EA201100761A1 - METHOD AND SYSTEM FOR ADDING A METAL-PROMOTER IN SITU IN THE INSTALLATION OF CATALYTIC REFORMING - Google Patents
METHOD AND SYSTEM FOR ADDING A METAL-PROMOTER IN SITU IN THE INSTALLATION OF CATALYTIC REFORMINGInfo
- Publication number
- EA201100761A1 EA201100761A1 EA201100761A EA201100761A EA201100761A1 EA 201100761 A1 EA201100761 A1 EA 201100761A1 EA 201100761 A EA201100761 A EA 201100761A EA 201100761 A EA201100761 A EA 201100761A EA 201100761 A1 EA201100761 A1 EA 201100761A1
- Authority
- EA
- Eurasian Patent Office
- Prior art keywords
- situ
- promoter
- promoter metal
- catalytic reforming
- installation
- 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
- C10G35/00—Reforming naphtha
- C10G35/04—Catalytic reforming
- C10G35/10—Catalytic reforming with moving catalysts
- C10G35/12—Catalytic reforming with moving catalysts according to the "moving-bed" method
-
- 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
- C10G35/00—Reforming naphtha
- C10G35/04—Catalytic reforming
- C10G35/06—Catalytic reforming characterised by the catalyst used
-
- 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
- B01J23/08—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of gallium, indium or thallium
-
- 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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/06—Halogens; Compounds thereof
- B01J27/128—Halogens; Compounds thereof with iron group metals or platinum group metals
- B01J27/13—Platinum group metals
-
- 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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/28—Regeneration or reactivation
- B01J27/32—Regeneration or reactivation of catalysts comprising compounds of halogens
-
- 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
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/02—Heat treatment
-
- 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
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
- B01J38/10—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst using elemental hydrogen
-
- 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
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
- B01J38/42—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst using halogen-containing material
- B01J38/44—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst using halogen-containing material and adding simultaneously or subsequently free oxygen; using oxyhalogen compound
-
- 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
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/48—Liquid treating or treating in liquid phase, e.g. dissolved or suspended
-
- 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
- B01J38/00—Regeneration or reactivation of catalysts, in general
- B01J38/48—Liquid treating or treating in liquid phase, e.g. dissolved or suspended
- B01J38/60—Liquid treating or treating in liquid phase, e.g. dissolved or suspended using acids
-
- 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
- C10G35/00—Reforming naphtha
- C10G35/02—Thermal reforming
-
- 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
- C10G35/00—Reforming naphtha
- C10G35/04—Catalytic reforming
- C10G35/06—Catalytic reforming characterised by the catalyst used
- C10G35/085—Catalytic reforming characterised by the catalyst used containing platinum group metals or compounds thereof
-
- 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
- C10G2300/70—Catalyst aspects
Abstract
Одним примером осуществления изобретения может быть способ, облегчающий добавление металла-промотора по меньшей мере к одной частице катализатора in situ в установке каталитического риформинга нафты. Способ может включать ввод соединения, содержащего металл-промотор, в установку каталитического риформинга нафты и добавление эффективного количества металла-промотора из соединения, содержащего металл-промотор, к частице катализатора в условиях, способствующих такому добавлению и улучшению конверсии углеводородного сырья.One embodiment of the invention may be a method for facilitating the addition of a promoter metal to at least one catalyst particle in situ in a naphtha catalytic reformer. The method may include introducing a promoter metal compound into a naphtha catalytic reforming unit and adding an effective amount of a promoter metal from the promoter metal compound to the catalyst particle under conditions conducive to such addition and improving conversion of the hydrocarbon feed.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/269,366 US20100116714A1 (en) | 2008-11-12 | 2008-11-12 | Process and System for the Addition of Promoter Metal In Situ in a Catalytic Reforming Unit |
