AR073643A1 - Proceso para la produccion de etileno de baja concentracion para usar como reactivo - Google Patents

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

Info

Publication number
AR073643A1
AR073643A1 ARP090101996A ARP090101996A AR073643A1 AR 073643 A1 AR073643 A1 AR 073643A1 AR P090101996 A ARP090101996 A AR P090101996A AR P090101996 A ARP090101996 A AR P090101996A AR 073643 A1 AR073643 A1 AR 073643A1
Authority
AR
Argentina
Prior art keywords
fraction
ethylene
reagent
column
stream
Prior art date
Application number
ARP090101996A
Other languages
English (en)
Inventor
Michel Strebelle
Dominique Balthasart
Michel Lempereur
Joachim Kotter
Hans-Dieter Winkler
Peter Mews
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 AR073643A1 publication Critical patent/AR073643A1/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

Abstract

Proceso para la produccion 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 pirolisis 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 sucesion de pasos de tratamiento, que incluyen un paso de compresion, 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 o más átomos de carbono de tal manera que pueden ser eliminados de la corriente de gas en bruto purificado; d) luego, suministrar la corriente de gas purificado que se obtiene como resultado de una columna de separacion, donde se separa en una fraccion que contiene hidrogeno, metano y etileno (fraccion A) que se obtiene en la cabeza de la columna y se separa una fraccion pesada (fraccion C) que se obtiene en el fondo de la columna; e) suministrar una parte del reflujo de esta columna a un ciclo de refrigeracion que permite obtener una fraccion enriquecida en etileno (fraccion B); f) suministrar por separado la fraccion A y la fraccion B al uso del etileno como reactivo.
ARP090101996A 2008-06-03 2009-06-03 Proceso para la produccion de etileno de baja concentracion para usar como reactivo AR073643A1 (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
AR073643A1 true AR073643A1 (es) 2010-11-24

Family

ID=40278989

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP090101996A AR073643A1 (es) 2008-06-03 2009-06-03 Proceso para la produccion 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) CN102056873A (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)

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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
US10815439B2 (en) 2018-08-22 2020-10-27 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
US10889769B2 (en) 2018-08-22 2021-01-12 Exxonmobil Research And Engineering Company Manufacturing a base stock from ethanol
US10858600B2 (en) 2018-08-22 2020-12-08 Exxonmobil Research And Engineering Company Manufacturing a base stock
US10858599B2 (en) 2018-08-22 2020-12-08 Exxonmobil Research And Engineering Company Manufacturing hydrocarbons
US11015131B2 (en) 2018-08-22 2021-05-25 Exxonmobil Research And Engineering Company Manufacturing hydrocarbons

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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
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EP2130814A1 (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
EP2130813A1 (en) 2008-06-03 2009-12-09 SOLVAY (Société Anonyme) Process for the manufacture of at least one ethylene derivative compound

Also Published As

Publication number Publication date
CN105001034A (zh) 2015-10-28
US20110077439A1 (en) 2011-03-31
AU2009253975A1 (en) 2009-12-10
EA201071391A1 (ru) 2011-06-30
MX2010013000A (es) 2010-12-20
JP2011521995A (ja) 2011-07-28
WO2009147076A2 (en) 2009-12-10
PE20100436A1 (es) 2010-07-04
EP2294037A2 (en) 2011-03-16
EA019902B1 (ru) 2014-07-30
KR20110022614A (ko) 2011-03-07
CA2724590A1 (en) 2009-12-10
TW201004921A (en) 2010-02-01
BRPI0913217A2 (pt) 2016-07-26
EP2130811A1 (en) 2009-12-09
CO6351771A2 (es) 2011-12-20
WO2009147076A3 (en) 2010-03-04
US8173855B2 (en) 2012-05-08
CN102056873A (zh) 2011-05-11

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