MX2009005330A - Reactor separador no reflujante. - Google Patents

Reactor separador no reflujante.

Info

Publication number
MX2009005330A
MX2009005330A MX2009005330A MX2009005330A MX2009005330A MX 2009005330 A MX2009005330 A MX 2009005330A MX 2009005330 A MX2009005330 A MX 2009005330A MX 2009005330 A MX2009005330 A MX 2009005330A MX 2009005330 A MX2009005330 A MX 2009005330A
Authority
MX
Mexico
Prior art keywords
reaction system
distillative
stream
uppermost
section
Prior art date
Application number
MX2009005330A
Other languages
English (en)
Inventor
Stephen Craig Arnold
Original Assignee
Lummus 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
Application filed by Lummus Technology Inc filed Critical Lummus Technology Inc
Publication of MX2009005330A publication Critical patent/MX2009005330A/es

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00—Purification; Separation; Use of additives
    • C07C7/04—Purification; Separation; Use of additives by distillation
    • 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
    • B01D3/009—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in combination with chemical reactions
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G35/00—Reforming naphtha
    • C10G35/04—Catalytic reforming
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/44—Hydrogenation of the aromatic hydrocarbons
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/002—Apparatus for fixed bed hydrotreatment processes
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G7/00—Distillation of hydrocarbon oils
    • 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Water Supply & Treatment (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Se proporciona un proceso para tratar catalíticamente una corriente de alimentación que contiene al menos un compuesto orgánico, el cual consiste en disponer de un sistema de reacción destilativa que tenga una sección de reacción colocada en una parte alta del sistema de reacción destilativa y un re-hervidor y/o sección de arrastre de gas para vaporizar al menos una parte de una corriente residual y regresar la parte vaporizada de la corriente residual a una parte residual del sistema de reacción destilativa, introducir una corriente de alimentación orgánica al sistema de reacción destilativa por debajo de la sección de reacción más alta introduciendo opcionalmente una corriente de alimentación reactante gaseosa en el sistema de reacción destilativa por debajo de la sección de reacción más alta, y retirar una corriente de productos de cabeza a partir de una parte del sistema de reacción destilativa por encima de la sección más alta sin reflujo considerable o recirculación de la corriente de productos de cabeza o la alimentación de alguna otra corriente de líquidos que podría recircular los productos deseados u otros compuestos cualesquiera que no se desee que sean reflujados, a la sección de reacción más alta.
MX2009005330A 2006-11-20 2007-11-19 Reactor separador no reflujante. MX2009005330A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US11/602,020 US20080116053A1 (en) 2006-11-20 2006-11-20 Non-refluxing reactor stripper
PCT/US2007/024120 WO2008063584A2 (en) 2006-11-20 2007-11-19 Non-refluxing reactor stripper

Publications (1)

Publication Number Publication Date
MX2009005330A true MX2009005330A (es) 2009-08-20

Family

ID=39415823

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2009005330A MX2009005330A (es) 2006-11-20 2007-11-19 Reactor separador no reflujante.

Country Status (14)

Country Link
US (1) US20080116053A1 (es)
EP (1) EP2097359B1 (es)
JP (1) JP2010510351A (es)
KR (1) KR20090093995A (es)
CN (1) CN101578250A (es)
AR (1) AR063870A1 (es)
AT (1) ATE522486T1 (es)
BR (1) BRPI0719034A2 (es)
CA (1) CA2669928A1 (es)
CL (1) CL2007003293A1 (es)
MX (1) MX2009005330A (es)
TW (1) TW200835543A (es)
WO (1) WO2008063584A2 (es)
ZA (1) ZA200904265B (es)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7828962B2 (en) * 2008-11-20 2010-11-09 Merichem Company Apparatus for treating a waste stream
WO2012042614A1 (ja) * 2010-09-29 2012-04-05 トヨタ自動車株式会社 コロイダルダンパ
CN103429710B (zh) * 2011-01-19 2015-11-25 利亚特莱克什科技有限公司 在蒸馏塔内的三个催化反应区上的粗汽油异构化
CZ307108B6 (cs) * 2013-09-06 2018-01-17 Vysoké Učení Technické V Brně Multifunkční poloprovozní jednotka pro snižování polutantů z odpadního plynu
CN109173310A (zh) * 2018-08-29 2019-01-11 张家港市科华化工装备制造有限公司 甲缩醛精馏塔

Family Cites Families (28)

