AR061630A1 - Proceso de elaboracion de 1.2-dicloroetano - Google Patents
Proceso de elaboracion de 1.2-dicloroetanoInfo
- Publication number
- AR061630A1 AR061630A1 ARP070102808A ARP070102808A AR061630A1 AR 061630 A1 AR061630 A1 AR 061630A1 AR P070102808 A ARP070102808 A AR P070102808A AR P070102808 A ARP070102808 A AR P070102808A AR 061630 A1 AR061630 A1 AR 061630A1
- Authority
- AR
- Argentina
- Prior art keywords
- fraction
- dichloroethane
- reactor
- optionally
- ethylene
- Prior art date
Links
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 title abstract 10
- 238000000034 method Methods 0.000 title abstract 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 abstract 8
- 239000005977 Ethylene Substances 0.000 abstract 8
- 238000005660 chlorination reaction Methods 0.000 abstract 7
- 239000007789 gas Substances 0.000 abstract 7
- 239000000203 mixture Substances 0.000 abstract 6
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 abstract 5
- 150000001875 compounds Chemical class 0.000 abstract 3
- 210000002196 fr. b Anatomy 0.000 abstract 3
- 210000003918 fraction a Anatomy 0.000 abstract 3
- 238000000926 separation method Methods 0.000 abstract 3
- 238000010521 absorption reaction Methods 0.000 abstract 2
- 238000003795 desorption Methods 0.000 abstract 2
- 230000003197 catalytic effect Effects 0.000 abstract 1
- 239000000470 constituent Substances 0.000 abstract 1
- 210000000540 fraction c Anatomy 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 238000010926 purge Methods 0.000 abstract 1
- 238000000746 purification Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- 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
- C07C17/25—Preparation of halogenated hydrocarbons by splitting-off hydrogen halides from halogenated 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
- C07C19/00—Acyclic saturated compounds containing halogen atoms
- C07C19/01—Acyclic saturated compounds containing halogen atoms containing chlorine
- C07C19/043—Chloroethanes
- C07C19/045—Dichloroethanes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C21/00—Acyclic unsaturated compounds containing halogen atoms
- C07C21/02—Acyclic unsaturated compounds containing halogen atoms containing carbon-to-carbon double bonds
- C07C21/04—Chloro-alkenes
- C07C21/06—Vinyl chloride
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F14/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
- C08F14/02—Monomers containing chlorine
- C08F14/04—Monomers containing two carbon atoms
- C08F14/06—Vinyl chloride
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F14/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
- C08F14/02—Monomers containing chlorine
- C08F14/04—Monomers containing two carbon atoms
- C08F14/12—1,2- Dichloroethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2/00—Processes of polymerisation
- C08F2/04—Polymerisation in solution
- C08F2/10—Aqueous solvent
-
- 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 de elaboracion de 1,2-dicloroetano comenzando a partir de un flujo de etano, donde: a) el flujo de etano es sometido a una oxideshidrogenacion catalítica que produce una mezcla de gases que contiene etileno, etano no convertido, agua y constituyentes secundarios; b) dicha mezcla de gases opcionalmente se lava y se seca, produciendo así una mezcla de gases seca; c) después de una etapa de purificacion opcional adicional, dicha mezcla de gases seca que comprende al flujo de productos derivado del reactor de cloracion R2 separada en la etapa e), es sometida a una absorcion A que consiste de la separacion de dicha mezcla de gases en una fraccion enriquecida con los compuestos que son más livianos que etileno que contienen parte del etileno (fraccion A) y en una fraccion F1; d) la fraccion A es desviada hacia un reactor de cloracion R1 en el cual la mayor parte del etileno presente en la fraccion A es convertido en 1,2- dicloroetano y el 1,2-dicloroetano obtenido es separado del flujo de productos derivado del reactor de cloracion R1; e) la fraccion F1 es sometida a una desorcion D1 que consiste en la separacion de la fraccion F1 en una fraccion de etileno agotado en compuestos que son más livianos que etileno (fraccion C) que es desviada hacia un reactor de cloracion R2, donde el flujo de productos derivado de este reactor se agrega a la mezcla de gases seca sometida a la etapa c) opcionalmente después de haber extraído el 1,2-dicloroetano formado, y en una fraccion F2; f) la fraccion F2 es sometida a una desorcion D2 que consiste en la separacion de la fraccion F2 