SG11201811402SA - Processes for high severity fluid catalytic cracking systems - Google Patents

Processes for high severity fluid catalytic cracking systems

Info

Publication number
SG11201811402SA
SG11201811402SA SG11201811402SA SG11201811402SA SG11201811402SA SG 11201811402S A SG11201811402S A SG 11201811402SA SG 11201811402S A SG11201811402S A SG 11201811402SA SG 11201811402S A SG11201811402S A SG 11201811402SA SG 11201811402S A SG11201811402S A SG 11201811402SA
Authority
SG
Singapore
Prior art keywords
dhahran
international
oil company
catalyst
gas condensate
Prior art date
Application number
SG11201811402SA
Inventor
Mansour Ali Al-Herz
Nathan Hould
Ahmed Al-Asseel
Wala Algozeeb
Musaed Al-Ghrami
Original Assignee
Saudi Arabian Oil Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Saudi Arabian Oil Co filed Critical Saudi Arabian Oil Co
Publication of SG11201811402SA publication Critical patent/SG11201811402SA/en

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
    • C07C4/06—Catalytic processes
    • 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
    • C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04—Oxides
    • C10G11/05—Crystalline alumino-silicates, e.g. molecular sieves
    • 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
    • B01J29/085—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
    • 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
    • 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
    • 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
    • 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
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00—Catalysts comprising molecular sieves
    • C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
    • C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • C07C2529/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00—Catalysts comprising molecular sieves
    • C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
    • C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • C07C2529/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00—Catalysts comprising molecular sieves
    • C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
    • C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • C07C2529/80—Mixtures of different zeolites
    • 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)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

