CO6351771A2 - Proceso para la producion de etileno de baja concentracion para usar como reactivo - Google Patents

Proceso para la producion de etileno de baja concentracion para usar como reactivo

Info

Publication number
CO6351771A2
CO6351771A2 CO10147585A CO10147585A CO6351771A2 CO 6351771 A2 CO6351771 A2 CO 6351771A2 CO 10147585 A CO10147585 A CO 10147585A CO 10147585 A CO10147585 A CO 10147585A CO 6351771 A2 CO6351771 A2 CO 6351771A2
Authority
CO
Colombia
Prior art keywords
fraction
ethylene
column
reagent
purified
Prior art date
Application number
CO10147585A
Other languages
English (en)
Inventor
Joachim Kotter
Hans-Dieter Winkler
Peter Mews
Michel Lempereur
Dominique Balthasart
Michel Strebelle
Original Assignee
Solvay
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 Solvay filed Critical Solvay
Publication of CO6351771A2 publication Critical patent/CO6351771A2/es

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
    • F25J3/0228—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 characterised by the separated product stream
    • F25J3/0238—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 characterised by the separated product stream separation of CnHm with 2 carbon atoms or more
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C11/00—Aliphatic unsaturated hydrocarbons
    • C07C11/02—Alkenes
    • C07C11/04—Ethylene
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
    • C07C4/04—Thermal processes
    • 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
    • F25J3/0204—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 characterised by the feed stream
    • F25J3/0219—Refinery gas, cracking gas, coke oven gas, gaseous mixtures containing aliphatic unsaturated CnHm or gaseous mixtures of undefined nature
    • 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
    • F25J3/0228—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 characterised by the separated product stream
    • F25J3/0252—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 characterised by the separated product stream separation of hydrogen
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/1048—Middle distillates
    • C10G2300/1059—Gasoil having a boiling range of about 330 - 427 °C
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1081—Alkanes
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20—C2-C4 olefins
    • 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
    • F25J2200/00—Processes or apparatus using separation by rectification
    • F25J2200/02—Processes or apparatus using separation by rectification in a single pressure main column system
    • 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
    • F25J2200/00—Processes or apparatus using separation by rectification
    • F25J2200/74—Refluxing the column with at least a part of the partially condensed overhead gas
    • 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
    • F25J2210/00—Processes characterised by the type or other details of the feed stream
    • F25J2210/12—Refinery or petrochemical off-gas
    • 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
    • F25J2215/00—Processes characterised by the type or other details of the product stream
    • F25J2215/62—Ethane or ethylene
    • 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
    • F25J2270/00—Refrigeration techniques used
    • F25J2270/02—Internal refrigeration with liquid vaporising loop
    • 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
    • Y02P30/00—Technologies relating to oil refining and petrochemical industry
    • Y02P30/40—Ethylene production

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Proceso para la producción de etileno para usar como reactivo a partir de una fuente de hidrocarburos de acuerdo con el cual se sigue el procedimiento de:a) someter a la fuente de hidrocarburos a un primer paso de craqueo, es decir, se lleva a cabo un paso de pirólisis en un horno de craqueo, para producir de esa manera una mezcla de productos de craqueo;b) someter a dicha mezcla de productos de craqueo a una sucesión de pasos de tratamiento, que incluyen un paso de compresión, que hace posible obtener una corriente de gas en bruto purificado;c) luego, enfriar la corriente de gas en bruto purificado hasta una temperatura a la cual condensan los hidrocarburos de 6 y más átomos de carbono de tal manera que puedan ser eliminados de la corriente de gas en bruto purificado;d) luego, suministrar la corriente de gas purificado que se obtiene como resultado a una columna de separación, donde se separa en una fracción que contiene hidrógeno, metano y etileno (fracción A) que se obtiene en la cabeza de la columna y se separa una fracción pesada (fracción C) que se obtiene en el fondo de la columna;e) suministrar una parte del reflujo de esta columna a un ciclo de refrigeración que permite obtener una fracción enriquecida en etileno (fracción B);f) suministrar por separado la fracción A y la fracción B al uso del etileno como reactivo.
CO10147585A 2008-06-03 2010-11-24 Proceso para la producion de etileno de baja concentracion para usar como reactivo CO6351771A2 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP08157514A EP2130811A1 (en) 2008-06-03 2008-06-03 Process for the production of low-concentration ethylene for chemical use

