AR072884A1 - Aditivo con sistema multiple de zeolitas para unidades de craqueo catalitico fluido y metodo de preparacion - Google Patents
Aditivo con sistema multiple de zeolitas para unidades de craqueo catalitico fluido y metodo de preparacionInfo
- Publication number
- AR072884A1 AR072884A1 ARP090102893A ARP090102893A AR072884A1 AR 072884 A1 AR072884 A1 AR 072884A1 AR P090102893 A ARP090102893 A AR P090102893A AR P090102893 A ARP090102893 A AR P090102893A AR 072884 A1 AR072884 A1 AR 072884A1
- Authority
- AR
- Argentina
- Prior art keywords
- additive
- fluid catalytic
- units
- zeolites
- preparation
- Prior art date
Links
- 239000000654 additive Substances 0.000 title abstract 4
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title abstract 4
- 239000010457 zeolite Substances 0.000 title abstract 4
- 230000000996 additive effect Effects 0.000 title abstract 2
- 230000003197 catalytic effect Effects 0.000 title 1
- 239000012530 fluid Substances 0.000 title 1
- 238000002360 preparation method Methods 0.000 title 1
- 229910021536 Zeolite Inorganic materials 0.000 abstract 3
- QQONPFPTGQHPMA-UHFFFAOYSA-N Propene Chemical compound CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 abstract 2
- 150000001336 alkenes Chemical class 0.000 abstract 2
- 239000003054 catalyst Substances 0.000 abstract 2
- 238000004519 manufacturing process Methods 0.000 abstract 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 abstract 1
- 238000004231 fluid catalytic cracking Methods 0.000 abstract 1
- 239000011159 matrix material Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 239000002245 particle Substances 0.000 abstract 1
- 229910052698 phosphorus Inorganic materials 0.000 abstract 1
- 239000011574 phosphorus Substances 0.000 abstract 1
Classifications
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- 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
- 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
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
-
- 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
- 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
- B01J29/80—Mixtures of different zeolites
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
- B01J37/0027—Powdering
- B01J37/0045—Drying a slurry, e.g. spray drying
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/04—Mixing
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/28—Phosphorising
-
- 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/30—After treatment, characterised by the means used
- B01J2229/42—Addition of matrix or binder particles
-
- 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
- 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
- B01J29/084—Y-type faujasite
-
- 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
- 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
- B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/613—10-100 m2/g
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
- B01J35/647—2-50 nm
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
- B01J35/651—50-500 nm
-
- 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/20—C2-C4 olefins
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
Se han descripto aditivos para mezclar al inventario de catalizador en unidades de proceso de craqueo catalítico fluido - FCC para maximizar la produccion de GLP y de olefinas livianas. Tales aditivos comprenden una matriz que tiene incorporados una zeolita de tipo MFI, preferiblemente zeolita ZSM-5, una zeolita de tipo Y, y una fuente de fosforo, en una unica partícula. La mezcla de aditivo en proporciones de 1,0 a 40% en masa al catalizador de equilibrio de una unidad de FCC maximiza la produccion de GLP y de olefinas livianas, principalmente propeno.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BRPI0803617-9A BRPI0803617A2 (pt) | 2008-09-19 | 2008-09-19 | Aditivo com sistema múltiplo de zeólitas e método de preparo |
Publications (1)
Publication Number | Publication Date |
---|---|
AR072884A1 true AR072884A1 (es) | 2010-09-29 |
Family
ID=41445423
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP090102893A AR072884A1 (es) | 2008-09-19 | 2009-07-29 | Aditivo con sistema multiple de zeolitas para unidades de craqueo catalitico fluido y metodo de preparacion |
Country Status (7)
Country | Link |
---|---|
US (1) | US20110207984A1 (es) |
EP (1) | EP2350234A1 (es) |
JP (2) | JP5662936B2 (es) |
CN (1) | CN102131899B (es) |
AR (1) | AR072884A1 (es) |
BR (1) | BRPI0803617A2 (es) |
