CL2009001797A1 - Proceso para la eliminacion de mercaptanos de una mezcla de hidrocarburos que comprende una etapa de catalisis para la tioeterificacion de mercaptanos a tioeteres y destilacion. - Google Patents
Proceso para la eliminacion de mercaptanos de una mezcla de hidrocarburos que comprende una etapa de catalisis para la tioeterificacion de mercaptanos a tioeteres y destilacion.Info
- Publication number
- CL2009001797A1 CL2009001797A1 CL2009001797A CL2009001797A CL2009001797A1 CL 2009001797 A1 CL2009001797 A1 CL 2009001797A1 CL 2009001797 A CL2009001797 A CL 2009001797A CL 2009001797 A CL2009001797 A CL 2009001797A CL 2009001797 A1 CL2009001797 A1 CL 2009001797A1
- Authority
- CL
- Chile
- Prior art keywords
- mercaptans
- thioethers
- hydrocarbons
- reactor
- boiling point
- Prior art date
Links
Classifications
-
- 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
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
- C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
- C10G45/10—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing platinum group metals or compounds thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/48—Silver or gold
- B01J23/50—Silver
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/148—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/148—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
- C07C7/14875—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound with organic compounds
-
- 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
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
- C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
-
- 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
- C10G70/00—Working-up undefined normally gaseous mixtures obtained by processes covered by groups C10G9/00, C10G11/00, C10G15/00, C10G47/00, C10G51/00
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
- C10L3/10—Working-up natural gas or synthetic natural gas
- C10L3/101—Removal of contaminants
- C10L3/102—Removal of contaminants of acid contaminants
- C10L3/103—Sulfur containing contaminants
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/12—Liquefied petroleum gas
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/44—Palladium
-
- 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
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/202—Heteroatoms content, i.e. S, N, O, P
-
- 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
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4087—Catalytic distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Analytical Chemistry (AREA)
- Water Supply & Treatment (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
LA PRESENTE INVENCIÓN SE REFIERE A UN PROCESO PARA ELIMINAR MERCAPTANOS DE UNA MEZCLA DE FASE GASEOSA QUE COMPRENDE LAS ETAPES DE (AL ALIMENTAR A UN REACTOR UNA MEZCLA DE FASE GASEOSA QUE COMPRENDE HIDROCARBUROS Y MERCAPLANOS. EN DONDE EL REACTOR COMPRENDE UN CATALIZADOR QUE ES CAPAZ DE CATALIZAR LA TIOETERIFLCCIÓN DE MERCAPTANOS A TIOÉTERES PARA PRODUCIR UNA MUDA DE PRODUCTOS DEL REACTOR, EL CATALIZADOR COMPRENDE MÁS DE 200 PPM DE PALADIO, Y UNA PROPORCIÓN MOLAR DE PALADIO A PLATA EN EL RENGO DE 0,1 A 10; (B) ALIMENTAR LA MAZCLA DE PRODUCTOS DEL REACTOR A UNA UNIDAD DE DESTILACION QUE COMPRENDE UNA SECCIÓN SUPERIOR Y UNA LNFERIOR; (C) SEPARAR LOS HIDROCARBUROS DE BAJO PUNTO DE EBULLICIÓN DE LOS TIOÉTERES EN DONDE LOS HIDROCARBURO. DE MENOR PUNTO DE EBULLICIÓN ESTÁN SUSTANCIALMENTE CONTENIDOS EN LA SECCIÓN SUPERIOR Y LOS TIOÉTERES ESTÁN SUSTANCIALMENTE CONTENIDOS EN LA SECCIÓN INFERIOR, Y (D) RECUPERAR LOS HIDROCARBUROS DE BAJO PUNTO DE EBULLICIÓN DE LA PARLE SUPERIOR.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/207,390 US8197674B2 (en) | 2008-09-09 | 2008-09-09 | Thioetherification processes for the removal of mercaptans from gas streams |
