RU2008140381A - Состав катализатора для уменьшения содержания серы в бензине в процессе каталитического крекинга - Google Patents
Состав катализатора для уменьшения содержания серы в бензине в процессе каталитического крекинга Download PDFInfo
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- RU2008140381A RU2008140381A RU2008140381/04A RU2008140381A RU2008140381A RU 2008140381 A RU2008140381 A RU 2008140381A RU 2008140381/04 A RU2008140381/04 A RU 2008140381/04A RU 2008140381 A RU2008140381 A RU 2008140381A RU 2008140381 A RU2008140381 A RU 2008140381A
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- Prior art keywords
- catalyst
- sulfur content
- metal
- vanadium
- carrier
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- 239000003054 catalyst Substances 0.000 title claims abstract 16
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 title claims abstract 14
- 238000000034 method Methods 0.000 title claims abstract 14
- 229910052717 sulfur Inorganic materials 0.000 title claims abstract 14
- 239000011593 sulfur Substances 0.000 title claims abstract 14
- 239000000203 mixture Substances 0.000 title claims abstract 7
- 238000004523 catalytic cracking Methods 0.000 title claims abstract 4
- 229910052751 metal Inorganic materials 0.000 claims abstract 11
- 239000002184 metal Substances 0.000 claims abstract 11
- 229910052720 vanadium Inorganic materials 0.000 claims abstract 10
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 claims abstract 10
- -1 vanadate compound Chemical class 0.000 claims abstract 5
- 229910021536 Zeolite Inorganic materials 0.000 claims abstract 4
- 150000001450 anions Chemical class 0.000 claims abstract 4
- 239000007864 aqueous solution Substances 0.000 claims abstract 4
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical group O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract 4
- 239000010457 zeolite Substances 0.000 claims abstract 4
- 238000001354 calcination Methods 0.000 claims abstract 3
- 239000002253 acid Substances 0.000 claims abstract 2
- 125000005210 alkyl ammonium group Chemical group 0.000 claims abstract 2
- 229910052782 aluminium Inorganic materials 0.000 claims abstract 2
- UNTBPXHCXVWYOI-UHFFFAOYSA-O azanium;oxido(dioxo)vanadium Chemical compound [NH4+].[O-][V](=O)=O UNTBPXHCXVWYOI-UHFFFAOYSA-O 0.000 claims abstract 2
- 150000001768 cations Chemical class 0.000 claims abstract 2
- 229910052802 copper Inorganic materials 0.000 claims abstract 2
- 229910052749 magnesium Inorganic materials 0.000 claims abstract 2
- 229910052748 manganese Inorganic materials 0.000 claims abstract 2
- 150000002739 metals Chemical class 0.000 claims abstract 2
- 229910052759 nickel Inorganic materials 0.000 claims abstract 2
- 229910052761 rare earth metal Inorganic materials 0.000 claims abstract 2
- 150000002910 rare earth metals Chemical class 0.000 claims abstract 2
- 239000000243 solution Substances 0.000 claims abstract 2
- 239000000126 substance Substances 0.000 claims abstract 2
- 229910052727 yttrium Inorganic materials 0.000 claims abstract 2
- 229910052725 zinc Inorganic materials 0.000 claims abstract 2
- 229910052726 zirconium Inorganic materials 0.000 claims abstract 2
- 239000007858 starting material Substances 0.000 claims 2
- LSGOVYNHVSXFFJ-UHFFFAOYSA-N vanadate(3-) Chemical compound [O-][V]([O-])([O-])=O LSGOVYNHVSXFFJ-UHFFFAOYSA-N 0.000 claims 2
- 239000004215 Carbon black (E152) Substances 0.000 claims 1
- 230000015572 biosynthetic process Effects 0.000 claims 1
- 239000000969 carrier Substances 0.000 claims 1
- 229930195733 hydrocarbon Natural products 0.000 claims 1
- 150000002430 hydrocarbons Chemical class 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims 1
- 238000000151 deposition Methods 0.000 abstract 2
- 239000000908 ammonium hydroxide Substances 0.000 abstract 1
- 230000008021 deposition Effects 0.000 abstract 1
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- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
- B01J29/085—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead
- B01J29/088—Y-type faujasite
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- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
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- 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
- B01J23/20—Vanadium, niobium or tantalum
- B01J23/22—Vanadium
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- 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
- B01J23/32—Manganese, technetium or rhenium
- B01J23/34—Manganese
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- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/847—Vanadium, niobium or tantalum or polonium
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- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/847—Vanadium, niobium or tantalum or polonium
- B01J23/8472—Vanadium
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- B01J29/00—Catalysts comprising molecular sieves
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- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
