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MX2019010082A - Metodos para formar olefinas ligeras mediante craqueo. - Google Patents

Metodos para formar olefinas ligeras mediante craqueo.

Info

Publication number
MX2019010082A
MX2019010082A MX2019010082A MX2019010082A MX2019010082A MX 2019010082 A MX2019010082 A MX 2019010082A MX 2019010082 A MX2019010082 A MX 2019010082A MX 2019010082 A MX2019010082 A MX 2019010082A MX 2019010082 A MX2019010082 A MX 2019010082A
Authority
MX
Mexico
Prior art keywords
reactor
reactor section
light olefins
cracking
methods
Prior art date
Application number
MX2019010082A
Other languages
English (en)
Inventor
T Pretz Matthew
Liu Yu
Original Assignee
Dow Global Technologies Llc
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 Dow Global Technologies Llc filed Critical Dow Global Technologies Llc
Publication of MX2019010082A publication Critical patent/MX2019010082A/es

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G11/00Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
    • C10G11/182Regeneration
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C11/00Aliphatic unsaturated hydrocarbons
    • C07C11/02Alkenes
    • C07C11/04Ethylene
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C11/00Aliphatic unsaturated hydrocarbons
    • C07C11/02Alkenes
    • C07C11/06Propene
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C11/00Aliphatic unsaturated hydrocarbons
    • C07C11/02Alkenes
    • C07C11/08Alkenes with four carbon atoms
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/02Preparation 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
    • C07C4/06Catalytic processes
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/32Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
    • C07C5/327Formation of non-aromatic carbon-to-carbon double bonds only
    • C07C5/333Catalytic processes
    • C07C5/3335Catalytic processes with metals
    • C07C5/3337Catalytic processes with metals of the platinum group
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
    • C07C2523/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
    • C07C2523/42Platinum
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00Catalysts comprising molecular sieves
    • C07C2529/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
    • C07C2529/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • C07C2529/064Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing iron group metals, noble metals or copper
    • C07C2529/068Noble metals
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/1037Hydrocarbon fractions
    • C10G2300/1044Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20C2-C4 olefins
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00Technologies relating to oil refining and petrochemical industry
    • Y02P30/20Technologies relating to oil refining and petrochemical industry using bio-feedstock
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00Technologies relating to oil refining and petrochemical industry
    • Y02P30/40Ethylene production

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

De acuerdo con una o más modalidades descritas en la presente, las olefinas ligeras pueden formarse mediante un método que puede comprender introducir una corriente de alimentación en un reactor, hacer reaccionar la corriente de alimentación con un catalizador de craqueo en el reactor para formar una corriente de producto, y procesar el catalizador de craqueo. El reactor puede comprender una sección de reactor corriente arriba y una sección de reactor corriente abajo. La sección de reactor corriente arriba se puede situar debajo de la sección de reactor corriente abajo. La sección de reactor corriente arriba puede tener un área de sección transversal promedio que es al menos el 150% del área de sección transversal promedio de la sección de reactor corriente abajo.
MX2019010082A 2017-03-13 2018-03-09 Metodos para formar olefinas ligeras mediante craqueo. MX2019010082A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US201762470570P 2017-03-13 2017-03-13
PCT/US2018/021656 WO2018169768A1 (en) 2017-03-13 2018-03-09 Methods for forming light olefins by cracking

Publications (1)

Publication Number Publication Date
MX2019010082A true MX2019010082A (es) 2019-11-21

Family

ID=61692170

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2019010082A MX2019010082A (es) 2017-03-13 2018-03-09 Metodos para formar olefinas ligeras mediante craqueo.