Publications (1)
Publication Number | Publication Date |
---|---|
CL2009001797A1 true CL2009001797A1 (es) | 2009-12-04 |
Family
ID=41798283
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CL2009001797A CL2009001797A1 (es) | 2008-09-09 | 2009-09-02 | Proceso para la eliminacion de mercaptanos de una mezcla de hidrocarburos que comprende una etapa de catalisis para la tioeterificacion de mercaptanos a tioeteres y destilacion. |
Country Status (16)
Country | Link |
---|---|
US (1) | US8197674B2 (es) |
EP (1) | EP2326698A4 (es) |
JP (1) | JP5620912B2 (es) |
KR (1) | KR101533584B1 (es) |
CN (1) | CN102149793B (es) |
AR (1) | AR073362A1 (es) |
BR (1) | BRPI0918905A2 (es) |
CA (1) | CA2734692C (es) |
CL (1) | CL2009001797A1 (es) |
MX (1) | MX2011001891A (es) |
MY (1) | MY150589A (es) |
NO (1) | NO20110244A1 (es) |
SG (1) | SG193830A1 (es) |
TW (1) | TWI406935B (es) |
WO (1) | WO2010030576A1 (es) |
ZA (1) | ZA201102590B (es) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102012212317A1 (de) * | 2012-07-13 | 2014-01-16 | Evonik Industries Ag | Thioveretherung von Mercaptanen in C4-Kohlenwasserstoffgemischen |
CN103820149B (zh) * | 2012-11-16 | 2015-10-28 | 中国石油天然气股份有限公司 | 一种降低液化气中硫含量的方法 |
CN104511244B (zh) * | 2013-10-08 | 2018-09-25 | 中国石油化工股份有限公司 | 一种利用烷基化反应脱除气态烃中硫醇的方法 |
CN104971724B (zh) * | 2014-04-01 | 2018-02-16 | 中国石油天然气集团公司 | 一种低温硫醇硫醚化催化剂及其制备方法 |
CN105176615B (zh) * | 2014-06-05 | 2019-03-29 | 中国石油化工股份有限公司 | 一种液化气固定床脱硫醇方法 |
CN104194833B (zh) * | 2014-07-15 | 2015-12-02 | 中国石油大学(华东) | 一种液化气深度脱硫工艺方法 |
CN105561759B (zh) * | 2014-10-14 | 2018-09-25 | 中国石油化工股份有限公司 | 利用烷基化反应同时脱除工业气体中硫化氢和硫醇类物质的方法 |
Family Cites Families (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2988500A (en) * | 1959-03-13 | 1961-06-13 | Universal Oil Prod Co | Treatment of hydrocarbon distillates |
EP0016284B1 (en) * | 1979-03-21 | 1983-06-22 | DAVY McKEE (LONDON) LIMITED | Process for the production of a sulphur-free butene-1 rich stream |
US4626341A (en) * | 1985-12-23 | 1986-12-02 | Uop Inc. | Process for mercaptan extraction from olefinic hydrocarbons |
US4775462A (en) * | 1987-06-22 | 1988-10-04 | Uop Inc. | Non-oxidative method of sweetening a sour hydrocarbon fraction |
US5424051A (en) * | 1992-01-14 | 1995-06-13 | Uop | Process for the removal of carbon dioxide and mercaptans from a gas stream |
US5510568A (en) * | 1994-06-17 | 1996-04-23 | Chemical Research & Licensing Company | Process for the removal of mercaptans and hydrogen sulfide from hydrocarbon streams |
US5659106A (en) * | 1995-06-22 | 1997-08-19 | Uop | Catalytic distillation process for mercaptan and olefin removal |
US5759386A (en) * | 1997-01-09 | 1998-06-02 | Uop | Process for thioetherification and selective hydrogenation of light hydrocarbons |
US5851383A (en) * | 1997-01-09 | 1998-12-22 | Uop Llc | Process for thioetherification and selective hydrogenation of light olefins |
US6231752B1 (en) * | 1999-09-17 | 2001-05-15 | Catalytic Distillation Technologies | Process for the removal of mercaptans |
