BR9402432A - Sistema de colunas de destilação e método de retificação criogênica - Google Patents

Sistema de colunas de destilação e método de retificação criogênica

Info

Publication number
BR9402432A
BR9402432A BR9402432A BR9402432A BR9402432A BR 9402432 A BR9402432 A BR 9402432A BR 9402432 A BR9402432 A BR 9402432A BR 9402432 A BR9402432 A BR 9402432A BR 9402432 A BR9402432 A BR 9402432A
Authority
BR
Brazil
Prior art keywords
distillation column
column system
rectification method
cryogenic rectification
cryogenic
Prior art date
Application number
BR9402432A
Other languages
English (en)
Inventor
Michael James Lockett
Dante Patrick Bonaquist
Richard Amory Victor
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=22289291&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=BR9402432(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Praxair Technology Inc filed Critical Praxair Technology Inc
Publication of BR9402432A publication Critical patent/BR9402432A/pt

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04406—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a dual pressure main column system
    • F25J3/04412—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a dual pressure main column system in a classical double column flowsheet, i.e. with thermal coupling by a main reboiler-condenser in the bottom of low pressure respectively top of high pressure column
    • 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
    • B01D3/141—Fractional distillation or use of a fractionation or rectification column where at least one distillation column contains at least one dividing wall
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04642—Recovering noble gases from air
    • F25J3/04648—Recovering noble gases from air argon
    • F25J3/04654—Producing crude argon in a crude argon column
    • F25J3/04666—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system
    • F25J3/04672—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser
    • F25J3/04678—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser cooled by oxygen enriched liquid from high pressure column bottoms
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04642—Recovering noble gases from air
    • F25J3/04648—Recovering noble gases from air argon
    • F25J3/04654—Producing crude argon in a crude argon column
    • F25J3/04666—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system
    • F25J3/04672—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser
    • F25J3/04703—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser being arranged in more than one vessel
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04763—Start-up or control of the process; Details of the apparatus used
    • F25J3/04866—Construction and layout of air fractionation equipments, e.g. valves, machines
    • F25J3/04896—Details of columns, e.g. internals, inlet/outlet devices
    • F25J3/04927—Liquid or gas distribution devices
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04763—Start-up or control of the process; Details of the apparatus used
    • F25J3/04866—Construction and layout of air fractionation equipments, e.g. valves, machines
    • F25J3/04896—Details of columns, e.g. internals, inlet/outlet devices
    • F25J3/04933—Partitioning walls or sheets
    • F25J3/04939—Vertical, e.g. dividing wall columns
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S62/00—Refrigeration
    • Y10S62/902—Apparatus
    • Y10S62/905—Column

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
BR9402432A 1993-08-05 1994-06-15 Sistema de colunas de destilação e método de retificação criogênica BR9402432A (pt)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US08/102,326 US5339648A (en) 1993-08-05 1993-08-05 Distillation system with partitioned column

Publications (1)

Publication Number Publication Date
BR9402432A true BR9402432A (pt) 1995-03-14

Family

ID=22289291

Family Applications (1)

Application Number Title Priority Date Filing Date
BR9402432A BR9402432A (pt) 1993-08-05 1994-06-15 Sistema de colunas de destilação e método de retificação criogênica

Country Status (9)

Country Link
US (1) US5339648A (pt)
EP (1) EP0638778B1 (pt)
JP (1) JPH0760003A (pt)
KR (1) KR950005352A (pt)
CN (1) CN1099472A (pt)
BR (1) BR9402432A (pt)
CA (1) CA2125893A1 (pt)
DE (1) DE69402274T2 (pt)
ES (1) ES2099510T3 (pt)