Publications (1)

Publication Number Publication Date
CO6351771A2 true CO6351771A2 (es) 2011-12-20

Family

ID=40278989

Family Applications (1)

Application Number Title Priority Date Filing Date
CO10147585A CO6351771A2 (es) 2008-06-03 2010-11-24 Proceso para la producion de etileno de baja concentracion para usar como reactivo

Country Status (15)

Country Link
US (1) US8173855B2 (es)
EP (2) EP2130811A1 (es)
JP (1) JP2011521995A (es)
KR (1) KR20110022614A (es)
CN (2) CN105001034A (es)
AR (1) AR073643A1 (es)
AU (1) AU2009253975A1 (es)
BR (1) BRPI0913217A2 (es)
CA (1) CA2724590A1 (es)
CO (1) CO6351771A2 (es)
EA (1) EA019902B1 (es)
MX (1) MX2010013000A (es)
PE (1) PE20100436A1 (es)
TW (1) TW201004921A (es)
WO (1) WO2009147076A2 (es)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2902784B1 (fr) 2006-06-23 2008-09-05 Solvay Procede de fabrication de 1,2-dichloroethane
FR2902786B1 (fr) 2006-06-26 2008-08-29 Solvay Procede de fabrication de 1,2-dichloroethane
FR2902787B1 (fr) 2006-06-26 2008-09-05 Solvay Procede de fabrication de 1,2-dichloroethane
FR2902785B1 (fr) 2006-06-26 2008-08-08 Solvay Procede de fabrication de 1,2-dichloroethane
WO2014048864A2 (en) 2012-09-28 2014-04-03 Solvay Sa Process for producing liquefied impure ethylene
CN104152173B (zh) * 2013-05-14 2016-01-13 中国石油天然气股份有限公司大庆石化分公司 一种乙烯装置的开工减排方法
EP3282212A1 (de) * 2016-08-12 2018-02-14 Linde Aktiengesellschaft Verfahren zur gewinnung eines überwiegend kohlenwasserstoffe mit zwei kohlenstoffatomen enthaltenden trennprodukts
US10365038B2 (en) * 2016-09-15 2019-07-30 Lummus Technology Inc. Process for the production of dilute ethylene
RU2670433C1 (ru) * 2017-12-29 2018-10-23 Общество с ограниченной ответственностью "Газ Хим Технолоджи" Газохимическое производство этилена и пропилена
US10858599B2 (en) 2018-08-22 2020-12-08 Exxonmobil Research And Engineering Company Manufacturing hydrocarbons
US10858600B2 (en) 2018-08-22 2020-12-08 Exxonmobil Research And Engineering Company Manufacturing a base stock
US10889769B2 (en) 2018-08-22 2021-01-12 Exxonmobil Research And Engineering Company Manufacturing a base stock from ethanol
WO2020041096A1 (en) 2018-08-22 2020-02-27 Exxonmobil Research And Engineering Company Manufacturing hydrocarbons
WO2020041084A1 (en) 2018-08-22 2020-02-27 Exxonmobil Research And Engineering Company Manufacturing a base stock from ethanol
US11015131B2 (en) 2018-08-22 2021-05-25 Exxonmobil Research And Engineering Company Manufacturing hydrocarbons