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IT1129809B (it) * 1979-03-26 1986-06-11 Ugine Kuhlmann Composizione catalitica per la conversione di idrocarburi e procedimento per la disidratazione di acidi perfluoroalcansolfonici destinati a fare parte bella composizione
US5026459A (en) * 1988-03-21 1991-06-25 Institut Francais Du Petrole Apparatus for reactive distillation
US4847430A (en) * 1988-03-21 1989-07-11 Institut Francais Du Petrole Process for manufacturing a tertiary alkyl ether by reactive distillation
EP0693957B1 (en) * 1993-02-17 1998-01-21 China Petro-Chemical Corporation A multiple stage suspended reactive stripping process and apparatus
JPH0734073A (ja) * 1993-07-23 1995-02-03 Jgc Corp 石油類の水素化処理方法及び水素化処理装置
US5449501A (en) * 1994-03-29 1995-09-12 Uop Apparatus and process for catalytic distillation
US5461178A (en) * 1994-04-28 1995-10-24 Mobil Oil Corporation Catalytic stripping of hydrocarbon liquid
JP3464079B2 (ja) * 1995-06-28 2003-11-05 新日本石油株式会社 ベンゼン含有炭化水素油の水素化異性化方法
FR2737132B1 (fr) * 1995-07-24 1997-09-19 Inst Francais Du Petrole Procede et dispositif de distillation reactive avec distribution particuliere des phases liquide et vapeur
FR2743079B1 (fr) * 1995-12-27 1998-02-06 Inst Francais Du Petrole Procede et dispositif d'hydrogenation selective par distillation catalytique comportant une zone reactionnelle a co-courant ascendant liquide-gaz
FR2743080B1 (fr) * 1995-12-27 1998-02-06 Inst Francais Du Petrole Procede de reduction selective de la teneur en benzene et en composes insatures legers d'une coupe d'hydrocarbures
FR2744458B1 (fr) * 1996-02-05 1998-03-27 Inst Francais Du Petrole Procede d'isomerisation de paraffines par distillation reactive
US5847251A (en) * 1996-02-12 1998-12-08 Catalytic Distillation Technologies Multibed transalkylator and process
US5830345A (en) * 1996-02-28 1998-11-03 Chinese Petroleum Corporation Process of producing a debenzenated and isomerized gasoline blending stock by using a dual functional catalyst
US5837130A (en) * 1996-10-22 1998-11-17 Catalytic Distillation Technologies Catalytic distillation refining
US6045762A (en) * 1997-01-22 2000-04-04 Governors Of The University Of Alberta Apparatus for catalytic distillation
US5847249A (en) * 1997-07-28 1998-12-08 Catalytic Distillation Technologies Apparatus and process for catalytic distillations
FR2782322B1 (fr) * 1998-08-17 2000-10-06 Inst Francais Du Petrole Procede de conversion d'hydrocarbures par traitement dans une zone de distillation comprenant le soutirage lateral d'une coupe d'hydrocarbures, associee a une zone reactionnelle et son utilisation en hydrogenation du benzene
US6083378A (en) * 1998-09-10 2000-07-04 Catalytic Distillation Technologies Process for the simultaneous treatment and fractionation of light naphtha hydrocarbon streams
US6410804B1 (en) * 1999-12-21 2002-06-25 Exxon Mobil Oil Corporation Production of phenol using reactive distillation
US6906229B1 (en) * 2000-02-29 2005-06-14 Exxonmobil Chemical Patents, Inc. Process for hydrolyzing di-isopropyl ether to isopropyl alcohol by catalytic distillation using a solid acid catalyst
US6776859B1 (en) * 2000-11-27 2004-08-17 Saturn Electronics & Engineering, Inc. Anisotropic bonding system and method using dynamic feedback
EP1357167A1 (en) * 2002-04-18 2003-10-29 Haldor Topsoe A/S Process for production of high quality gasoline with low aromatic content
US7186873B2 (en) * 2002-06-19 2007-03-06 Exxonmobil Chemical Patents Inc. Manufacture of xylenes by reactive distillation of reformate
DE10243444A1 (de) * 2002-09-19 2004-03-25 Oxeno Olefinchemie Gmbh Verfahren zur Oligomerisierung von Butenen unter Rückgewinnung von linearen Butenen aus n-Butan-haltigen Restströmen
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US20060270885A1 (en) * 2005-05-31 2006-11-30 Boyer Christopher C Normal heptane isomerization

Also Published As

Publication number Publication date
AR063870A1 (es) 2009-02-25
WO2008063584A2 (en) 2008-05-29
ZA200904265B (en) 2010-06-30
CA2669928A1 (en) 2008-05-29
ATE522486T1 (de) 2011-09-15
US20080116053A1 (en) 2008-05-22
WO2008063584A3 (en) 2009-01-08
KR20090093995A (ko) 2009-09-02
EP2097359A2 (en) 2009-09-09
TW200835543A (en) 2008-09-01
EP2097359B1 (en) 2011-08-31
CL2007003293A1 (es) 2008-05-23
BRPI0719034A2 (pt) 2013-11-05
CN101578250A (zh) 2009-11-11
JP2010510351A (ja) 2010-04-02

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