RU2011132046A - Регенерация катализатора - Google Patents
Регенерация катализатора Download PDFInfo
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- RU2011132046A RU2011132046A RU2011132046/04A RU2011132046A RU2011132046A RU 2011132046 A RU2011132046 A RU 2011132046A RU 2011132046/04 A RU2011132046/04 A RU 2011132046/04A RU 2011132046 A RU2011132046 A RU 2011132046A RU 2011132046 A RU2011132046 A RU 2011132046A
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/23—Rearrangement of carbon-to-carbon unsaturated bonds
- C07C5/25—Migration of carbon-to-carbon double bonds
- C07C5/2506—Catalytic processes
- C07C5/2512—Catalytic processes with metal oxides
-
- 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/20—Regeneration or reactivation
-
- 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
-
- 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
- B01J23/90—Regeneration or reactivation
- B01J23/92—Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
-
- 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
-
- 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
- B01J38/06—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst using steam
-
- 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
- B01J38/12—Treating with free oxygen-containing gas
- B01J38/20—Plural distinct oxidation stages
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
- C07C6/02—Metathesis reactions at an unsaturated carbon-to-carbon bond
- C07C6/04—Metathesis reactions at an unsaturated carbon-to-carbon bond at a carbon-to-carbon double bond
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
- C07C6/02—Metathesis reactions at an unsaturated carbon-to-carbon bond
- C07C6/04—Metathesis reactions at an unsaturated carbon-to-carbon bond at a carbon-to-carbon double bond
- C07C6/06—Metathesis reactions at an unsaturated carbon-to-carbon bond at a carbon-to-carbon double bond at a cyclic carbon-to-carbon double bond
-
- 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/10—Magnesium; Oxides or hydroxides 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
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/30—Tungsten
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
- C07C2521/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- C07C2521/08—Silica
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
- C07C2521/10—Magnesium; Oxides or hydroxides thereof
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/24—Chromium, molybdenum or tungsten
- C07C2523/28—Molybdenum
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/24—Chromium, molybdenum or tungsten
- C07C2523/30—Tungsten
-
- 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
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
-
- 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
- Y02P20/584—Recycling of catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
1. Способ регенерации использованной каталитической смеси, содержащей (i) катализатор изомеризации, содержащий оксид магния, и (ii) катализатор метатезиса, содержащий неорганический носитель и по меньшей мере один компонент из оксида молибдена и оксида вольфрама, включающий: (a) удаление кокса из использованной каталитической смеси в присутствии кислородсодержащего газа, с получением каталитической смеси без кокса; и (b) контактирование каталитической смеси без кокса с паром при температуре в интервале от 100 до 300°C с получением регенерированной каталитической смеси.2. Способ по п.1, в котором стадию (b) выполняют при температуре в интервале от 150 до 250°C.3. Способ по п.1, в котором катализатор изомеризации содержит 95 мас.% оксида магния.4. Способ по п.1, в котором катализатор метатезиса содержит оксид вольфрама.5. Способ по п.4, в котором неорганический носитель является кремнеземом.6. Способ по п.1, в котором использованную каталитическую смесь извлекают из процесса получения пропилена из линейного бутена и этилена.
Claims (6)
1. Способ регенерации использованной каталитической смеси, содержащей (i) катализатор изомеризации, содержащий оксид магния, и (ii) катализатор метатезиса, содержащий неорганический носитель и по меньшей мере один компонент из оксида молибдена и оксида вольфрама, включающий: (a) удаление кокса из использованной каталитической смеси в присутствии кислородсодержащего газа, с получением каталитической смеси без кокса; и (b) контактирование каталитической смеси без кокса с паром при температуре в интервале от 100 до 300°C с получением регенерированной каталитической смеси.
2. Способ по п.1, в котором стадию (b) выполняют при температуре в интервале от 150 до 250°C.
3. Способ по п.1, в котором катализатор изомеризации содержит 95 мас.% оксида магния.
4. Способ по п.1, в котором катализатор метатезиса содержит оксид вольфрама.
5. Способ по п.4, в котором неорганический носитель является кремнеземом.