Country Status (10)

Country Link
US (1) US11459282B2 (es)
EP (1) EP3596188A1 (es)
KR (1) KR102531502B1 (es)
CN (1) CN110337485A (es)
AR (1) AR111237A1 (es)
BR (1) BR112019016941A2 (es)
CA (1) CA3070761A1 (es)
MX (1) MX2019010082A (es)
RU (1) RU2019130732A (es)
WO (1) WO2018169768A1 (es)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114286720B (zh) * 2019-08-05 2023-11-07 沙特基础工业全球技术公司 最大化低碳烯烃产率的带挡板的湍流/快速流化床反应器
WO2021024069A1 (en) * 2019-08-05 2021-02-11 Sabic Global Technologies B.V. Single and multiple turbulent/fast fluidized bed reactors in ncc process for maximizing aromatics production
US10934493B1 (en) * 2019-11-22 2021-03-02 Chevron U.S.A. Inc. Extraction of heavy polynuclear aromatics from heavy oil
US20220033714A1 (en) * 2020-07-28 2022-02-03 Saudi Arabian Oil Company Methods and apparatuses for processing hydrocarbons to produce light olefins
EP4221877A1 (en) * 2020-09-30 2023-08-09 Dow Global Technologies LLC Distributor support system for chemical feed distributors in fluidized bed systems
WO2022132884A1 (en) * 2020-12-18 2022-06-23 Dow Global Technologies Llc Methods for producing olefins
KR20240074824A (ko) * 2021-10-04 2024-05-28 다우 글로벌 테크놀로지스 엘엘씨 화학물질의 처리 방법
JP2025537328A (ja) * 2022-11-29 2025-11-14 ダウ グローバル テクノロジーズ エルエルシー 複数の粒子状固体流を分配するのに好適な粒子状固体分配器
US11873452B1 (en) 2022-12-12 2024-01-16 Saudi Arabian Oil Company Methods for processing hydrocarbons to produce light olefins using catalyst formulations or mixtures