PCT/US2009/055639 WO2010056412A2 (en) | 2008-11-12 | 2009-09-02 | Process and system for the addition of promoter metal in situ in a catalytic reforming unit |
Publications (1)
Publication Number | Publication Date |
---|---|
EA201100761A1 true EA201100761A1 (en) | 2011-10-31 |
Family
ID=42164225
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EA201100761A EA201100761A1 (en) | 2008-11-12 | 2009-09-02 | METHOD AND SYSTEM FOR ADDING A METAL-PROMOTER IN SITU IN THE INSTALLATION OF CATALYTIC REFORMING |
Country Status (10)
Country | Link |
---|---|
US (1) | US20100116714A1 (en) |
EP (1) | EP2352804A4 (en) |
JP (1) | JP2012508647A (en) |
KR (1) | KR20110093815A (en) |
CN (1) | CN102216426A (en) |
AU (1) | AU2009314446B2 (en) |
BR (1) | BRPI0921379A2 (en) |
EA (1) | EA201100761A1 (en) |
MY (1) | MY156541A (en) |
WO (1) | WO2010056412A2 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20130256193A1 (en) * | 2012-03-29 | 2013-10-03 | Uop Llc | Process and system for the addition of promoter metal during operation in a catalytic reforming unit |
US8912110B2 (en) | 2012-03-29 | 2014-12-16 | Uop Llc | Catalyst for conversion of hydrocarbons |
US9266091B2 (en) | 2012-03-29 | 2016-02-23 | Uop Llc | Reforming catalysts with tuned acidity for maximum aromatics yield |
GB201509019D0 (en) * | 2015-05-27 | 2015-07-08 | Johnson Matthey Plc | Process and catalyst |
CN117427685A (en) * | 2023-12-20 | 2024-01-23 | 山东寿光鲁清石化有限公司 | Reforming method of naphtha |
Family Cites Families (47)
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US3892657A (en) * | 1972-07-17 | 1975-07-01 | Universal Oil Prod Co | Hydrocarbon conversion with a multimetallic catalytic composite |
US3929431A (en) * | 1972-09-08 | 1975-12-30 | Exxon Research Engineering Co | Catalytic reforming process |
JPS5814258B2 (en) * | 1974-04-19 | 1983-03-18 | トウアネンリヨウコウギヨウ カブシキガイシヤ | The name of the tank isotenkayo. |
US4203923A (en) * | 1974-11-26 | 1980-05-20 | Allied Chemical Corporation | Method for promotion of phenol hydrogenation |
US4198287A (en) * | 1976-02-02 | 1980-04-15 | Uop Inc. | Method of regenerating coke-contaminated catalyst with simultaneous combustion of carbon monoxide |
US4064037A (en) * | 1976-07-09 | 1977-12-20 | Mobil Oil Corporation | Temporary shutdown of co-combustion devices |
AU525445B2 (en) * | 1978-08-16 | 1982-11-04 | Mobil Oil Corp. | Reforming catalyst of separate platinum-containing and iridium-containing particles |
US4251391A (en) * | 1979-04-13 | 1981-02-17 | Exxon Research & Engineering Co. | Reforming with multimetallic catalysts |
US4309280A (en) * | 1980-07-18 | 1982-01-05 | Mobil Oil Corporation | Promotion of cracking catalyst octane yield performance |
US4482637A (en) * | 1982-08-04 | 1984-11-13 | Chevron Research Company | In situ hydrocarbon conversion catalyst regeneration and sulfur decontamination of vessels communicating with catalyst reactor |
US4440627A (en) * | 1983-03-10 | 1984-04-03 | Exxon Research And Engineering Co. | Catalytic reforming process |
US4487848A (en) * | 1983-06-02 | 1984-12-11 | Uop Inc. | Indium-containing catalyst for reforming hydrocarbons |
US4529505A (en) * | 1983-06-02 | 1985-07-16 | Uop Inc. | Indium-containing catalyst for reforming hydrocarbons |
US4522935A (en) * | 1983-06-02 | 1985-06-11 | Uop Inc. | Platinum and indium-containing catalyst for reforming hydrocarbons |
US4608356A (en) * | 1984-12-20 | 1986-08-26 | Chevron Research Company | Preparation of a reforming catalyst |
US4677094A (en) * | 1986-09-22 | 1987-06-30 | Uop Inc. | Trimetallic reforming catalyst |
US4975178A (en) * | 1988-05-23 | 1990-12-04 | Exxon Research & Engineering Company | Multistage reforming with interstage aromatics removal |
US5221463A (en) * | 1991-12-09 | 1993-06-22 | Exxon Research & Engineering Company | Fixed-bed/moving-bed two stage catalytic reforming with recycle of hydrogen-rich stream to both stages |
US5211838A (en) * | 1991-12-09 | 1993-05-18 | Exxon Research & Engineering Company | Fixed-bed/moving-bed two stage catalytic reforming with interstage aromatics removal |