FR2807061B1 (fr) * | 2000-03-29 | 2002-05-31 | Inst Francais Du Petrole | Procede de desulfuration d'essence comprenant une desulfuration des fractions lourde et intermediaire issues d'un fractionnement en au moins trois coupes |
US6576588B2 (en) * | 2000-04-07 | 2003-06-10 | Catalytic Distillation Technologies | Process for selective hydrogenation of alkynes and catalyst therefor |
US6444118B1 (en) * | 2001-02-16 | 2002-09-03 | Catalytic Distillation Technologies | Process for sulfur reduction in naphtha streams |
US20040188327A1 (en) * | 2001-06-20 | 2004-09-30 | Catalytic Distillation Technologies | Process for sulfur reduction in naphtha streams |
US6849773B2 (en) * | 2002-01-23 | 2005-02-01 | Catalytic Distillation Technologies | Process for the utilization of refinery C4 streams |
MY137042A (en) * | 2002-06-14 | 2008-12-31 | Chevron Phillips Chemical Co | Hydrogenation palladium-silver catalyst and methods |
US6984312B2 (en) * | 2002-11-22 | 2006-01-10 | Catalytic Distillation Technologies | Process for the desulfurization of light FCC naphtha |
US20040260131A1 (en) * | 2003-06-23 | 2004-12-23 | Chevron Phillips Chemical Company ("Cpchem") | Selective hydrocarbon hydrogenation catalyst and process |
FR2873711B1 (fr) * | 2004-08-02 | 2006-09-15 | Inst Francais Du Petrole | Procede de capture des mercaptans contenus dans une charge gazeuse |
-
2008
- 2008-09-09 US US12/207,390 patent/US8197674B2/en active Active
-
2009
- 2009-09-02 CL CL2009001797A patent/CL2009001797A1/es unknown
- 2009-09-04 KR KR1020117007845A patent/KR101533584B1/ko active IP Right Grant
- 2009-09-04 EP EP09813484.4A patent/EP2326698A4/en not_active Withdrawn
- 2009-09-04 WO PCT/US2009/056050 patent/WO2010030576A1/en active Application Filing
- 2009-09-04 MX MX2011001891A patent/MX2011001891A/es active IP Right Grant
- 2009-09-04 MY MYPI20110724 patent/MY150589A/en unknown
- 2009-09-04 AR ARP090103412A patent/AR073362A1/es not_active Application Discontinuation
- 2009-09-04 CA CA2734692A patent/CA2734692C/en not_active Expired - Fee Related
- 2009-09-04 BR BRPI0918905A patent/BRPI0918905A2/pt not_active IP Right Cessation
- 2009-09-04 SG SG2013064837A patent/SG193830A1/en unknown
- 2009-09-04 CN CN200980134965.7A patent/CN102149793B/zh not_active Expired - Fee Related
- 2009-09-04 JP JP2011526925A patent/JP5620912B2/ja not_active Expired - Fee Related
- 2009-09-08 TW TW098130157A patent/TWI406935B/zh active
-
2011
- 2011-02-14 NO NO20110244A patent/NO20110244A1/no not_active Application Discontinuation
- 2011-04-07 ZA ZA2011/02590A patent/ZA201102590B/en unknown
Also Published As
Publication number | Publication date |
---|---|
CA2734692A1 (en) | 2010-03-18 |
KR20110059869A (ko) | 2011-06-07 |
TW201011100A (en) | 2010-03-16 |
US8197674B2 (en) | 2012-06-12 |
NO20110244A1 (no) | 2011-03-02 |
ZA201102590B (en) | 2011-12-28 |
CA2734692C (en) | 2016-02-16 |
JP5620912B2 (ja) | 2014-11-05 |
SG193830A1 (en) | 2013-10-30 |
CN102149793A (zh) | 2011-08-10 |
WO2010030576A1 (en) | 2010-03-18 |
BRPI0918905A2 (pt) | 2015-12-01 |
EP2326698A1 (en) | 2011-06-01 |
JP2012502171A (ja) | 2012-01-26 |
MX2011001891A (es) | 2011-05-25 |
AR073362A1 (es) | 2010-11-03 |
TWI406935B (zh) | 2013-09-01 |
MY150589A (en) | 2014-01-30 |
US20100059413A1 (en) | 2010-03-11 |
CN102149793B (zh) | 2017-06-20 |
EP2326698A4 (en) | 2014-05-21 |
KR101533584B1 (ko) | 2015-07-03 |
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