SG11202001243UA - Chemical looping processes for catalytic hydrocarbon cracking - Google Patents

Chemical looping processes for catalytic hydrocarbon cracking

Info

Publication number
SG11202001243UA
SG11202001243UA SG11202001243UA SG11202001243UA SG11202001243UA SG 11202001243U A SG11202001243U A SG 11202001243UA SG 11202001243U A SG11202001243U A SG 11202001243UA SG 11202001243U A SG11202001243U A SG 11202001243UA SG 11202001243U A SG11202001243U A SG 11202001243UA
Authority
SG
Singapore
Prior art keywords
hydrocarbon cracking
chemical looping
catalytic hydrocarbon
looping processes
processes
Prior art date
Application number
SG11202001243UA
Inventor
Wei Xu
Ibrahim Abba
Rodrigo Sandoval Rivera
Ola Ali
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 SG11202001243UA publication Critical patent/SG11202001243UA/en

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
    • 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
    • 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
    • B01J29/42—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 containing iron group metals, noble metals or copper
    • B01J29/46—Iron group metals or copper
    • 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
    • B01J29/48—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 containing arsenic, antimony, bismuth, vanadium, niobium tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • 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
    • 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
    • C10G11/16—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4006—Temperature

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
SG11202001243UA 2017-08-28 2018-08-21 Chemical looping processes for catalytic hydrocarbon cracking SG11202001243UA (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US201762551014P 2017-08-28 2017-08-28
PCT/US2018/047165 WO2019046031A1 (en) 2017-08-28 2018-08-21 Chemical looping processes for catalytic hydrocarbon cracking

Publications (1)

Publication Number Publication Date
SG11202001243UA true SG11202001243UA (en) 2020-03-30

Family

ID=63638339

Family Applications (1)

Application Number Title Priority Date Filing Date
SG11202001243UA SG11202001243UA (en) 2017-08-28 2018-08-21 Chemical looping processes for catalytic hydrocarbon cracking

Country Status (8)

Country Link
US (1) US10844289B2 (en)
EP (1) EP3676354A1 (en)
JP (1) JP2020531603A (en)
KR (1) KR20200044089A (en)
CN (1) CN111065714A (en)
SA (1) SA520411409B1 (en)
SG (1) SG11202001243UA (en)
WO (1) WO2019046031A1 (en)

Families Citing this family (6)

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Publication number Priority date Publication date Assignee Title
CA3092028C (en) 2012-01-13 2022-08-30 Lummus Technology Llc Process for separating hydrocarbon compounds
US9969660B2 (en) * 2012-07-09 2018-05-15 Siluria Technologies, Inc. Natural gas processing and systems
WO2015081122A2 (en) 2013-11-27 2015-06-04 Siluria Technologies, Inc. Reactors and systems for oxidative coupling of methane
US10301234B2 (en) 2014-01-08 2019-05-28 Siluria Technologies, Inc. Ethylene-to-liquids systems and methods
US10793490B2 (en) 2015-03-17 2020-10-06 Lummus Technology Llc Oxidative coupling of methane methods and systems
US9944573B2 (en) 2016-04-13 2018-04-17 Siluria Technologies, Inc. Oxidative coupling of methane for olefin production

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US3856659A (en) * 1972-12-19 1974-12-24 Mobil Oil Corp Multiple reactor fcc system relying upon a dual cracking catalyst composition
EP0381870B1 (en) * 1989-02-08 1993-05-12 Stone & Webster Engineering Corporation Process for the production of olefins
US20010016673A1 (en) 1999-04-12 2001-08-23 Equistar Chemicals, L.P. Method of producing olefins and feedstocks for use in olefin production from crude oil having low pentane insolubles and high hydrogen content
US6743961B2 (en) 2002-08-26 2004-06-01 Equistar Chemicals, Lp Olefin production utilizing whole crude oil
US7019187B2 (en) 2002-09-16 2006-03-28 Equistar Chemicals, Lp Olefin production utilizing whole crude oil and mild catalytic cracking
US6979757B2 (en) 2003-07-10 2005-12-27 Equistar Chemicals, Lp Olefin production utilizing whole crude oil and mild controlled cavitation assisted cracking
ES2913654T3 (en) * 2004-03-08 2022-06-03 China Petroleum & Chem Corp FCC procedure with two reaction zones
JP5053098B2 (en) * 2004-12-28 2012-10-17 中國石油化工股▲フン▼有限公司 Catalyst and method for cracking hydrocarbons
CN100389174C (en) * 2004-12-28 2008-05-21 中国石油化工股份有限公司 Cracking auxiliary agent for raising density of propylene
CN100392047C (en) * 2005-06-09 2008-06-04 中国科学院大连化学物理研究所 Method for preparing olefin by catalytic oxidation of petroleum hydrocarbon
US7374664B2 (en) 2005-09-02 2008-05-20 Equistar Chemicals, Lp Olefin production utilizing whole crude oil feedstock
US7396449B2 (en) 2006-03-01 2008-07-08 Equistar Chemicals, Lp Olefin production utilizing condensate feedstock
US7550642B2 (en) 2006-10-20 2009-06-23 Equistar Chemicals, Lp Olefin production utilizing whole crude oil/condensate feedstock with enhanced distillate production
US20080277314A1 (en) 2007-05-08 2008-11-13 Halsey Richard B Olefin production utilizing whole crude oil/condensate feedstock and hydrotreating
US7404889B1 (en) 2007-06-27 2008-07-29 Equistar Chemicals, Lp Hydrocarbon thermal cracking using atmospheric distillation
US7858834B2 (en) 2007-08-17 2010-12-28 Equistar Chemicals, Lp Olefin production utilizing a feed containing condensate and crude oil
US20090050523A1 (en) 2007-08-20 2009-02-26 Halsey Richard B Olefin production utilizing whole crude oil/condensate feedstock and selective hydrocracking
CN101469275B (en) 2007-12-28 2012-05-30 中国石油化工股份有限公司 Method for producing light olefin from inferior crude
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CN101683621B (en) 2008-09-28 2012-01-25 中国石油化工股份有限公司 Catalyst for producing low-carbon olefins through catalytic cracking by fixed bed
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KR101787210B1 (en) * 2012-06-14 2017-10-18 사우디 아라비안 오일 컴퍼니 Direct catalytic cracking of crude oil by a temperature gradient process
US10265685B2 (en) * 2015-02-04 2019-04-23 Pc-Cups Ltd. Metallo-silicate catalyst (MSC) compositions, methods of preparation and methods of use in partial upgrading of hydrocarbon feedstocks

Also Published As

Publication number Publication date
KR20200044089A (en) 2020-04-28
SA520411409B1 (en) 2023-01-22
CN111065714A (en) 2020-04-24
JP2020531603A (en) 2020-11-05
US20190062642A1 (en) 2019-02-28
EP3676354A1 (en) 2020-07-08
WO2019046031A1 (en) 2019-03-07
US10844289B2 (en) 2020-11-24

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