INTERNATIONAL APPLICATION PUBLISHED UNDER THE PATENT COOPERATION TREATY (PCT) (19) World Intellectual Property 111111H111011111111111111111111111111111011011110110111110111111111111111011111 Organization International Bureau (10) International Publication Number (43) International Publication Date ......0\"\"1 WO 2017/223310 Al 28 December 2017 (28.12.2017) WIP0 I PCT (51) International Patent Classification: di Arabian Oil Company, Post Office Box 5000, Dhahran, ClOG 11/05 (2006.01) B01J 29/40 (2006.01) 31311 (SA). AL-GHRAMI, Musaed; c/o Saudi Arabian ClOG 11/18 (2006.01) Oil Company, Post Office Box 5000, Dhahran, 31311 (SA). (21) International Application Number: (74) Agent: MOLLOY, Matthew A. et al.; Dinsmore & Shohl PCT/US2017/038740 LLP, One South Main Street, Fifth Third Center - Suite 1300, Dayton, Ohio 45402 (US). (22) International Filing Date: 22 June 2017 (22.06.2017) (81) Designated States (unless otherwise indicated, for every (25) Filing Language: English kind of national protection available): AE, AG, AL, AM, AO, AT, AU, AZ, BA, BB, BG, BH, BN, BR, BW, BY, BZ, (26) Publication Language: English CA, CH, CL, CN, CO, CR, CU, CZ, DE, DJ, DK, DM, DO, (30) Priority Data: DZ, EC, EE, EG, ES, FI, GB, GD, GE, GH, GM, GT, HN, 15/190,327 23 June 2016 (23.06.2016) US HR, HU, ID, IL, IN, IR, IS, JO, JP, KE, KG, KH, KN, KP, KR, KW, KZ, LA, LC, LK, LR, LS, LU, LY, MA, MD, ME, (71) Applicant: SAUDI ARABIAN OIL COMPANY MG, MK, MN, MW, MX, MY, MZ, NA, NG, NI, NO, NZ, [SA/SA]; Post Office Box 5000, Dhahran, 31311 (SA). OM, PA, PE, PG, PH, PL, PT, QA, RO, RS, RU, RW, SA, SC, SD, SE, SG, SK, SL, SM, ST, SV, SY, TH, TJ, TM, TN, (71) Applicant (for AG only): ARAMCO SERVICES COM- TR, TT, TZ, UA, UG, US, UZ, VC, VN, ZA, ZM, ZW. PANY [US/US]; 9009 West Loop South, Houston, Texas 77096 (US). (84) Designated States (unless otherwise indicated, for every kind of regional protection available): ARIPO (BW, GH, (72) Inventors: AL-HERZ, Mansour Ali; c/o Saudi Arabi- GM, KE, LR, LS, MW, MZ, NA, RW, SD, SL, ST, SZ, TZ, an Oil Company, Post Office Box 5000, Dhahran, 31311 = UG, ZM, ZW), Eurasian (AM, AZ, BY, KG, KZ, RU, TJ, (SA). HOULD, Nathan; c/o Saudi Arabian Oil Company, TM), European (AL, AT, BE, BG, CH, CY, CZ, DE, DK, = Post Office Box 5000, Dhahran, 31311 (SA). AL-ASSEEL, EE, ES, FI, FR, GB, GR, HR, HU, IE, IS, IT, LT, LU, LV, Ahmed; c/o Saudi Arabian Oil Company, Post OfficeBox —MC, MK, MT, NL, NO, PL, PT, RO, RS, SE, SI, SK, SM, = 5000, Dhahran, 31311 (SA). ALGOZEEB, Wala; c/o Sau- = = (54) Title: = = = 11O >\ = AM I PROCESSES FOR HIGH SEVERITY FLUID CATALYTIC CRACKING SYSTEMS V120 (57) : Embodiments of methods for converting gas condensate into a product stream com- prising propylene comprise feeding gas condensate at a top region of a downflow high severity flu- idized catalytic cracking reactor (HSFCC), where the gas condensate comprises: at least 50% by weight paraffms, and less than 0.1 % by weight olefms. The method further comprises feeding catalyst to the 110 top region of the downflow HSFCC reactor in an amount characterized by a catalyst to gas condensate e weight ratio of about 5:1 to about 40:1, where the catalyst comprises nano-ZSM-5 zeolite catalyst hav- ing an average particle diameter from 0.01 to 0.2 p.m, a Si/A1 molar ratio from 20 to 40, and a surface = 105 100--,_ = = = 50 = = 11 area of at least 20 cm 2 /g. The method further comprises cracking the gas condensate in the presence of the catalyst at a reaction temperature of about 500° C to about 700° C to produce the product stream comprising propylene. © 107 140 11 M M ei ei IN 1-1 FIG. 0 ei r 160 1 O [Continued on next page] WO 2017/223310 Al MIDEDIMOHNIIMMEMODIMOINOMMUMEHOIMIE TR), OAPI (BF, BJ, CF, CG, CI, CM, GA, GN, GQ, GW, KM, ML, MR, NE, SN, TD, TG). Published: — with international search report (Art. 21(3))
SG11201811402SA 2016-06-23 2017-06-22 Processes for high severity fluid catalytic cracking systems SG11201811402SA (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US15/190,327 US9981888B2 (en) 2016-06-23 2016-06-23 Processes for high severity fluid catalytic cracking systems
PCT/US2017/038740 WO2017223310A1 (en) 2016-06-23 2017-06-22 Processes for high severity fluid catalytic cracking systems

Publications (1)

Publication Number Publication Date
SG11201811402SA true SG11201811402SA (en) 2019-01-30

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SG10201912689PA SG10201912689PA (en) 2016-06-23 2017-06-22 Processes for high severity fluid catalytic cracking systems
SG11201811402SA SG11201811402SA (en) 2016-06-23 2017-06-22 Processes for high severity fluid catalytic cracking systems

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Country Status (7)

