PE20130169A1 - PROCESS FOR THE MANUFACTURE OF AT LEAST ONE COMPOUND DERIVED FROM ETHYLENE - Google Patents

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

Info

Publication number
PE20130169A1
PE20130169A1 PE2012000744A PE2012000744A PE20130169A1 PE 20130169 A1 PE20130169 A1 PE 20130169A1 PE 2012000744 A PE2012000744 A PE 2012000744A PE 2012000744 A PE2012000744 A PE 2012000744A PE 20130169 A1 PE20130169 A1 PE 20130169A1
Authority
PE
Peru
Prior art keywords
fraction
ethylene
enriched
manufacture
give
Prior art date
Application number
PE2012000744A
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 PE20130169A1 publication Critical patent/PE20130169A1/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

QUE COMPRENDE LOS PASOS DE: a) SOMETER EL GAS RESIDUAL DE BAJO VALOR, QUE OPCIONALMENTE CONTIENE LA FRACCION E1 RECICLADA DEL PASO d), A UNA SERIE DE PASOS DE TRATAMIENTO EN UNA UNIDAD DE RECUPERACION DE GAS RESIDUAL DE BAJO VALOR PARA ELIMINAR LOS COMPONENTES NO DESEADOS PRESENTES EN EL MISMO Y PARA OBTENER UNA MEZCLA DE PRODUCTOS QUE CONTIENE ETILENO Y OTROS CONSTITUYENTES; b) SOMETER DICHA MEZCLA DE PRODUCTOS A UN PRIMER PASO DE SEPARACION S1 QUE CONSISTE EN SEPARAR A DICHOS PRODUCTOS QUE CONTIENE ETILENO Y OTROS CONSTITUYENTES PARA DAR UNA FRACCION QUE CONTIENE A LOS COMPUESTOS QUE SON MAS LIVIANOS QUE EL ETILENO Y PARTE DEL ETILENO QUE SE DENOMINA FRACCION F1 Y F2; c) LA FRACCION F1 SE ENVIA A UNA UNIDAD DE RECUPERACION DE ETILENO EN LA CUAL SE SEPARA PARA DAR UNA FRACCION ENRIQUECIDA EN ETILENO DENOMINADA FRACCION E1 Y EN UNA FRACCION ENRIQUECIDA CON LOS COMPUESTOS QUE SON MAS LIVIANOS QUE EL ETILENO; d) RECICLAR LA FRACCION E1 AL PASO a) O LLEVARLA A LA FABRICACION DE POR LO MENOS UN COMPUESTO DERIVADO DE ETILENO; e) SOMETER LA FRACCION F2 A UN SEGUNDO PASO DE SEPARACION S2, QUE CONSISTE EN SEPARAR LA FRACCION F2 PARA DAR UNA FRACCION ENRIQUECIDA CON ETILENO DENOMINADA FRACCION E2 O EN DOS FRACCIONES ENRIQUECIDAS CON ETILENO LLAMADAS FRACCIONES E2a Y E2b, Y UNA FRACCION ENRIQUECIDA EN ETANO E HIDROCARBUROS QUE CONTIENEN POR LO MENOS 3 ATOMOS DE CARBONO; F) LLEVAR LA FRACCION E2 O LAS FRACCIONES E2a Y E2b A LA FABRICACION DE POR LO MENOS UN COMPUESTO DERIVADO DE ETILENOWHICH INCLUDES THE STEPS OF: a) SUBMITTING THE LOW VALUE WASTE GAS, WHICH OPTIONALLY CONTAINS THE RECYCLED E1 FRACTION FROM STEP d), TO A SERIES OF TREATMENT STEPS IN A LOW VALUE WASTE GAS RECOVERY UNIT TO ELIMINATE THE COMPONENTS NOT WANTED PRESENT IN THE SAME AND TO OBTAIN A MIX OF PRODUCTS THAT CONTAINS ETHYLENE AND OTHER CONSTITUENTS; b) SUBMIT SAID MIXTURE OF PRODUCTS TO A FIRST STEP OF SEPARATION S1 WHICH CONSISTS OF SEPARATING SAID PRODUCTS THAT CONTAIN ETHYLENE AND OTHER CONSTITUENTS TO GIVE A FRACTION THAT CONTAINS COMPOUNDS THAT ARE LIGHTER THAN ETHYLENE AND PART OF THE ETHYLENE THAT IS DIVIDED FROM ETHYLENE FRACTION F1 AND F2; c) FRACTION F1 IS SENT TO AN ETHYLENE RECOVERY UNIT IN WHICH IT IS SEPARATED TO GIVE A FRACTION ENRICHED IN ETHYLENE CALLED FRACTION E1 AND IN A FRACTION ENRICHED WITH COMPOUNDS THAT ARE LIGHTER THAN ETHYLENE; d) RECYCLE FRACTION E1 TO STEP a) OR TAKE IT TO THE MANUFACTURE OF AT LEAST ONE COMPOUND DERIVED FROM ETHYLENE; e) SUBMIT THE FRACTION F2 TO A SECOND STEP OF SEPARATION S2, WHICH CONSISTS OF SEPARATING THE FRACTION F2 TO GIVE AN ENRICHED FRACTION WITH ETHYLENE CALLED FRACTION E2 OR IN TWO FRACTIONS ENRICHED WITH ETHYLENE CALLED FRACTIONS IN AN ETHANEB AND FRACTION IN E2a AND FRAC2 AND HYDROCARBONS CONTAINING AT LEAST 3 CARBON ATOMS; F) TAKE FRACTION E2 OR FRACTIONS E2a AND E2b TO THE MANUFACTURE OF AT LEAST ONE COMPOUND DERIVED FROM ETHYLENE

