AR079302A1 - PROCESS FOR THE MANUFACTURE OF AT LEAST A COMPOUND DERIVED FROM ETHYLENE - Google Patents

PROCESS FOR THE MANUFACTURE OF AT LEAST A COMPOUND DERIVED FROM ETHYLENE

Info

Publication number
AR079302A1
AR079302A1 ARP100104481A ARP100104481A AR079302A1 AR 079302 A1 AR079302 A1 AR 079302A1 AR P100104481 A ARP100104481 A AR P100104481A AR P100104481 A ARP100104481 A AR P100104481A AR 079302 A1 AR079302 A1 AR 079302A1
Authority
AR
Argentina
Prior art keywords
fraction
ethylene
called
enriched
manufacture
Prior art date
Application number
ARP100104481A
Other languages
Spanish (es)
Inventor
Andre Petitjean
Massimo Giansante
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 AR079302A1 publication Critical patent/AR079302A1/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00—Preparation of halogenated hydrocarbons
    • C07C17/38—Separation; Purification; Stabilisation; Use of additives
    • C07C17/389—Separation; Purification; Stabilisation; Use of additives by adsorption on solids
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00—Preparation of halogenated hydrocarbons
    • C07C17/013—Preparation of halogenated hydrocarbons by addition of halogens
    • C07C17/02—Preparation of halogenated hydrocarbons by addition of halogens to unsaturated hydrocarbons
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00—Preparation of halogenated hydrocarbons
    • C07C17/093—Preparation of halogenated hydrocarbons by replacement by halogens
    • C07C17/15—Preparation of halogenated hydrocarbons by replacement by halogens with oxygen as auxiliary reagent, e.g. oxychlorination
    • C07C17/152—Preparation of halogenated hydrocarbons by replacement by halogens with oxygen as auxiliary reagent, e.g. oxychlorination of hydrocarbons
    • C07C17/156—Preparation of halogenated hydrocarbons by replacement by halogens with oxygen as auxiliary reagent, e.g. oxychlorination of hydrocarbons of unsaturated hydrocarbons
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00—Preparation of halogenated hydrocarbons
    • C07C17/38—Separation; Purification; Stabilisation; Use of additives
    • C07C17/383—Separation; Purification; Stabilisation; Use of additives by distillation
    • 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
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/582—Recycling of unreacted starting or intermediate materials

Abstract

Proceso para la fabricacion de por lo menos un compuesto derivado de etileno a partir de una fuente de hidrocarburos en el cual se siguen los pasos de: a) someter a la fuente de hidrocarburos, que opcionalmente contiene la fraccion E1 reciclada del paso (d), a un craqueo simplificado que produce una mezcla de productos que contiene etileno y otros constituyentes; b) someter a dicha mezcla de productos a un primer paso de separacion S1 que consiste en separar a dichos productos que contienen etileno y otros constituyentes para dar una fraccion que contiene a los compuestos que son más livianos que el etileno y parte del etileno que se denomina fraccion F1 y una fraccion F2; c) enviar a la fraccion F1 a una unidad de recuperacion de etileno en la cual se la separa para dar una fraccion enriquecida en etileno que se denomina la fraccion E1 y una fraccion enriquecida en los compuestos que son más livianos que el etileno que se denomina fraccion liviana; d) reciclar la fraccion E1 al paso a) o llevarla a la fabricacion de por lo menos un compuesto derivado de etileno; e) someter a la fraccion F2 a un segundo paso de separacion S2 que consiste en separar a la fraccion F2 para dar una fraccion enriquecida en etileno que se denomina la fraccion E2 o dos fracciones enriquecidas con etileno que se denominan las fracciones E2a y E2b, y una fraccion enriquecida en etano e hidrocarburos que contienen por lo menos 3 átomos de carbono que se denomina la fraccion pesada; f) llevar luego a la fraccion E2 o a las fracciones E2a y E2b a la fabricacion de por lo menos un compuesto derivado de etileno.Process for the manufacture of at least one ethylene-derived compound from a hydrocarbon source in which the steps of: a) submitting to the hydrocarbon source, which optionally contains the recycled fraction E1 of step (d) are followed. , to a simplified cracking that produces a mixture of products containing ethylene and other constituents; b) subjecting said product mixture to a first separation step S1 which consists in separating said products containing ethylene and other constituents to give a fraction containing compounds that are lighter than ethylene and part of ethylene that is denominate fraction F1 and a fraction F2; c) send fraction F1 to an ethylene recovery unit in which it is separated to give a fraction enriched in ethylene called fraction E1 and a fraction enriched in compounds that are lighter than ethylene that is called light fraction; d) recycle fraction E1 to step a) or take it to the manufacture of at least one ethylene derivative compound; e) subject the fraction F2 to a second separation step S2 which consists of separating the fraction F2 to give a fraction enriched in ethylene which is called the fraction E2 or two fractions enriched with ethylene which are called the fractions E2a and E2b, and a fraction enriched in ethane and hydrocarbons containing at least 3 carbon atoms called the heavy fraction; f) then lead to fraction E2 or fractions E2a and E2b to the manufacture of at least one ethylene derivative compound.