6. Способ по п.1, в котором использованную каталитическую смесь извлекают из процесса получения пропилена из линейного бутена и этилена.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/317,873 US8722557B2 (en) | 2008-12-30 | 2008-12-30 | Catalyst regeneration |
US12/317,873 | 2008-12-30 | ||
PCT/US2009/006147 WO2010077265A1 (en) | 2008-12-30 | 2009-11-17 | Catalyst regeneration |
Publications (2)
Publication Number | Publication Date |
---|---|
RU2011132046A true RU2011132046A (ru) | 2013-02-10 |
RU2503499C2 RU2503499C2 (ru) | 2014-01-10 |
Family
ID=41466974
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
RU2011132046/04A RU2503499C2 (ru) | 2008-12-30 | 2009-11-17 | Регенерация катализатора |
Country Status (11)
Country | Link |
---|---|
US (1) | US8722557B2 (ru) |
EP (1) | EP2370208A1 (ru) |
JP (2) | JP2012513895A (ru) |
KR (1) | KR101668504B1 (ru) |
CN (1) | CN102316984A (ru) |
BR (1) | BRPI0923732B1 (ru) |
CA (1) | CA2748338C (ru) |
MX (1) | MX2011007098A (ru) |
RU (1) | RU2503499C2 (ru) |
SG (1) | SG172406A1 (ru) |
WO (1) | WO2010077265A1 (ru) |
Families Citing this family (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8722557B2 (en) * | 2008-12-30 | 2014-05-13 | Lyondell Chemical Technology, L.P. | Catalyst regeneration |
JP5499918B2 (ja) * | 2009-06-05 | 2014-05-21 | 三菱化学株式会社 | 触媒の再生方法 |
CN103537271B (zh) * | 2012-07-12 | 2015-07-08 | 中国石油化工股份有限公司 | 烯烃异构化催化剂的再生方法 |
JP5959658B2 (ja) | 2012-10-06 | 2016-08-02 | クラリアント触媒株式会社 | オレフィンメタセシス反応用混合触媒およびその製造方法並びにそれを用いたプロピレン製造方法 |
EP2829317A1 (en) * | 2013-07-23 | 2015-01-28 | Borealis AG | Improved catalyst bed configuration for olefin production |
EP2848300A1 (en) | 2013-09-13 | 2015-03-18 | Borealis AG | Process for olefin production by metathesis and reactor system therefore |
EP2862629A1 (en) | 2013-10-15 | 2015-04-22 | Borealis AG | Catalyst and process for olefin metathesis reaction |
EP2873459A1 (en) | 2013-11-14 | 2015-05-20 | Borealis AG | Catalyst bed configuration for olefin conversion and process for obtaining olefins |
EP2886189A1 (en) | 2013-12-20 | 2015-06-24 | Borealis AG | Process for olefin production by metathesis and reactor system therefor |
EP2891643A1 (en) | 2014-01-02 | 2015-07-08 | Borealis AG | Process for obtaining olefins by metathesis |
WO2016038570A2 (en) * | 2014-09-11 | 2016-03-17 | Reliance Industries Limited | A ziegler-natta catalyst composition for preparing polyehtylene |
US9815753B2 (en) | 2014-09-15 | 2017-11-14 | Northwestern University | Supported metal oxides for olefin metathesis and related methods |
SG11201702901VA (en) | 2014-10-28 | 2017-05-30 | Smh Co Ltd | Metathesis catalyst on mixed metal oxide-zeolite support and process for use thereof |
EP3238819B1 (en) | 2015-03-20 | 2020-11-04 | SMH Co., Ltd. | Process for olefin metathesis |
RU168779U1 (ru) * | 2016-03-01 | 2017-02-17 | Общество с ограниченной ответственностью "ПромСинтез" (ООО "ПромСинтез") | Установка для регенерации катализатора гидрообработки |
US10407363B2 (en) | 2017-08-16 | 2019-09-10 | Saudi Arabian Oil Company | Steam-less process for converting butenes to 1,3-butadiene |
EP3668644A1 (en) * | 2017-08-17 | 2020-06-24 | Saudi Arabian Oil Company | Aerosol processing method for controlled coating of surface species to generate catalysts |
KR102283123B1 (ko) * | 2018-11-30 | 2021-07-28 | 주식회사 엘지화학 | 부타디엔의 제조방법 |
CN112691706A (zh) * | 2020-12-23 | 2021-04-23 | 中触媒新材料股份有限公司 | 一种乙醇制乙腈催化剂的再生方法 |
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US8722557B2 (en) * | 2008-12-30 | 2014-05-13 | Lyondell Chemical Technology, L.P. | Catalyst regeneration |
-
2008
- 2008-12-30 US US12/317,873 patent/US8722557B2/en active Active
-
2009
- 2009-11-17 KR KR1020117015023A patent/KR101668504B1/ko active IP Right Grant
- 2009-11-17 WO PCT/US2009/006147 patent/WO2010077265A1/en active Application Filing
- 2009-11-17 JP JP2011544406A patent/JP2012513895A/ja active Pending
- 2009-11-17 MX MX2011007098A patent/MX2011007098A/es active IP Right Grant
- 2009-11-17 BR BRPI0923732-1A patent/BRPI0923732B1/pt active IP Right Grant
- 2009-11-17 CN CN2009801535684A patent/CN102316984A/zh active Pending
- 2009-11-17 SG SG2011047164A patent/SG172406A1/en unknown
- 2009-11-17 RU RU2011132046/04A patent/RU2503499C2/ru active
- 2009-11-17 EP EP09761051A patent/EP2370208A1/en not_active Withdrawn
- 2009-11-17 CA CA2748338A patent/CA2748338C/en active Active
-
2015
- 2015-02-02 JP JP2015018273A patent/JP5828975B2/ja active Active
Also Published As
Publication number | Publication date |
---|---|
SG172406A1 (en) | 2011-07-28 |
CA2748338C (en) | 2016-07-05 |
KR101668504B1 (ko) | 2016-10-21 |
US20100167911A1 (en) | 2010-07-01 |
BRPI0923732A2 (pt) | 2016-01-19 |
KR20110107332A (ko) | 2011-09-30 |
WO2010077265A1 (en) | 2010-07-08 |
RU2503499C2 (ru) | 2014-01-10 |
JP5828975B2 (ja) | 2015-12-09 |
MX2011007098A (es) | 2011-11-18 |
BRPI0923732B1 (pt) | 2018-02-06 |
JP2015145004A (ja) | 2015-08-13 |
EP2370208A1 (en) | 2011-10-05 |
JP2012513895A (ja) | 2012-06-21 |
CA2748338A1 (en) | 2010-07-08 |
CN102316984A (zh) | 2012-01-11 |
US8722557B2 (en) | 2014-05-13 |
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