en una fraccion enriquecida con etileno (fraccion B) y en una fraccion F3, que opcionalmente contiene al 1,2-dicloroetano formado en el reactor de cloracion R2 luego se extrae, si no ha sido extraído previamente, que es reciclada hacia la absorcion A, opcionalmente después de un tratamiento adicional destinado a reducir la concentracion, en la fraccion F3, de los compuestos que son más pesados que el etano; g) la fraccion B es desviada hacia un reactor de oxicloracion en el cual la mayor parte del etileno presente en la fraccion B es convertido en 1,2-dicloroetano, el 1,2-dicloroetano obtenido es separado del flujo de productos derivado del reactor de oxicloracion y opcionalmente se agrega al 1,2-dicloroetano formado en el reactor de cloracion R1 y opcionalmente al que se formo en el reactor de cloracion R2; y h) el flujo de productos derivado del reactor de oxicloracion, de cual se ha extraído el 1,2-dicloroetano, que opcionalmente contiene un flujo de etano adicional introducido previamente en una de las etapas b) a g), es reciclado opcionalmente hacia la etapa a) opcionalmente después de haber purgado los gases y/o después de un tratamiento opcional con el fin de eliminar los productos dorados contenidos en el mismo.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR0605718A FR2902787B1 (fr) | 2006-06-26 | 2006-06-26 | Procede de fabrication de 1,2-dichloroethane |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AR061630A1 true AR061630A1 (es) | 2008-09-10 |
Family
ID=37964826
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ARP070102808A AR061630A1 (es) | 2006-06-26 | 2007-06-25 | Proceso de elaboracion de 1.2-dicloroetano |
Country Status (17)
| Country | Link |
|---|---|
| US (1) | US8119745B2 (es) |
| EP (1) | EP2043978A1 (es) |
| JP (1) | JP2009541422A (es) |
| KR (1) | KR20090023500A (es) |
| CN (1) | CN101500972B (es) |
| AR (1) | AR061630A1 (es) |
| AU (1) | AU2007263766B2 (es) |
| BR (1) | BRPI0714169A2 (es) |
| CA (1) | CA2655123C (es) |
| EA (1) | EA015307B1 (es) |
| FR (1) | FR2902787B1 (es) |
| MX (1) | MX2009000181A (es) |
| MY (1) | MY146963A (es) |
| NO (1) | NO20085236L (es) |
| TW (1) | TW200827325A (es) |
| UA (1) | UA96299C2 (es) |
| WO (1) | WO2008000693A1 (es) |
Families Citing this family (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008525379A (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 |
| 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 |
| FR2902786B1 (fr) | 2006-06-26 | 2008-08-29 | Solvay | Procede de fabrication de 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 (ja) * | 2008-02-28 | 2011-04-28 | ソルベイ（ソシエテ アノニム） | 少なくとも１つのエチレン誘導体化合物の製造方法 |
| EP2130815A1 (en) | 2008-06-03 | 2009-12-09 | SOLVAY (Société Anonyme) | Process for the manufacture of at least one ethylene derivative compound |
| EP2130811A1 (en) | 2008-06-03 | 2009-12-09 | SOLVAY (Société Anonyme) | Process for the production of low-concentration ethylene for chemical use |
| 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 |
| EP2130814A1 (en) | 2008-06-03 | 2009-12-09 | SOLVAY (Société Anonyme) | Process for the manufacture of at least one ethylene derivative compound |
| EA201290428A1 (ru) | 2009-12-03 | 2013-01-30 | Солвей Са | Способ получения по меньшей мере одного производного соединения этилена |
| MX2012006124A (es) | 2009-12-03 | 2012-06-19 | Solvay | Proceso para la fabricacion de por lo menos un compuesto derivado de etileno. |
| WO2013026720A1 (en) | 2011-08-25 | 2013-02-28 | Solvay Sa | Process for the manufacture of 1,2 - dichloroethane (dce) |
| EP2606963A1 (en) | 2011-12-20 | 2013-06-26 | Solvay Sa | Catalyst, process for catalyst manufacture and process for catalytic oxidative dehydrogenation |
| EP2606964A1 (en) | 2011-12-20 | 2013-06-26 | Solvay Sa | Catalyst, process for catalyst manufacture and process for catalytic oxidative dehydrogenation |
| EP2606965A1 (en) | 2011-12-20 | 2013-06-26 | Solvay Sa | Catalyst, process for catalyst manufacture and process for catalytic oxidative dehydrogenation |
| WO2014048864A2 (en) | 2012-09-28 | 2014-04-03 | Solvay Sa | Process for producing liquefied impure ethylene |
| EP2772475A1 (en) | 2013-03-01 | 2014-09-03 | Solvay SA | Process for the manufacture of a crude alkane and/or alkene oxidation product |
| CN105837395A (zh) * | 2015-01-13 | 2016-08-10 | 青岛海晶化工集团有限公司 | 一种低温乙烯冷能在乙烯平衡氧氯化法制备vcm的利用方法 |
Family Cites Families (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL6901398A (es) | 1969-01-29 | 1969-11-25 | ||