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- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
- B01J29/10—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y containing iron group metals, noble metals or copper
- B01J29/106—Y-type faujasite
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- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
- B01J29/16—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J29/166—Y-type faujasite
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0201—Impregnation
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- 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
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- C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
- C10G11/04—Oxides
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- 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
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- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/16—After treatment, characterised by the effect to be obtained to increase the Si/Al ratio; Dealumination
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- B01J2229/18—After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself
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Abstract
1. Катализатор для уменьшения содержания серы в флюидизированном продукте каталитического крекинга, состоящий из: ! (i) носителя, ! (ii) соединения металл-ванадата, находящегося на носителе. ! 2. Катализатор для уменьшения содержания серы по п.1, который отличается тем, что металл в составе данного металл-ванадата - это один или несколько металлов, выбранных из редкоземельных металлов, Zn, Mn, Zr, Al, Mg, Ni, и Cu. ! 3. Катализатор для уменьшения содержания серы по п.1, который отличается тем, что носитель - это цеолит, выбранный из группы, состоящей из Y, USY, REY, REUSY, бета цеолита, ZSM-5, и смесей этих веществ. ! 4. Катализатор для уменьшения содержания серы по п.1, который содержит вплоть до 15 мас.%, от всей массы катализатора, соединения металл-ванадата. ! 5. Катализатор для уменьшения содержания серы по п.3, который отличается тем, что атомное соотношение ванадия на поверхности носителя и ванадия в основной части носителя больше, чем 1,5. ! 6. Метод получения состава катализатора для уменьшения содержания серы, который состоит в нанесении как минимум одного аниона, содержащего ванадий, на носитель с последующим кальцинированием этих носителей. ! 7. Метод по п.6, который отличается тем, что анион, содержащий ванадий, - это водный раствор метаванадата аммония, а метод также включает добавление основания и/или кислоты к данному водному раствору для достижения необходимого рН раствора. ! 8. Метод по п.7, который отличается тем, что основание - это гидроокись алкиламмония. ! 9. Метод по п.6, который включает нанесение как минимум одного катиона металла, кроме ванадия, на вышеупомянутый носитель и образование металл-ванадата на вышеупомянутом носителе во вре
Claims (11)
1. Катализатор для уменьшения содержания серы в флюидизированном продукте каталитического крекинга, состоящий из:
(i) носителя,
(ii) соединения металл-ванадата, находящегося на носителе.
2. Катализатор для уменьшения содержания серы по п.1, который отличается тем, что металл в составе данного металл-ванадата - это один или несколько металлов, выбранных из редкоземельных металлов, Zn, Mn, Zr, Al, Mg, Ni, и Cu.
3. Катализатор для уменьшения содержания серы по п.1, который отличается тем, что носитель - это цеолит, выбранный из группы, состоящей из Y, USY, REY, REUSY, бета цеолита, ZSM-5, и смесей этих веществ.
4. Катализатор для уменьшения содержания серы по п.1, который содержит вплоть до 15 мас.%, от всей массы катализатора, соединения металл-ванадата.
5. Катализатор для уменьшения содержания серы по п.3, который отличается тем, что атомное соотношение ванадия на поверхности носителя и ванадия в основной части носителя больше, чем 1,5.
6. Метод получения состава катализатора для уменьшения содержания серы, который состоит в нанесении как минимум одного аниона, содержащего ванадий, на носитель с последующим кальцинированием этих носителей.
7. Метод по п.6, который отличается тем, что анион, содержащий ванадий, - это водный раствор метаванадата аммония, а метод также включает добавление основания и/или кислоты к данному водному раствору для достижения необходимого рН раствора.
8. Метод по п.7, который отличается тем, что основание - это гидроокись алкиламмония.
9. Метод по п.6, который включает нанесение как минимум одного катиона металла, кроме ванадия, на вышеупомянутый носитель и образование металл-ванадата на вышеупомянутом носителе во время кальцинирования.
10. Метод по п.6, который включает обработку вышеупомянутого носителя основанием, как упомянуто выше.
11. Процесс каталитического крекинга углеводородных исходных соединений с получением продуктов, которые включают бензин, где упомянутый процесс включает взаимодействие вышеупомянутого исходного соединения с катализатором для уменьшения содержания серы, который состоит из соединения металл-ванадата, находящегося на носителе.