Family Cites Families (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2588323A (en) * 1949-09-03 1952-03-04 Lummus Co Production of ethylene
US2804488A (en) * 1954-12-27 1957-08-27 Phillips Petroleum Co Separation and recovery of ethylene
GB846679A (en) * 1958-06-02 1960-08-31 Exxon Research Engineering Co Ethylene production
AT260191B (de) 1965-05-08 1968-02-12 Bayer Ag Verfahren zur Hydrierung aller ungesättigter Verbindungen in C3 Kohlenwasserstoff Fraktionen
US3444696A (en) * 1967-02-10 1969-05-20 Stone & Webster Eng Corp Demethanization employing different temperature level refrigerants
US3485886A (en) * 1967-05-05 1969-12-23 Phillips Petroleum Co Production of high purity ethylene
US4743282A (en) * 1982-05-03 1988-05-10 Advanced Extraction Technologies, Inc. Selective processing of gases containing olefins by the mehra process
US4548706A (en) * 1983-01-26 1985-10-22 Standard Oil Company (Indiana) Thermal cracking of hydrocarbons
US4900347A (en) * 1989-04-05 1990-02-13 Mobil Corporation Cryogenic separation of gaseous mixtures
US5082481A (en) * 1990-04-10 1992-01-21 Lummus Crest, Inc. Membrane separation process for cracked gases
US5421167A (en) * 1994-04-01 1995-06-06 The M. W. Kellogg Company Enhanced olefin recovery method
US5453559A (en) * 1994-04-01 1995-09-26 The M. W. Kellogg Company Hybrid condensation-absorption olefin recovery
US5746066A (en) * 1996-09-17 1998-05-05 Manley; David B. Pre-fractionation of cracked gas or olefins fractionation by one or two mixed refrigerant loops and cooling water
DE19716092A1 (de) * 1997-04-17 1998-10-22 Linde Ag Verfahren zur Ethylenerzeugung aus einem Kohlenwasserstoffeinsatz
US6441263B1 (en) * 2000-07-07 2002-08-27 Chevrontexaco Corporation Ethylene manufacture by use of molecular redistribution on feedstock C3-5 components
US6405561B1 (en) * 2001-05-15 2002-06-18 Black & Veatch Pritchard, Inc. Gas separation process
DE10159615A1 (de) 2001-12-05 2003-06-12 Basf Ag Verfahren zur Herstellung von 1,2-Dichlorethan
US7294749B2 (en) * 2004-07-02 2007-11-13 Kellogg Brown & Root Llc Low pressure olefin recovery process
CN103396287B (zh) 2004-12-23 2015-10-07 索维公司 制造1,2-二氯乙烷的方法
AU2005318152B2 (en) 2004-12-23 2011-10-13 Solvay (Societe Anonyme) Process for the manufacture of 1,2-dichloroethane
BRPI0518650A2 (pt) 2004-12-23 2008-12-02 Solvay processos para a manufatura de 1, 2-dicloro-etano partindo de uma fonte de hidrocarbonetos, para a manufatura de cloreto de vinila, e de poli(cloreto de vinila)
JP2008525377A (ja) 2004-12-23 2008-07-17 ソルヴェイ（ソシエテ アノニム） １，２−ジクロロエタンの製造方法
JP2009502915A (ja) * 2005-07-28 2009-01-29 イネオス ユーエスエイ リミテッド ライアビリティ カンパニー 自己熱分解反応装置流出物からエチレンを回収する方法
FR2902784B1 (fr) 2006-06-23 2008-09-05 Solvay Procede de fabrication de 1,2-dichloroethane
FR2902785B1 (fr) 2006-06-26 2008-08-08 Solvay Procede de fabrication de 1,2-dichloroethane
FR2902787B1 (fr) 2006-06-26 2008-09-05 Solvay Procede de fabrication de 1,2-dichloroethane
FR2902786B1 (fr) 2006-06-26 2008-08-29 Solvay Procede de fabrication de 1,2-dichloroethane
US8256243B2 (en) * 2006-12-16 2012-09-04 Kellogg Brown & Root Llc Integrated olefin recovery process
US20100331587A1 (en) 2008-02-28 2010-12-30 Solvay (Societe Anonyme) Process for the manufacture of at least one ethylene derivative compound
EP2130814A1 (en) 2008-06-03 2009-12-09 SOLVAY (Société Anonyme) Process for the manufacture of at least one ethylene derivative compound
EP2130813A1 (en) 2008-06-03 2009-12-09 SOLVAY (Société Anonyme) Process for the manufacture of at least one ethylene derivative compound
EP2130810A1 (en) 2008-06-03 2009-12-09 SOLVAY (Société Anonyme) Process for the manufacture of 1,2-dichloroethane and of at least one ethylene derivative compound different from 1,2-dichloroethane