ARP100104481A 2009-12-03 2010-12-03 PROCESS FOR THE MANUFACTURE OF AT LEAST A COMPOUND DERIVED FROM ETHYLENE AR079302A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP09177960 2009-12-03

Publications (1)

Publication Number Publication Date
AR079302A1 true AR079302A1 (en) 2012-01-18

Family

ID=42154427

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP100104481A AR079302A1 (en) 2009-12-03 2010-12-03 PROCESS FOR THE MANUFACTURE OF AT LEAST A COMPOUND DERIVED FROM ETHYLENE

Country Status (5)

Country Link
CN (1) CN102725252B (en)
AR (1) AR079302A1 (en)
EA (1) EA201290428A1 (en)
TW (1) TW201139333A (en)
WO (1) WO2011067237A2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014048864A2 (en) 2012-09-28 2014-04-03 Solvay Sa Process for producing liquefied impure ethylene

Family Cites Families (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1229999B (en) * 1964-01-31 1966-12-08 Huels Chemische Werke Ag Process for the production of 1, 2-dichloroethane
NL6901398A (en) 1969-01-29 1969-11-25
US4046822A (en) * 1971-10-26 1977-09-06 Stauffer Chemical Company Method for recovering ethylene values
DE3226042A1 (en) * 1982-07-12 1984-01-12 Hoechst Ag, 6230 Frankfurt Process for the preparation of 1,2-dichloroethane
FR2600643B1 (en) 1986-06-27 1988-09-23 Solvay ETHYLENE OXYCHLORATION PROCESS AND CATALYTIC COMPOSITIONS FOR OXYCHLORATION
EP0494474B1 (en) 1991-01-11 1994-09-21 SOLVAY (Société Anonyme) Oxychlorination catalytic composition and ethylene oxychlorination process using this composition
BE1007818A3 (en) 1993-12-08 1995-10-31 Solvay CATALYST COMPOSITION AND METHOD oxychlorination of ethylene USING THE COMPOSITION.
BE1013616A3 (en) 1998-10-30 2002-05-07 Solvay Chlorination ethylene cracking hydrocarbons obtained.
DE10159615A1 (en) * 2001-12-05 2003-06-12 Basf Ag Process for the preparation of 1,2-dichloroethane
FR2880019B1 (en) * 2004-12-23 2007-03-09 Solvay PROCESS FOR PRODUCING 1,2-DICHLOROETHANE
US20080108856A1 (en) 2004-12-23 2008-05-08 Michel Strebelle Process For The Manufacture Of 1,2-Dichloroethane
WO2006067188A1 (en) 2004-12-23 2006-06-29 Solvay (Société Anonyme) Process for the manufacture of 1,2-dichloroethane
WO2006067190A1 (en) 2004-12-23 2006-06-29 Solvay (Société Anonyme) Process for the manufacture of 1,2-dichloroethane
BRPI0519701A2 (en) 2004-12-23 2009-07-14 Solvay processes for the manufacture of 1,2 - dichloroethane and for the manufacture of vinyl chloride
FR2902784B1 (en) 2006-06-23 2008-09-05 Solvay PROCESS FOR PRODUCING 1,2-DICHLOROETHANE
FR2902785B1 (en) 2006-06-26 2008-08-08 Solvay PROCESS FOR PRODUCING 1,2-DICHLOROETHANE
FR2902786B1 (en) 2006-06-26 2008-08-29 Solvay PROCESS FOR PRODUCING 1,2-DICHLOROETHANE
FR2902787B1 (en) 2006-06-26 2008-09-05 Solvay PROCESS FOR PRODUCING 1,2-DICHLOROETHANE
EP2096095A1 (en) * 2008-02-28 2009-09-02 SOLVAY (Société Anonyme) Process for the manufacture of at least one ethylene derivative compound
JP2011513270A (en) * 2008-02-28 2011-04-28 ソルベイ（ソシエテ アノニム） Method for producing at least one ethylene derivative compound

Also Published As

Publication number Publication date
CN102725252A (en) 2012-10-10
EA201290428A1 (en) 2013-01-30
WO2011067237A2 (en) 2011-06-09
WO2011067237A3 (en) 2011-08-04
TW201139333A (en) 2011-11-16
CN102725252B (en) 2015-11-25

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