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US78249306P | 2006-03-15 | 2006-03-15 | |
US60/782,493 | 2006-03-15 |
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RU2008140381A true RU2008140381A (ru) | 2010-04-20 |
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RU2008140381/04A RU2008140381A (ru) | 2006-03-15 | 2007-03-06 | Состав катализатора для уменьшения содержания серы в бензине в процессе каталитического крекинга |
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US (2) | US7960307B2 (ru) |
EP (1) | EP1993726B1 (ru) |
KR (1) | KR101444472B1 (ru) |
CN (1) | CN101855013B (ru) |
AU (1) | AU2007227684A1 (ru) |
BR (1) | BRPI0708885B1 (ru) |
CA (1) | CA2645839C (ru) |
MX (1) | MX2008011635A (ru) |
MY (1) | MY146107A (ru) |
RU (1) | RU2008140381A (ru) |
TW (1) | TW200800394A (ru) |
WO (1) | WO2007108939A2 (ru) |
Families Citing this family (10)
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EP1993726B1 (en) * | 2006-03-15 | 2013-11-20 | BASF Corporation | Catalyst composition reducing gasoline sulfur content in catalytic cracking process |
US8148290B2 (en) * | 2006-06-27 | 2012-04-03 | Basf Corporation | Diesel exhaust treatment system catalyst monitoring |
US20090230023A1 (en) * | 2006-06-28 | 2009-09-17 | Idemitsu Kosan Co., Ltd. | Fluid catalytic cracking catalyst having desulfurizing functions, process for production of the same, and process for production of low-sulfur catalytically cracked gasoline with the catalyst |
TWI478767B (zh) * | 2009-04-23 | 2015-04-01 | Treibacher Ind Ag | 用於使廢氣進行選擇性催化還原反應之催化劑組成物 |
KR101821406B1 (ko) * | 2010-04-16 | 2018-01-23 | 트라이바허 인두스트리 아게 | 배기 가스의 선택적 촉매 환원을 위한 촉매 조성물 |
JP5490074B2 (ja) * | 2010-12-28 | 2014-05-14 | トヨタ自動車株式会社 | 三酸化硫黄分解用触媒、及び水素生成方法 |
JP5497688B2 (ja) | 2011-05-25 | 2014-05-21 | トヨタ自動車株式会社 | 三酸化硫黄分解用触媒、及び水素生成方法 |
SG188753A1 (en) * | 2011-09-30 | 2013-04-30 | Bharat Petroleum Corp Ltd | Sulphur reduction catalyst additive composition in fluid catalytic cracking and method of preparation thereof |
JP6074559B2 (ja) | 2012-05-25 | 2017-02-08 | サウジ アラビアン オイル カンパニー | 流動接触分解においてプロピレンを増強させるための触媒 |
RU2729422C1 (ru) * | 2019-10-24 | 2020-08-06 | ФЕДЕРАЛЬНОЕ ГОСУДАРСТВЕННОЕ БЮДЖЕТНОЕ УЧРЕЖДЕНИЕ НАУКИ ИНСТИТУТ ОРГАНИЧЕСКОЙ ХИМИИ им. Н.Д. ЗЕЛИНСКОГО РОССИЙСКОЙ АКАДЕМИИ НАУК (ИОХ РАН) | Катализатор для удаления оксидов серы из дымовых газов электростанций |
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US4824815A (en) * | 1985-06-11 | 1989-04-25 | Exxon Research And Engineering Company | Cracking catalysts containing strontium carbonate |
BR8707259A (pt) | 1986-04-07 | 1988-04-19 | Katalistiks Int Inc | Composicao aperfeicoada de espinelio contendo terra para e vanadio e processo para sua utilizacao |
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US6036847A (en) | 1996-03-26 | 2000-03-14 | W. R. Grace & Co.-Conn. | Compositions for use in catalytic cracking to make reduced sulfur content gasoline |
US6846403B2 (en) | 1998-12-28 | 2005-01-25 | Mobil Oil Corporation | Gasoline sulfur reduction in fluid catalytic cracking |
US6852214B1 (en) * | 1998-08-31 | 2005-02-08 | Mobil Oil Corporation | Gasoline sulfur reduction in fluid catalytic cracking |
US20020153283A1 (en) * | 1998-12-28 | 2002-10-24 | Arthur W Chester | Gasoline sulfur reduction in fluid catalytic cracking |
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DK176408B1 (da) * | 1998-12-28 | 2007-12-17 | Mobil Oil Corp | Benzinsvovl-reduktion i fluid-katalytisk krakning |
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CN1122703C (zh) * | 1998-12-29 | 2003-10-01 | 中国石油化工集团公司 | 用于烃类催化裂化的一种助剂及其使用方法 |