PE2012000744A 2009-12-03 2010-11-30 PROCESS FOR THE MANUFACTURE OF AT LEAST ONE COMPOUND DERIVED FROM ETHYLENE PE20130169A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP09177959 2009-12-03

Publications (1)

Publication Number Publication Date
PE20130169A1 true PE20130169A1 (en) 2013-03-09

Family

ID=42086348

Family Applications (1)

Application Number Title Priority Date Filing Date
PE2012000744A PE20130169A1 (en) 2009-12-03 2010-11-30 PROCESS FOR THE MANUFACTURE OF AT LEAST ONE COMPOUND DERIVED FROM ETHYLENE

Country Status (9)

Country Link
CN (1) CN102725253B (en)
AR (1) AR079436A1 (en)
BR (1) BR112012013333A2 (en)
CO (1) CO6571897A2 (en)
EA (1) EA024187B1 (en)
MX (1) MX2012006124A (en)
PE (1) PE20130169A1 (en)
TW (1) TW201125849A (en)
WO (1) WO2011067231A1 (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 (19)

* 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
ATE111771T1 (en) 1991-01-11 1994-10-15 Solvay OXYCHLORATION CATALYTIC COMPOSITION AND PROCESS FOR THE OXYCHLORATION OF ETHYLENE USING SUCH 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
JP2008525377A (en) 2004-12-23 2008-07-17 ソルヴェイ（ソシエテ アノニム） Process for producing 1,2-dichloroethane
WO2006067188A1 (en) 2004-12-23 2006-06-29 Solvay (Société Anonyme) Process for the manufacture of 1,2-dichloroethane
JP2008525379A (en) 2004-12-23 2008-07-17 ソルヴェイ（ソシエテ アノニム） Process for producing 1,2-dichloroethane
AR052833A1 (en) 2004-12-23 2007-04-04 Solvay ELEBORATION PROCESS OF 1,2- DICHLOROETHANE
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
FR2902787B1 (en) 2006-06-26 2008-09-05 Solvay PROCESS FOR PRODUCING 1,2-DICHLOROETHANE
FR2902786B1 (en) 2006-06-26 2008-08-29 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
WO2011067231A1 (en) 2011-06-09
AR079436A1 (en) 2012-01-25
TW201125849A (en) 2011-08-01
CO6571897A2 (en) 2012-11-30
BR112012013333A2 (en) 2016-03-01
CN102725253A (en) 2012-10-10
EA201290427A1 (en) 2013-01-30
CN102725253B (en) 2015-11-25
EA024187B1 (en) 2016-08-31
MX2012006124A (en) 2012-06-19

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