Lp Use of downcomer beam to support adjacent cross flow trays within a mass transfer column and process involving same
US8833742B2 (en) 2011-09-09 2014-09-16 Uop Llc Co-current vapor-liquid contacting apparatuses for offshore processes
KR101987169B1 (ko) 2012-12-17 2019-06-10 엘지이노텍 주식회사 모터
EP3049173B1 (de) * 2013-09-25 2018-01-03 Linde Aktiengesellschaft Verfahren zum reinigen eines spaltgasstroms in einer ölwaschkolonne
US10005004B2 (en) 2013-09-25 2018-06-26 Linde Aktiengesellschaft Oil scrubbing column
MX2018000232A (es) 2015-07-08 2018-03-08 Koch Glitsch Lp Bandeja de valvula de contacto para una columna de transferencia de masa.
US10989471B2 (en) 2015-10-30 2021-04-27 Praxair Technology, Inc. Multiple pass, parallel flow downcomer tray for a mass transfer column
US10012436B2 (en) 2015-10-30 2018-07-03 Praxair Technology, Inc. Multiple pass, parallel flow downcomer tray for a mass transfer column
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
CN108452649A (zh) * 2017-07-10 2018-08-28 山东海丰能源科技有限公司 一种脱碳塔
EP3628385A1 (en) * 2018-09-28 2020-04-01 Casale Sa A perforated-tray column and a method of revamping the same
CN114849264B (zh) * 2022-05-09 2024-03-01 湖北云图石化工程有限公司 一种化工生产用高效节能精馏塔

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3417975A (en) * 1964-12-01 1968-12-24 Union Carbide Corp Apparatus for liquid-gas contacting tray
US3410540A (en) * 1964-11-09 1968-11-12 Union Carbide Corp Vapor-liquid contact system and method
US3434701A (en) * 1966-08-15 1969-03-25 Phillips Petroleum Co Vapor-liquid contacting apparatus
US3658306A (en) * 1970-07-23 1972-04-25 Universal Oil Prod Co Apparatus for contacting a liquid with a vapor
FR2102927A5 (en) * 1970-08-31 1972-04-07 Speichim Overflow for mass transfer column tray
SU405558A1 (es) * 1971-07-26 1973-11-05
US4499035A (en) * 1977-03-17 1985-02-12 Union Carbide Corporation Gas-liquid contacting tray with improved inlet bubbling means
CA1110538A (en) * 1977-08-16 1981-10-13 Walter Bruckert Outlet means for vapor liquid contacting tray
US4159291A (en) * 1977-08-16 1979-06-26 Union Carbide Corporation Outlet means for vapor-liquid contacting tray
GB2053720A (en) * 1979-06-08 1981-02-11 Davy Int Oil & Chemi Distillation tray
US4582569A (en) * 1981-01-22 1986-04-15 Distillation Technology Limited Mass transfer apparatus
CA1211364A (en) * 1982-04-15 1986-09-16 Jeremy B. Bentham Apparatus for contacting a liquid with a gas
GB8406634D0 (en) * 1984-03-14 1984-04-18 Shell Int Research Gas/liquid contacting apparatus
US5098615A (en) * 1990-10-19 1992-03-24 Uop Multiple-downcomer contacting tray with fluid directing baffles

Also Published As

Publication number Publication date
US5223183A (en) 1993-06-29
NO931891L (no) 1994-11-28
EP0626185A1 (en) 1994-11-30
CN1037747C (zh) 1998-03-18
JPH0829201B2 (ja) 1996-03-27
DE69305840D1 (de) 1996-12-12
ZA933642B (en) 1993-12-21
NO931891D0 (no) 1993-05-25
CA2096787A1 (en) 1994-11-22
NO180255B (no) 1996-12-09
EP0626185B1 (en) 1996-11-06
CN1095639A (zh) 1994-11-30
DE69305840T2 (de) 1997-03-06
AU659735B2 (en) 1995-05-25
NO180255C (no) 1997-03-19
AU3980893A (en) 1994-12-15
ATE144908T1 (de) 1996-11-15
JPH06343801A (ja) 1994-12-20
DK0626185T3 (da) 1996-11-25

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