BR0014102B1 (pt) * | 1999-09-20 | 2011-06-14 | reduÇço do teor de enxofre em gasolina em craqueamento catalÍtico fluido. | |
US6635169B1 (en) | 1999-09-20 | 2003-10-21 | Mobil Oil Corporation | Method for reducing gasoline sulfur in fluid catalytic cracking |
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US6635168B2 (en) * | 2001-04-13 | 2003-10-21 | W. R. Grace & Co.-Conn | Gasoline sulfur reduction catalyst for fluid catalytic cracking process |
US7153413B2 (en) | 2001-07-10 | 2006-12-26 | W.R. Grace &Co.-Conn. | Gasoline sulfur reduction in fluid catalytic cracking |
US7138358B2 (en) * | 2001-11-13 | 2006-11-21 | Sud-Chemie Inc. | Catalyzed diesel particulate matter filter with improved thermal stability |
KR100972705B1 (ko) | 2002-06-28 | 2010-07-28 | 알베마를 네덜란드 비.브이. | 가솔린 및 디젤 중의 황 함량을 감소시키기 위한 fcc촉매 |
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CN1261216C (zh) | 2003-05-30 | 2006-06-28 | 中国石油化工股份有限公司 | 一种含分子筛的烃类裂化催化剂及其制备方法 |
EP1656200A1 (en) * | 2003-08-21 | 2006-05-17 | BP Chemicals Limited | Catalyst composition and use thereof in ethane oxidation |
US8084383B2 (en) | 2004-03-16 | 2011-12-27 | W.R. Grace & Co.-Conn. | Gasoline sulfur reduction catalyst for fluid catalytic cracking process |
US20060198774A1 (en) * | 2005-03-03 | 2006-09-07 | Cross Joseph B | Mercury Removal sorbent |
EP1993726B1 (en) * | 2006-03-15 | 2013-11-20 | BASF Corporation | Catalyst composition reducing gasoline sulfur content in catalytic cracking process |
US20090230023A1 (en) | 2006-06-28 | 2009-09-17 | Idemitsu Kosan Co., Ltd. | Fluid catalytic cracking catalyst having desulfurizing functions, process for production of the same, and process for production of low-sulfur catalytically cracked gasoline with the catalyst |
-
2007
- 2007-03-06 EP EP07752504.6A patent/EP1993726B1/en not_active Not-in-force
- 2007-03-06 RU RU2008140381/04A patent/RU2008140381A/ru not_active Application Discontinuation
- 2007-03-06 MY MYPI20083570A patent/MY146107A/en unknown
- 2007-03-06 CA CA2645839A patent/CA2645839C/en not_active Expired - Fee Related
- 2007-03-06 BR BRPI0708885A patent/BRPI0708885B1/pt not_active IP Right Cessation
- 2007-03-06 AU AU2007227684A patent/AU2007227684A1/en not_active Abandoned
- 2007-03-06 KR KR1020087025029A patent/KR101444472B1/ko active IP Right Grant
- 2007-03-06 US US11/714,357 patent/US7960307B2/en not_active Expired - Fee Related
- 2007-03-06 WO PCT/US2007/005812 patent/WO2007108939A2/en active Application Filing
- 2007-03-06 CN CN2007800135420A patent/CN101855013B/zh not_active Expired - Fee Related
- 2007-03-06 MX MX2008011635A patent/MX2008011635A/es active IP Right Grant
- 2007-03-13 TW TW096108619A patent/TW200800394A/zh unknown
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2011
- 2011-02-23 US US13/032,787 patent/US8449762B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
AU2007227684A1 (en) | 2007-09-27 |
US7960307B2 (en) | 2011-06-14 |
EP1993726A2 (en) | 2008-11-26 |
CN101855013A (zh) | 2010-10-06 |
US20110139684A1 (en) | 2011-06-16 |
WO2007108939A2 (en) | 2007-09-27 |
BRPI0708885B1 (pt) | 2016-07-26 |
EP1993726B1 (en) | 2013-11-20 |
CA2645839C (en) | 2016-08-16 |
BRPI0708885A2 (pt) | 2011-06-14 |
WO2007108939A3 (en) | 2008-01-24 |
US8449762B2 (en) | 2013-05-28 |
MY146107A (en) | 2012-06-29 |
MX2008011635A (es) | 2008-10-17 |
TW200800394A (en) | 2008-01-01 |
KR20090004963A (ko) | 2009-01-12 |
US20070249495A1 (en) | 2007-10-25 |
CN101855013B (zh) | 2013-05-01 |
KR101444472B1 (ko) | 2014-09-24 |
CA2645839A1 (en) | 2007-09-27 |
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