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US (2) US9981888B2 (en)
EP (1) EP3475393B1 (en)
JP (1) JP6959269B2 (en)
KR (1) KR102431019B1 (en)
CN (1) CN109415635B (en)
SG (2) SG10201912689PA (en)
WO (1) WO2017223310A1 (en)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110724553B (en) 2018-07-16 2021-04-06 中国石油化工股份有限公司 Method and system for catalytic cracking by adopting dilute phase conveying bed and rapid fluidized bed
CN110724550B (en) 2018-07-16 2021-04-06 中国石油化工股份有限公司 Method and system for catalytic cracking by adopting fast fluidized bed
CN111607425B (en) * 2019-02-26 2022-03-29 中国石油天然气股份有限公司 Method for catalytic cracking of straight-run diesel oil
WO2021024120A1 (en) * 2019-08-05 2021-02-11 Sabic Global Technologies B.V. A method for catalytic cracking of hydrocarbons to produce olefins and aromatics without steam as diluent
US11066606B2 (en) * 2019-11-12 2021-07-20 Saudi Arabian Oil Company Systems and methods for catalytic upgrading of vacuum residue to distillate fractions and olefins with steam
US11066605B2 (en) * 2019-11-12 2021-07-20 Saudi Arabian Oil Company Systems and methods for catalytic upgrading of vacuum residue to distillate fractions and olefins
US11225612B2 (en) * 2020-03-27 2022-01-18 Saudi Arabian Oil Company Catalyst and process for catalytic steam cracking of heavy distillate
US11213810B1 (en) 2020-07-06 2022-01-04 Saudi Arabian Oil Company Method of producing a cracking catalyst
US11278873B2 (en) * 2020-07-16 2022-03-22 Saudi Arabian Oil Company Method of producing an aromatization catalyst
US11370975B2 (en) 2020-09-30 2022-06-28 Saudi Arabian Oil Company Steam-enhanced catalytic cracking of hydrocarbons to produce light olefins
US11370731B1 (en) 2021-01-12 2022-06-28 Saudi Arabian Oil Company Systems and processes for producing olefins from crude oil
WO2024006381A1 (en) * 2022-06-29 2024-01-04 W.R. Grace & Co.-Conn. Fcc process useful for production of petrochemicals
US20240010926A1 (en) * 2022-07-06 2024-01-11 Saudi Arabian Oil Company Process and catalyst formulation for cracking crude oil to produce light olefins and aromatics
US11827855B1 (en) * 2022-07-06 2023-11-28 Saudi Arabian Oil Company Process and nano-ZSM-5 based catalyst formulation for cracking crude oil to produce light olefins and aromatics
US11866651B1 (en) * 2022-11-09 2024-01-09 Saudi Arabian Oil Company Process and catalyst formulation for cracking crude oil
US11866660B1 (en) 2022-11-09 2024-01-09 Saudi Arabian Oil Company Process and catalyst formulation for cracking crude oil
US11814593B1 (en) * 2022-12-12 2023-11-14 Saudi Arabian Oil Company Processes for hydroprocessing and cracking crude oil
US11814594B1 (en) * 2022-12-12 2023-11-14 Saudi Arabian Oil Company Processes for hydroprocessing and cracking crude oil