| US4250346A (en) * | 1980-04-14 | 1981-02-10 | Union Carbide Corporation | Low temperature oxydehydrogenation of ethane to ethylene |
| FR2600643B1 (fr) | 1986-06-27 | 1988-09-23 | Solvay | Procede d'oxychloration de l'ethylene et compositions catalytiques pour l'oxychloration |
| ATE111771T1 (de) | 1991-01-11 | 1994-10-15 | Solvay | Oxychlorierung katalytischer zusammensetzung und verfahren für die oxychlorierung von ethylen unter verwendung dieser zusammensetzung. |
| US6803342B1 (en) | 1993-12-08 | 2004-10-12 | Solvay (Societe Anonyme) | Catalytic composition and process for the oxychlorination of ethylene using such a composition |
| BE1007818A3 (fr) | 1993-12-08 | 1995-10-31 | Solvay | Composition catalytique et procede d'oxychloration de l'ethylene utilisant une telle composition. |
| BE1013616A3 (fr) * | 1998-10-30 | 2002-05-07 | Solvay | Chloration d'ethylene obtenu par cracking d'hydrocarbures. |
| WO2000048971A1 (en) * | 1999-02-22 | 2000-08-24 | Symyx Technologies, Inc. | Compositions comprising nickel and their use as catalyst in oxidative dehydrogenation of alkanes |
| HUP0204200A3 (en) * | 1999-11-22 | 2003-11-28 | Dow Chemical Co | Process for vinyl chloride manufacture from ethane and ethylene with immediate hcl recovery from reactor effluent |
| DE10159615A1 (de) * | 2001-12-05 | 2003-06-12 | Basf Ag | Verfahren zur Herstellung von 1,2-Dichlorethan |
| AR052833A1 (es) | 2004-12-23 | 2007-04-04 | Solvay | Proceso de eleboracion de 1,2- dicloroetano |
| WO2006067188A1 (en) | 2004-12-23 | 2006-06-29 | Solvay (Société Anonyme) | Process for the manufacture of 1,2-dichloroethane |
| 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 |
| JP2008525379A (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 |
| 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 |
| FR2902785B1 (fr) | 2006-06-26 | 2008-08-08 | Solvay | Procede de fabrication de 1,2-dichloroethane |
| FR2913421B1 (fr) | 2007-03-07 | 2009-05-15 | Solvay | Procede de fabrication de dichloropropanol. |
| JP2011513270A (ja) | 2008-02-28 | 2011-04-28 | ソルベイ（ソシエテ アノニム） | 少なくとも１つのエチレン誘導体化合物の製造方法 |
| 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 |
| EP2130811A1 (en) | 2008-06-03 | 2009-12-09 | SOLVAY (Société Anonyme) | Process for the production of low-concentration ethylene for chemical use |
| EP2130813A1 (en) | 2008-06-03 | 2009-12-09 | SOLVAY (Société 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 |
-
2006
- 2006-06-26 FR FR0605718A patent/FR2902787B1/fr not_active Expired - Fee Related
-
2007
- 2007-06-22 CN CN2007800293443A patent/CN101500972B/zh not_active Expired - Fee Related
- 2007-06-22 MY MYPI20085036A patent/MY146963A/en unknown
- 2007-06-22 WO PCT/EP2007/056227 patent/WO2008000693A1/en active Application Filing
- 2007-06-22 MX MX2009000181A patent/MX2009000181A/es active IP Right Grant
- 2007-06-22 EA EA200970054A patent/EA015307B1/ru not_active IP Right Cessation
- 2007-06-22 BR BRPI0714169-6A patent/BRPI0714169A2/pt not_active IP Right Cessation
- 2007-06-22 KR KR1020097001238A patent/KR20090023500A/ko not_active Application Discontinuation
- 2007-06-22 CA CA2655123A patent/CA2655123C/en not_active Expired - Fee Related
- 2007-06-22 UA UAA200900516A patent/UA96299C2/ru unknown
- 2007-06-22 US US12/304,434 patent/US8119745B2/en not_active Expired - Fee Related
- 2007-06-22 AU AU2007263766A patent/AU2007263766B2/en not_active Ceased
- 2007-06-22 EP EP07730297A patent/EP2043978A1/en not_active Withdrawn
- 2007-06-22 JP JP2009517133A patent/JP2009541422A/ja not_active Ceased
- 2007-06-25 AR ARP070102808A patent/AR061630A1/es unknown
- 2007-06-26 TW TW096123083A patent/TW200827325A/zh unknown
-
2008
- 2008-12-16 NO NO20085236A patent/NO20085236L/no not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| CN101500972A (zh) | 2009-08-05 |
| MY146963A (en) | 2012-10-15 |
| AU2007263766A1 (en) | 2008-01-03 |
| EA015307B1 (ru) | 2011-06-30 |
| US8119745B2 (en) | 2012-02-21 |
| MX2009000181A (es) | 2009-01-23 |
| EP2043978A1 (en) | 2009-04-08 |
| FR2902787B1 (fr) | 2008-09-05 |
| JP2009541422A (ja) | 2009-11-26 |
| CA2655123C (en) | 2014-10-07 |
| BRPI0714169A2 (pt) | 2012-12-25 |
| WO2008000693A1 (en) | 2008-01-03 |
| FR2902787A1 (fr) | 2007-12-28 |
| TW200827325A (en) | 2008-07-01 |
| AU2007263766B2 (en) | 2012-03-29 |
| US20090203854A1 (en) | 2009-08-13 |
| CA2655123A1 (en) | 2008-01-03 |
| CN101500972B (zh) | 2013-03-27 |
| KR20090023500A (ko) | 2009-03-04 |
| UA96299C2 (ru) | 2011-10-25 |
| NO20085236L (no) | 2009-02-27 |
| EA200970054A1 (ru) | 2009-06-30 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FB | Suspension of granting procedure |