Also Published As

Publication number Publication date
WO2009147076A2 (en) 2009-12-10
EP2294037A2 (en) 2011-03-16
JP2011521995A (ja) 2011-07-28
TW201004921A (en) 2010-02-01
MX2010013000A (es) 2010-12-20
PE20100436A1 (es) 2010-07-04
CN105001034A (zh) 2015-10-28
EA201071391A1 (ru) 2011-06-30
US8173855B2 (en) 2012-05-08
EA019902B1 (ru) 2014-07-30
US20110077439A1 (en) 2011-03-31
CN102056873A (zh) 2011-05-11
AR073643A1 (es) 2010-11-24
KR20110022614A (ko) 2011-03-07
CA2724590A1 (en) 2009-12-10
BRPI0913217A2 (pt) 2016-07-26
WO2009147076A3 (en) 2010-03-04
EP2130811A1 (en) 2009-12-09
AU2009253975A1 (en) 2009-12-10

Similar Documents

Publication Publication Date Title
CO6351771A2 (es) Proceso para la producion de etileno de baja concentracion para usar como reactivo
RU2636317C2 (ru) Установка и способ производства этилена
MY157897A (en) Integrated ngl recovery in the production of liquefied natural gas
MY177598A (en) High efficiency processes for olefins, alkynes,and hydrogen co-production from light hydrocarbons such as methane
MY157791A (en) Liquefied natural gas production
NZ599333A (en) Hydrocarbon gas processing
MY142025A (en) Integrated ngl recovery and liquefied natural gas production
EA201001114A1 (ru) Способ многоступенчатого разделения с использованием мембран
ZA201003346B (en) Process for producing a purified synthesis gas stream
CL2008001443A1 (es) Proceso para la separacion de gas natural licuado que coprende su vaporizacion parcial, alimentacion a columna de fraccionamiento y extraccion de una corriente de vapor de destilacion, del cual se obtiene una fraccion volatil rica en metano y c2, y una fraccion liquida concentrada en hidrocarburos superiores
EA201071392A1 (ru) Способ получения 1,2-дихлорэтана и по меньшей мере одного соединения производного этилена, отличного от 1,2-дихлорэтана
MX2013014864A (es) Configuraciones y metodos para reajustar una instalacion de recuperacion de gas natural licuado.
RU2016127551A (ru) Способ разделения водородсодержащей углеводородной смеси, сепарационная секция и олефиновая установка
BR112012023999A2 (pt) processo para a preparação de uma corrente de alimentação a ser carregada em uma unidade de craqueamento a vapor para produção de etileno
MX2010009187A (es) Proceso para la fabricacion de por lo menos un compuesto derivado de etileno.
AR067187A1 (es) Procedimiento para separar hidrocarburos aromaticos de gas de hornos de coque
EA201071407A1 (ru) Способ получения по меньшей мере одного производного этилена
EA201391783A1 (ru) Способ получения углеводородной композиции
EA201270004A1 (ru) Переработка углеводородного газа
KR101971616B1 (ko) 약한 열 분해로부터 탄화수소의 분리 시퀀스
MY183059A (en) Natural gas treatment method for minimizing ethane loss
PE20151929A1 (es) Metodos para separar los gases de hidrocarburo
EA201891032A1 (ru) Возврат флегмы в колоннах для деметанирования
JO3074B1 (ar) عملية وجهاز لتعدين زيت من خليط غاز بخاري
WO2010128886A3 (ru) Способ получения углеводородов из газообразных продуктов плазменной переработки твёрдых отходов ( варианты)

Legal Events

Date Code Title Description
FC Application refused