Family Cites Families (69)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3837822A (en) 1972-09-28 1974-09-24 Universal Oil Prod Co Two-stage countercurrent fluid-solid contacting process
CN1004878B (en) 1987-08-08 1989-07-26 中国石油化工总公司 Hydrocarbon catalytic conversion method for preparing low-carbon olefin
US5043522A (en) 1989-04-25 1991-08-27 Arco Chemical Technology, Inc. Production of olefins from a mixture of Cu+ olefins and paraffins
US5026935A (en) 1989-10-02 1991-06-25 Arco Chemical Technology, Inc. Enhanced production of ethylene from higher hydrocarbons
US5026936A (en) 1989-10-02 1991-06-25 Arco Chemical Technology, Inc. Enhanced production of propylene from higher hydrocarbons
US5160424A (en) 1989-11-29 1992-11-03 Mobil Oil Corporation Hydrocarbon cracking, dehydrogenation and etherification process
US5171921A (en) 1991-04-26 1992-12-15 Arco Chemical Technology, L.P. Production of olefins
US5232580A (en) 1991-06-21 1993-08-03 Mobil Oil Corporation Catalytic process for hydrocarbon cracking using synthetic mesoporous crystalline material
CN1029407C (en) * 1992-07-16 1995-08-02 中国石油化工总公司 Catalytic cracking method for adaptable multieffect hydrocarbons
US5318689A (en) 1992-11-16 1994-06-07 Texaco Inc. Heavy naphtha conversion process
JPH06192135A (en) * 1992-12-25 1994-07-12 Asahi Chem Ind Co Ltd Method for converting light hydrocarbon
US5523502A (en) 1993-11-10 1996-06-04 Stone & Webster Engineering Corp. Flexible light olefins production
US5770042A (en) 1993-11-15 1998-06-23 Uop Upgrading of cyclic naphthas
US5549813A (en) 1994-03-07 1996-08-27 Dai; Pei-Shing E. FCC process employing low unit cell size y-zeolites
AU4737896A (en) 1994-11-23 1996-06-17 Exxon Chemical Patents Inc. Hydrocarbon conversion process using a zeolite bound zeolite catalyst
US5637207A (en) 1995-04-14 1997-06-10 Abb Lummus Global Inc. Fluid catalytic cracking process
US5685972A (en) 1995-07-14 1997-11-11 Timken; Hye Kyung C. Production of benzene, toluene, and xylene (BTX) from FCC naphtha
NO319519B1 (en) 1997-10-15 2005-08-22 Res Inst Petroleum Processing Process for Preparation of Ethylene and Propylene by Catalytic Pyrolysis of Heavy Hydrocarbons
US5976356A (en) 1997-11-12 1999-11-02 Phillips Petroleum Company Acid treated zeolite containing boron and silver used as a catalyst for converting hydrocarbons and a method of making and using such catalyst
EP0921179A1 (en) 1997-12-05 1999-06-09 Fina Research S.A. Production of olefins
CN1304440A (en) 1998-05-05 2001-07-18 埃克森化学专利公司 Hydrocarbon conversion to propylene with high silica medium pore zeolite catalysts
US6602403B1 (en) 1998-05-05 2003-08-05 Exxonmobil Chemical Patents Inc. Process for selectively producing high octane naphtha
US6069287A (en) 1998-05-05 2000-05-30 Exxon Research And Engineering Co. Process for selectively producing light olefins in a fluid catalytic cracking process
US6315890B1 (en) 1998-05-05 2001-11-13 Exxonmobil Chemical Patents Inc. Naphtha cracking and hydroprocessing process for low emissions, high octane fuels
US6455750B1 (en) 1998-05-05 2002-09-24 Exxonmobil Chemical Patents Inc. Process for selectively producing light olefins
US6294493B1 (en) 1998-05-26 2001-09-25 Exxon Mobil Chemical Patents Inc. Silicoaluminophosphates having an AEL structure
US6015933A (en) 1998-07-15 2000-01-18 Uop Llc Process for removing polymeric by-products from acetylene hydrogenation product
EP1117750B1 (en) 1998-09-28 2004-06-30 BP Corporation North America Inc. Process for manufacturing olefins using a pentasil zeolite based catalyst
US20020003103A1 (en) 1998-12-30 2002-01-10 B. Erik Henry Fluid cat cracking with high olefins prouduction
EP1116775A1 (en) 2000-01-12 2001-07-18 Akzo Nobel N.V. Catalyst composition with high efficiency for the production of light olefins
US20010042700A1 (en) 2000-04-17 2001-11-22 Swan, George A. Naphtha and cycle oil conversion process
US6652737B2 (en) 2000-07-21 2003-11-25 Exxonmobil Research And Engineering Company Production of naphtha and light olefins
US6784329B2 (en) 2002-01-14 2004-08-31 Chevron U.S.A. Inc. Olefin production from low sulfur hydrocarbon fractions
DE10217863A1 (en) 2002-04-22 2003-10-30 Linde Ag Process and apparatus for olefin production
CA2490908C (en) 2002-06-28 2011-09-20 Albemarle Netherlands B.V. Fcc catalyst for reducing the sulfur content in gasoline and diesel
US6867341B1 (en) 2002-09-17 2005-03-15 Uop Llc Catalytic naphtha cracking catalyst and process