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DE4418488A1 (de) * 1994-05-27 1995-11-30 Basf Ag Verfahren und Vorrichtung zur destillativen Trennung von Stoffgemischen
US5486318A (en) * 1994-12-29 1996-01-23 The Boc Group, Inc. Liquid-vapor contact column
US5755933A (en) * 1995-07-24 1998-05-26 The M. W. Kellogg Company Partitioned distillation column
DE19617210A1 (de) * 1996-04-30 1997-11-06 Basf Ag Trennwandkolonne zur kontinuierlichen destillativen Zerlegung von Mehrstoffgemischen
US5669236A (en) * 1996-08-05 1997-09-23 Praxair Technology, Inc. Cryogenic rectification system for producing low purity oxygen and high purity oxygen
US5902460A (en) * 1996-09-23 1999-05-11 Gerhold; Bruce W. Multi-stage fractional distillation process and apparatus
US5836174A (en) * 1997-05-30 1998-11-17 Praxair Technology, Inc. Cryogenic rectification system for producing multi-purity oxygen
US5958191A (en) * 1997-09-11 1999-09-28 Kvaerner Canada, Inc. Column for the separation of a volatile liquid from a mixture with another liquid of lower volatility
US20030047438A1 (en) * 1998-05-06 2003-03-13 Sumitomo Heavy Industries, Ltd. Distillation apparatus and distillation method
CN1108845C (zh) * 1998-05-06 2003-05-21 住友重机械工业株式会社 蒸馏装置及蒸馏方法
US5896755A (en) * 1998-07-10 1999-04-27 Praxair Technology, Inc. Cryogenic rectification system with modular cold boxes
US5946942A (en) * 1998-08-05 1999-09-07 Praxair Technology, Inc. Annular column for cryogenic rectification
DE19849651C2 (de) * 1998-10-29 2003-01-16 Krupp Uhde Gmbh Rektifizierkolonne für die Extraktivdestillation von eng- oder azeotrop siedenden Gemischen
US6077985A (en) * 1999-03-10 2000-06-20 Kellogg Brown & Root, Inc. Integrated deethanizer/ethylene fractionation column
DE19914966A1 (de) * 1999-04-01 2000-10-05 Basf Ag Verfahren zur kontinuierlich betriebenen destillativen Abtrennung eines höherschmelzenden Stoffes
US6173586B1 (en) 1999-08-31 2001-01-16 Praxair Technology, Inc. Cryogenic rectification system for producing very high purity oxygen
US6250106B1 (en) * 1999-12-13 2001-06-26 Air Products And Chemicals, Inc. Process for separation of multicomponent fluids using a multizone distallation column
US6240744B1 (en) * 1999-12-13 2001-06-05 Air Products And Chemicals, Inc. Process for distillation of multicomponent fluid and production of an argon-enriched stream from a cryogenic air separation process
DE10002806A1 (de) * 2000-01-24 2001-07-26 Basf Ag Multishaft-Kolonne
US6347533B1 (en) * 2000-03-04 2002-02-19 Peter Tung Hydraulically balanced fully thermally coupled system
DE10028866A1 (de) * 2000-06-10 2001-12-20 Messer Ags Gmbh Verfahren und Vorrichtung zur Gewinnung von Argon
US6930206B1 (en) 2001-07-05 2005-08-16 Catalytic Distillation Technologies Process and apparatus for catalytic distillations
AU2003229590A1 (en) * 2002-04-12 2003-10-27 Linde Aktiengesellschaft Method for extracting argon by low-temperature air separation
ATE512946T1 (de) * 2002-06-11 2011-07-15 Catalytic Distillation Tech Verfahren und vorrichtung für katalytische destillierungen
DE10341614A1 (de) 2003-09-10 2005-04-28 Basf Ag Verfahren zur Herstellung von Xylylendiamin (XDA)
DE102004022734A1 (de) * 2004-05-07 2005-12-01 Vinnolit Gmbh & Co. Kg Verfahren zur Destillation von Produktgemischen
US7357378B2 (en) * 2004-10-18 2008-04-15 Air Prodcuts And Chemicals, Inc. Divided wall exchange column
US9139503B2 (en) * 2007-09-10 2015-09-22 Lummus Technology Inc. Method for the production of dimethyl ether
CN101244982B (zh) * 2008-01-31 2011-03-23 中国石油大学(华东) 一种乙酸甲酯的水解分离装置及其工艺
FR2929532B1 (fr) * 2008-04-07 2010-12-31 Air Liquide Colonne a garnissage d'echange de chaleur et/ou matiere
US8480860B2 (en) * 2008-10-22 2013-07-09 Air Products And Chemicals, Inc. Divided wall columns for smaller sized plants
JP5027173B2 (ja) * 2009-03-06 2012-09-19 大陽日酸株式会社 アルゴン製造方法およびその装置
WO2011143215A2 (en) 2010-05-10 2011-11-17 Catalytic Distillation Technologies Production of jet and other heavy fuels from isobutanol
CN102040542B (zh) * 2010-10-28 2013-08-14 河北工业大学 利用隔板塔共沸精馏从废水中回收乙腈的工艺
CN102068829B (zh) * 2010-11-24 2012-12-26 天津大学 一种利用隔板反应精馏设备进行二氯二氢硅和四氯化硅的反歧化反应的方法
US20130019634A1 (en) * 2011-07-18 2013-01-24 Henry Edward Howard Air separation method and apparatus
EP2822683B1 (en) 2012-03-06 2016-04-27 Air Products and Chemicals, Inc. Structured packing
FR3017698B1 (fr) * 2014-02-14 2019-03-29 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Colonne de separation d'air par distillation cryogenique, appareil de separation d'air comportant une telle colonne et procede de fabrication d'une telle colonne
FR3018200B1 (fr) * 2014-03-10 2017-12-01 Ifp Energies Now Contacteur pour colonne d'echange constitue de compartiments de garnissage vrac
JP6204231B2 (ja) * 2014-03-11 2017-09-27 大陽日酸株式会社 空気液化分離装置及び方法
CN104027994B (zh) * 2014-05-30 2017-10-20 英尼奥斯欧洲股份公司 粗乙腈与丙烯腈的分离
US10578357B2 (en) 2017-08-25 2020-03-03 Praxair Technology, Inc. Annular divided wall column with ring shaped collectors and distributers for an air separation unit
US10684071B2 (en) 2017-08-25 2020-06-16 Praxair Technology, Inc. Annular divided wall column for an air separation unit
EP3614084A1 (de) 2018-08-22 2020-02-26 Linde Aktiengesellschaft Verfahren und anlage zur tieftemperaturzerlegung von luft
US20250115537A1 (en) 2022-01-19 2025-04-10 Exxonmobil Chemical Patents Inc. Compositions Containing Tri-Cyclopentadiene and Processes for Making Same
CN114923313B (zh) * 2022-05-17 2024-02-09 陕西聚能新创煤化科技有限公司 粗氩精制液氩系统及其精制工艺
WO2025244981A1 (en) 2024-05-20 2025-11-27 ExxonMobil Technology and Engineering Company Processes for making exo-dicyclopentadiene and tricyclopentadiene

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US5265428A (en) * 1990-10-05 1993-11-30 Exxon Production Research Company Bubble cap tray for melting solids and method for using same

Also Published As

Publication number Publication date
EP0638778A1 (en) 1995-02-15
DE69402274T2 (de) 1997-09-04
CN1099472A (zh) 1995-03-01
KR950005352A (ko) 1995-03-20
EP0638778B1 (en) 1997-03-26
US5339648A (en) 1994-08-23
JPH0760003A (ja) 1995-03-07
CA2125893A1 (en) 1995-02-06
ES2099510T3 (es) 1997-05-16
DE69402274D1 (de) 1997-04-30

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