WO (1) | WO2010032025A1 (es) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BRPI0803617A2 (pt) * | 2008-09-19 | 2010-06-15 | Petroleo Brasileiro Sa | Aditivo com sistema múltiplo de zeólitas e método de preparo |
KR20120029429A (ko) * | 2009-05-19 | 2012-03-26 | 쉘 인터내셔날 리써취 마트샤피지 비.브이. | 배합 산소화물 전환 촉매의 제조 방법, 배합 산소화물 전환 촉매 및 올레핀계 생성물의 제조 방법 |
EP2855012B1 (en) | 2012-05-25 | 2019-06-26 | Saudi Arabian Oil Company | Catalyst for enhanced propylene in fluidized catalytic cracking |
CN103447063B (zh) * | 2012-06-01 | 2016-02-10 | 中国石油天然气股份有限公司 | 重油高效转化催化裂化催化剂及其制备方法 |
US8895790B2 (en) | 2013-02-12 | 2014-11-25 | Saudi Basic Industries Corporation | Conversion of plastics to olefin and aromatic products |
US9428695B2 (en) | 2013-02-12 | 2016-08-30 | Saudi Basic Industries Corporation | Conversion of plastics to olefin and aromatic products with product recycle |
US9447332B2 (en) | 2013-02-12 | 2016-09-20 | Saudi Basic Industries Corporation | Conversion of plastics to olefin and aromatic products using temperature control |
CN104096590B (zh) * | 2013-04-10 | 2016-09-14 | 上海碧科清洁能源技术有限公司 | 混合分子筛催化剂及其制备方法和应用 |
CN105983400B (zh) * | 2015-01-28 | 2018-07-13 | 中国石油天然气股份有限公司 | 一种中孔氧化铝粘结剂的制备方法及其在重油催化裂化催化剂中的应用 |
CN108025298B (zh) | 2015-07-23 | 2021-07-06 | 雅宝公司 | Fcc催化剂添加剂和粘合剂 |
KR20200026792A (ko) * | 2017-04-10 | 2020-03-11 | 릴라이언스 인더스트리즈 리미티드 | Fcc 촉매 첨가제 및 그의 제조 방법 |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3758403A (en) * | 1970-10-06 | 1973-09-11 | Mobil Oil | Olites catalytic cracking of hydrocarbons with mixture of zsm-5 and other ze |
AU595706B2 (en) * | 1987-06-11 | 1990-04-05 | Mobil Oil Corporation | Integrated process for gasoline production |
US5456821A (en) * | 1991-03-12 | 1995-10-10 | Mobil Oil Corp. | Catalytic conversion with improved catalyst |
JPH06313176A (ja) * | 1993-03-02 | 1994-11-08 | Nippon Oil Co Ltd | 重質油の流動接触分解法 |
US5472594A (en) * | 1994-07-18 | 1995-12-05 | Texaco Inc. | FCC process for producing enhanced yields of C4 /C5 olefins |
DE69832938T2 (de) * | 1997-10-15 | 2006-08-10 | China Petro-Chemical Corp. | Krackkatalysator für die Produktion von leichten Olefinen und dessen Herstellung |
EP1116775A1 (en) * | 2000-01-12 | 2001-07-18 | Akzo Nobel N.V. | Catalyst composition with high efficiency for the production of light olefins |
ES2168208B1 (es) * | 2000-03-24 | 2003-04-01 | Univ Valencia Politecnica | Catalizadores de craqueo basados en zeolitas. |
US6858556B2 (en) * | 2002-02-25 | 2005-02-22 | Indian Oil Corporation Limited | Stabilized dual zeolite single particle catalyst composition and a process thereof |
AR052122A1 (es) * | 2004-11-05 | 2007-03-07 | Grace W R & Co | Catalizadores para olefinas livianas y glp gas licuado de petroleo en unidades de craqueo catalitico fluidizado |
JP5008666B2 (ja) * | 2006-06-28 | 2012-08-22 | 出光興産株式会社 | 脱硫機能付加流動接触分解触媒及びその製造方法並びに該脱硫機能付加流動接触分解触媒を用いた低硫黄接触分解ガソリンの製造方法 |
BRPI0602678B1 (pt) * | 2006-07-14 | 2015-09-01 | Petroleo Brasileiro Sa | Aditivo para maximização de glp e propeno adequado a operação da unidade de craqueamento catalítico fluido em baixa severidade e processo de preparo do mesmo |
US9701914B2 (en) * | 2006-11-07 | 2017-07-11 | Saudi Arabian Oil Company | Advanced control of severe fluid catalytic cracking process for maximizing propylene production from petroleum feedstock |
BRPI0803617A2 (pt) * | 2008-09-19 | 2010-06-15 | Petroleo Brasileiro Sa | Aditivo com sistema múltiplo de zeólitas e método de preparo |
-
2008
- 2008-09-19 BR BRPI0803617-9A patent/BRPI0803617A2/pt not_active Application Discontinuation
-
2009
- 2009-07-29 AR ARP090102893A patent/AR072884A1/es not_active Application Discontinuation
- 2009-09-18 WO PCT/GB2009/002254 patent/WO2010032025A1/en active Application Filing
- 2009-09-18 US US13/059,377 patent/US20110207984A1/en not_active Abandoned
- 2009-09-18 CN CN200980133030.7A patent/CN102131899B/zh not_active Expired - Fee Related
- 2009-09-18 EP EP09785144A patent/EP2350234A1/en not_active Withdrawn
- 2009-09-18 JP JP2011527400A patent/JP5662936B2/ja not_active Expired - Fee Related
-
2014
- 2014-09-12 JP JP2014186714A patent/JP5860516B2/ja not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
WO2010032025A1 (en) | 2010-03-25 |
JP5860516B2 (ja) | 2016-02-16 |
JP5662936B2 (ja) | 2015-02-04 |
CN102131899B (zh) | 2016-05-18 |
JP2012503065A (ja) | 2012-02-02 |
US20110207984A1 (en) | 2011-08-25 |
BRPI0803617A2 (pt) | 2010-06-15 |
EP2350234A1 (en) | 2011-08-03 |
JP2015063686A (ja) | 2015-04-09 |
CN102131899A (zh) | 2011-07-20 |
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Legal Events
Date | Code | Title | Description |
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FC | Refusal |