US7270739B2 (en) 2003-02-28 2007-09-18 Exxonmobil Research And Engineering Company Fractionating and further cracking a C6 fraction from a naphtha feed for propylene generation
US7273543B2 (en) * 2003-08-04 2007-09-25 Stone & Webster Process Technology, Inc. Process and apparatus for controlling catalyst temperature in a catalyst stripper
US7326332B2 (en) 2003-09-25 2008-02-05 Exxonmobil Chemical Patents Inc. Multi component catalyst and its use in catalytic cracking
US7128827B2 (en) 2004-01-14 2006-10-31 Kellogg Brown & Root Llc Integrated catalytic cracking and steam pyrolysis process for olefins
KR100632563B1 (en) 2004-09-10 2006-10-09 에스케이 주식회사 Solid acid catalyst for catalytic cracking and process for selectively preparing light olefins from full range naphtha
US7323099B2 (en) 2004-11-19 2008-01-29 Exxonmobil Chemical Patents Inc. Two stage fluid catalytic cracking process for selectively producing C2 to C4 olefins
US7374660B2 (en) 2004-11-19 2008-05-20 Exxonmobil Chemical Patents Inc. Process for selectively producing C3 olefins in a fluid catalytic cracking process with recycle of a C4 fraction to a secondary reaction zone separate from a dense bed stripping zone
US7459596B1 (en) 2005-07-26 2008-12-02 Uop Llc Nanocrystalline silicalite for catalytic naphtha cracking
CN100391610C (en) 2005-08-15 2008-06-04 中国石油化工股份有限公司 Catalytic cracking fluid bed catalyst containing molecular sieve
KR101270191B1 (en) 2005-08-15 2013-05-31 상하이 리서치 인스티튜트 오브 페트로케미칼 테크놀로지 시노펙 Method for preparation of ethylene and propylene by catalytic cracking using a fluid-bed catalyst
CN101490216B (en) * 2006-07-26 2013-04-17 道达尔石油化学产品研究弗吕公司 Production of olefins
US7935654B2 (en) 2006-09-28 2011-05-03 Lg Chem, Ltd. Oxide catalyst and phosphoric oxide catalyst for hydrocarbon steam cracking, method for preparing the same and method for preparing olefin by using the same
BRPI0718870A8 (en) * 2006-11-07 2017-02-07 Saudi Arabian Oil Co advanced control of severe fluid catalytic cracking process to maximize propylene production of an oil feedstock
US7727486B2 (en) * 2007-08-01 2010-06-01 Uop Llc Apparatus for heating regeneration gas
CN101367699B (en) * 2007-10-31 2012-05-09 陕西煤化工技术工程中心有限公司 Preparation of propylene
US8652737B2 (en) 2007-11-08 2014-02-18 Canon Kabushiki Kaisha Toner and image forming process
FR2932495B1 (en) * 2008-06-17 2011-03-25 Inst Francais Du Petrole DEVICE FOR CONTROLLING OPERATIVE CONDITIONS IN A CATALYTIC CRACKING UNIT WITH TWO RISERS.
US8137533B2 (en) 2008-10-24 2012-03-20 Uop Llc Mixture of catalysts for cracking naphtha to olefins
CN102209767A (en) 2008-11-06 2011-10-05 环球油品公司 Nanocrystalline silicalite for catalytic naphtha cracking
BRPI0805207B1 (en) 2008-11-25 2019-11-12 Petroleo Brasileiro Sa Petrobras catalytic cracking process of a hydrocarbon stream for maximizing light olefins
US8246914B2 (en) * 2008-12-22 2012-08-21 Uop Llc Fluid catalytic cracking system
WO2010113174A1 (en) * 2009-03-30 2010-10-07 Indian Oil Corporation Limited A fluidized catalytic cracking process
US8845882B2 (en) 2010-03-18 2014-09-30 W. R. Grace & Co.-Conn. High light olefins FCC catalyst compositions
US8247631B2 (en) 2010-06-21 2012-08-21 Uop Llc Process for catalytic cracking of hydrocarbons using UZM-35
US8524630B2 (en) * 2010-10-08 2013-09-03 Exxonmobil Research And Engineering Company Mesoporous aluminas stabilized with rare earth and phosphorous
US9101853B2 (en) 2011-03-23 2015-08-11 Saudi Arabian Oil Company Integrated hydrocracking and fluidized catalytic cracking system and process
KR101821451B1 (en) * 2012-02-14 2018-01-23 릴라이언스 인더스트리즈 리미티드 A process for catalytic conversion of low value hydrocarbon streams to light olefins
US9919985B2 (en) 2012-03-02 2018-03-20 Raquel Bastiani Additives for maximizing light olefins in fluid catalytic cracking and process units
CN104334694B (en) 2012-03-20 2016-06-29 沙特阿拉伯石油公司 Processed by the integrated hydrogenation of crude oil production petroleum chemicals, steam pyrolysis and catalytic cracking process
CN103159579A (en) * 2013-02-07 2013-06-19 大连理工大学 Method of light alkane catalytic cracking by using modified molecular sieve catalyst
US8895790B2 (en) 2013-02-12 2014-11-25 Saudi Basic Industries Corporation Conversion of plastics to olefin and aromatic products
CN105980531B (en) 2013-12-02 2018-06-19 沙特阿拉伯石油公司 For the solvent deasphalting and fluidized catalytic cracking method of the integration of light olefin production
JP6329436B2 (en) * 2014-05-30 2018-05-23 Ｊｘｔｇエネルギー株式会社 Fluid catalytic cracking of heavy oil

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