FR2704864B1 (en) * | 1993-05-06 | 1995-11-17 | Inst Francais Du Petrole | CATALYTIC HYDROREFORMING PROCESS. |
US5342907A (en) * | 1993-06-28 | 1994-08-30 | Union Carbide Chemicals & Plastics Technology Corporation | Ethylene/propylene copolymer rubbers |
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US5565090A (en) * | 1994-11-25 | 1996-10-15 | Uop | Modified riser-reactor reforming process |
FR2735487B1 (en) * | 1995-06-16 | 1997-08-22 | Inst Francais Du Petrole | PROCESS FOR THE CATALYTIC TRANSFORMATION OF HYDROCARBONS INTO AROMATIC COMPOUNDS WITH A CATALYST CONTAINING ALKALINE OR ALKALINO-EARTH METALS |
US6034018A (en) * | 1995-10-20 | 2000-03-07 | Uop Llc | Method for reducing chloride emissions from a moving bed catalyst regeneration process |
US5879537A (en) * | 1996-08-23 | 1999-03-09 | Uop Llc | Hydrocarbon conversion process using staggered bypassing of reaction zones |
US5883032A (en) * | 1996-11-21 | 1999-03-16 | Uop Llc | Selective multimetallic multigradient reforming catalyst |
US6495487B1 (en) * | 1996-12-09 | 2002-12-17 | Uop Llc | Selective bifunctional multimetallic reforming catalyst |
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US5858908A (en) * | 1997-04-17 | 1999-01-12 | Uop Llc | Selective multimetallic-multigradient reforming catalyst |
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FR2770535B1 (en) * | 1997-10-31 | 1999-12-10 | Inst Francais Du Petrole | CATALYTIC HYDROREFORMING PROCESS |
US6106696A (en) * | 1997-12-16 | 2000-08-22 | Uop Llc | Moving bed reforming process without heating between the combined feed exchanger and the lead reactor |
US6036845A (en) * | 1998-05-04 | 2000-03-14 | Uop Llc | Modified riser-reactor reforming process with prereactor |
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FR2813304B1 (en) * | 2000-08-23 | 2002-11-29 | Inst Francais Du Petrole | PROCESS FOR DEHYDROGENATION OF ORGANIC COMPOUNDS IN THE PRESENCE OF A SUPPORTED BIMETALLIC CATALYST HAVING A STRONG INTERACTION BETWEEN A GROUP VIII METAL AND TIN |
US7037871B1 (en) * | 2001-11-21 | 2006-05-02 | Uop Llc | Low-temperature regeneration of zeolite L using ozone |
US20040102315A1 (en) * | 2002-11-27 | 2004-05-27 | Bailie Jillian Elaine | Reforming catalyst |
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US20060013763A1 (en) * | 2003-12-12 | 2006-01-19 | Baird Lance A | Process for the production of high purity hydrogen from a catalytic reformer |
US7846399B2 (en) * | 2004-03-23 | 2010-12-07 | W.R. Grace & Co.-Conn. | System and process for injecting catalyst and/or additives into a fluidized catalytic cracking unit |
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USH2244H1 (en) * | 2005-03-22 | 2010-08-03 | Exxonmobil Research And Engineering Company | Method for operating catalytic reformers |
US7638673B2 (en) * | 2005-05-04 | 2009-12-29 | Exxonmobil Chemical Patents Inc. | Process for hydrocarbon conversion with on-line solid particulate material removal |
US7909988B2 (en) * | 2008-04-17 | 2011-03-22 | Uop Llc | Process and system for the transfer of a metal catalyst component from one particle to another |
-
2008
- 2008-11-12 US US12/269,366 patent/US20100116714A1/en not_active Abandoned
-
2009
- 2009-09-02 EP EP09826485.6A patent/EP2352804A4/en not_active Withdrawn
- 2009-09-02 WO PCT/US2009/055639 patent/WO2010056412A2/en active Application Filing
- 2009-09-02 BR BRPI0921379A patent/BRPI0921379A2/en not_active IP Right Cessation
- 2009-09-02 MY MYPI2011001831A patent/MY156541A/en unknown
- 2009-09-02 EA EA201100761A patent/EA201100761A1/en unknown
- 2009-09-02 JP JP2011536350A patent/JP2012508647A/en active Pending
- 2009-09-02 KR KR1020117012034A patent/KR20110093815A/en not_active Application Discontinuation
- 2009-09-02 CN CN2009801450084A patent/CN102216426A/en active Pending
- 2009-09-02 AU AU2009314446A patent/AU2009314446B2/en not_active Ceased
Also Published As
Publication number | Publication date |
---|---|
JP2012508647A (en) | 2012-04-12 |
EP2352804A4 (en) | 2014-03-12 |
MY156541A (en) | 2016-02-26 |
EP2352804A2 (en) | 2011-08-10 |
BRPI0921379A2 (en) | 2015-12-29 |
AU2009314446B2 (en) | 2013-10-31 |
CN102216426A (en) | 2011-10-12 |
WO2010056412A2 (en) | 2010-05-20 |
US20100116714A1 (en) | 2010-05-13 |
KR20110093815A (en) | 2011-08-18 |
WO2010056412A3 (en) | 2010-07-01 |
AU2009314446A1 (en) | 2010-05-20 |
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