Family Cites Families (41)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4051013A (en) * 1973-05-21 1977-09-27 Uop Inc. Fluid catalytic cracking process for upgrading a gasoline-range feed
US4458096A (en) 1983-05-26 1984-07-03 Air Products And Chemicals, Inc. Process for the production of ethylene and propylene
US4579716A (en) 1983-09-06 1986-04-01 Mobil Oil Corporation Closed reactor FCC system with provisions for surge capacity
US4719189A (en) * 1984-04-26 1988-01-12 Mobil Oil Corporation Reactivation of noble metal-containing zeolite catalyst materials
US4595567A (en) * 1984-12-28 1986-06-17 Uop Inc. Cooling fluidized catalytic cracking regeneration zones with heat pipe apparatus
US4686028A (en) * 1985-04-05 1987-08-11 Driesen Roger P Van Upgrading of high boiling hydrocarbons
US4840928A (en) * 1988-01-19 1989-06-20 Mobil Oil Corporation Conversion of alkanes to alkylenes in an external catalyst cooler for the regenerator of a FCC unit
US4912273A (en) * 1988-01-19 1990-03-27 Mobil Oil Corp. Production of aromatic hydrocarbons from alkanes
US5000838A (en) * 1989-12-13 1991-03-19 Mobil Oil Corporation Low efficiency deasphalting and catalytic cracking
US5456821A (en) * 1991-03-12 1995-10-10 Mobil Oil Corp. Catalytic conversion with improved catalyst
US5190650A (en) 1991-06-24 1993-03-02 Exxon Research And Engineering Company Tangential solids separation transfer tunnel
US7169293B2 (en) 1999-08-20 2007-01-30 Uop Llc Controllable space velocity reactor and process
US20020024276A1 (en) 2000-03-23 2002-02-28 Egbert Neuhaus Drawer which is incorporated in a cupboard, in particular kitchen cupboard drawer
US6392113B1 (en) * 2000-10-03 2002-05-21 Abb Lummus Global Inc. Catalytic hydrocarbon dehydrogenation system with prereaction
US7396971B2 (en) * 2002-08-01 2008-07-08 Exxonmobil Chemical Patents Inc. Two stage hydrocarbon conversion reaction system
US6867341B1 (en) 2002-09-17 2005-03-15 Uop Llc Catalytic naphtha cracking catalyst and process
US7128827B2 (en) 2004-01-14 2006-10-31 Kellogg Brown & Root Llc Integrated catalytic cracking and steam pyrolysis process for olefins
WO2005077867A2 (en) 2004-02-09 2005-08-25 The Dow Chemical Company Process for the preparation of dehydrogenated hydrocarbon compounds
KR100651418B1 (ko) 2006-03-17 2006-11-30 에스케이 주식회사 고속유동층을 이용하여 탄화수소 원료로부터 경질 올레핀을제조하는 접촉분해 공정
US7758817B2 (en) * 2006-08-09 2010-07-20 Uop Llc Device for contacting high contaminated feedstocks with catalyst in an FCC unit
US7491315B2 (en) * 2006-08-11 2009-02-17 Kellogg Brown & Root Llc Dual riser FCC reactor process with light and mixed light/heavy feeds
CN101239868B (zh) 2007-02-07 2011-05-18 中国石油化工股份有限公司 提高乙烯、丙烯收率的方法
CN101348409B (zh) 2007-07-19 2011-06-15 中国石油化工股份有限公司 一种生产低碳烯烃的方法
US20100152516A1 (en) * 2008-12-11 2010-06-17 Christopher Naunheimer Moving Bed Hydrocarbon Conversion Process
US8157985B2 (en) 2009-06-22 2012-04-17 Uop Llc Process for catalytic cracking of hydrocarbons using UZM-35HS
WO2011057978A2 (en) 2009-11-10 2011-05-19 Shell Internationale Research Maatschappij B.V. Process for the preparation of a lower olefin product
WO2011121613A2 (en) * 2010-03-31 2011-10-06 Indian Oil Corporation Ltd A process for simultaneous cracking of lighter and heavier hydrocarbon feed and system for the same
US8618011B2 (en) 2010-04-09 2013-12-31 Kellogg Brown & Root Llc Systems and methods for regenerating a spent catalyst
US8258359B2 (en) * 2010-04-20 2012-09-04 Fina Technology, Inc. Alkylation of toluene to form styrene and ethylbenzene
CN101838546B (zh) * 2010-05-10 2013-02-06 中国石油大学(华东) 一种重油和轻烯烃组合进料制备丙烯的反应器及方法
CN102531821B (zh) 2010-12-28 2015-03-25 中国科学院大连化学物理研究所 采用改性zsm-5分子筛催化剂催化甲醇耦合石脑油催化裂解反应的方法
BR112015005747B1 (pt) 2012-09-17 2020-02-18 Dow Global Technologies Llc Arranjo de reator e distribuição de alimentação
CN103773407A (zh) * 2012-10-25 2014-05-07 中国石油大学(北京) 用于催化裂化生物质的方法
US20140275675A1 (en) * 2013-03-13 2014-09-18 Kellogg Brown & Root Llc Dual riser fluid bed process and reactor
CN203448073U (zh) 2013-08-20 2014-02-26 上海河图工程股份有限公司 一种高低并列密相流化床反应-再生装置
CN104437274B (zh) 2013-09-16 2017-01-11 中国石油大学(华东) 一种用于轻烯烃裂解、甲醇制烯烃的流化床反应器
CN111875468A (zh) 2013-11-12 2020-11-03 陶氏环球技术有限责任公司 催化脱氢方法
WO2016069918A1 (en) * 2014-10-29 2016-05-06 Flint Hills Resources, Lp Methods for dehydrogenating one or more alkanes
US20160362613A1 (en) 2015-06-09 2016-12-15 Exxonmobil Research And Engineering Company Fluid catalytic cracking with supplemental heat
US9889418B2 (en) 2015-09-29 2018-02-13 Dow Global Technologies Llc Fluidized fuel gas combustor system for a catalytic dehydrogenation process
AR111124A1 (es) * 2017-03-13 2019-06-05 Dow Global Technologies Llc Métodos para fabricar olefinas ligeras a partir de corrientes de alimentación diferentes

Also Published As

Publication number Publication date
WO2018169768A1 (en) 2018-09-20
KR102531502B1 (ko) 2023-05-12
US11459282B2 (en) 2022-10-04
CA3070761A1 (en) 2018-09-20
KR20190120352A (ko) 2019-10-23
EP3596188A1 (en) 2020-01-22
CN110337485A (zh) 2019-10-15
US20200017426A1 (en) 2020-01-16
AR111237A1 (es) 2019-06-19
RU2019130732A3 (es) 2021-06-22
BR112019016941A2 (pt) 2020-04-07
RU2019130732A (ru) 2021-03-30

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