AR111237A1 - Métodos y aparatos para formar olefinas ligeras por craqueo - Google Patents

Métodos y aparatos para formar olefinas ligeras por craqueo

Info

Publication number
AR111237A1
AR111237A1 ARP180100534A ARP180100534A AR111237A1 AR 111237 A1 AR111237 A1 AR 111237A1 AR P180100534 A ARP180100534 A AR P180100534A AR P180100534 A ARP180100534 A AR P180100534A AR 111237 A1 AR111237 A1 AR 111237A1
Authority
AR
Argentina
Prior art keywords
reactor
section
light olefins
craqueo
appliances
Prior art date
Application number
ARP180100534A
Other languages
English (en)
Inventor
Yu Liu
Matthew T Pretz
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 AR111237A1 publication Critical patent/AR111237A1/es

Links

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
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C11/00—Aliphatic unsaturated hydrocarbons
    • C07C11/02—Alkenes
    • C07C11/04—Ethylene
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C11/00—Aliphatic unsaturated hydrocarbons
    • C07C11/02—Alkenes
    • C07C11/06—Propene
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C11/00—Aliphatic unsaturated hydrocarbons
    • C07C11/02—Alkenes
    • C07C11/08—Alkenes with four carbon atoms
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
    • C07C5/327—Formation of non-aromatic carbon-to-carbon double bonds only
    • C07C5/333—Catalytic processes
    • C07C5/3335—Catalytic processes with metals
    • C07C5/3337—Catalytic processes with metals of the platinum group
    • 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
    • C10G11/182—Regeneration
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
    • C07C2523/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
    • C07C2523/42—Platinum
    • 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
    • C07C2529/064—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing iron group metals, noble metals or copper
    • C07C2529/068—Noble metals
    • 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
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
    • 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
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00—Technologies relating to oil refining and petrochemical industry
    • Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00—Technologies relating to oil refining and petrochemical industry
    • Y02P30/40—Ethylene 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

Las olefinas ligeras pueden formarse por 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 del reactor corriente arriba y una sección del reactor corriente abajo. La sección del reactor corriente arriba puede estar situada por debajo de la sección del reactor corriente abajo. La sección del reactor corriente arriba puede tener un área de sección transversal promedio que es al menos 150% del área de sección transversal promedio de la sección del reactor corriente abajo.
ARP180100534A 2017-03-13 2018-03-07 Métodos y aparatos para formar olefinas ligeras por craqueo AR111237A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US201762470570P 2017-03-13 2017-03-13

Publications (1)

Publication Number Publication Date
AR111237A1 true AR111237A1 (es) 2019-06-19

Family

ID=61692170

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP180100534A AR111237A1 (es) 2017-03-13 2018-03-07 Métodos y aparatos para formar olefinas ligeras por 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 (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021024119A1 (en) * 2019-08-05 2021-02-11 Sabic Global Technologies B.V. Turbulent/fast fluidized bed reactor with baffles to maximize light olefin yields
CN114207091B (zh) * 2019-08-05 2024-07-16 沙特基础全球技术有限公司 用于最大化芳族化合物产量的ncc方法中的单个和多个湍流/快速流化床反应器
US20220033714A1 (en) * 2020-07-28 2022-02-03 Saudi Arabian Oil Company Methods and apparatuses for processing hydrocarbons to produce light olefins
BR112023005869A2 (pt) * 2020-09-30 2023-05-02 Dow Global Technologies Llc Sistema de processamento de leito fluidizado
KR20240074824A (ko) * 2021-10-04 2024-05-28 다우 글로벌 테크놀로지스 엘엘씨 화학물질의 처리 방법
WO2024118461A1 (en) * 2022-11-29 2024-06-06 Dow Global Technologies Llc Particulate solid distributors suitable for distributing multiple particulate solid streams
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 (42)

* 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
US4912273A (en) * 1988-01-19 1990-03-27 Mobil Oil Corp. Production of aromatic hydrocarbons from alkanes
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
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
ZA200606323B (en) 2004-02-09 2008-02-27 Dow Chemical Co 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
CN102666794B (zh) 2009-11-10 2015-12-02 国际壳牌研究有限公司 用于制备低级烯烃产品的方法
CA2795120C (en) * 2010-03-31 2019-10-08 Indian Oil Corporation Ltd A process for simulataneous 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
AR092578A1 (es) 2012-09-17 2015-04-22 Dow Global Technologies Llc Ensamble de reactor y distribucion de la alimentacion
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
RU2665480C1 (ru) 2013-11-12 2018-08-30 ДАУ ГЛОБАЛ ТЕКНОЛОДЖИЗ ЭлЭлСи Способ каталитического дегидрирования
US20170333889A1 (en) * 2014-10-29 2017-11-23 Flint Hills Resources, Lp Methods for dehydrogenating one or more alkanes
WO2016200565A1 (en) 2015-06-09 2016-12-15 Exxonmobil Research And Engineering Company Fluid catalytic cracking with supplemental heat
US9815040B2 (en) 2015-06-26 2017-11-14 Dow Global Technologies Llc Fluid solids contacting device
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
BR112019016941A2 (pt) 2020-04-07
RU2019130732A3 (es) 2021-06-22
RU2019130732A (ru) 2021-03-30
US20200017426A1 (en) 2020-01-16
EP3596188A1 (en) 2020-01-22
KR20190120352A (ko) 2019-10-23
CA3070761A1 (en) 2018-09-20
CN110337485A (zh) 2019-10-15
KR102531502B1 (ko) 2023-05-12
MX2019010082A (es) 2019-11-21
WO2018169768A1 (en) 2018-09-20
US11459282B2 (en) 2022-10-04

Similar Documents

Publication Publication Date Title
AR111237A1 (es) Métodos y aparatos para formar olefinas ligeras por craqueo
AR111992A1 (es) Sistemas de reactor que comprenden el reciclado de fluidos
BR112016018282A8 (pt) mistura de catalisador para pirólise rápida catalítica e método para produzir produtos monoaromáticos
AR115281A1 (es) Métodos y dispositivos para la producción de biodiésel, hidrocarburos de la gama diésel y productos obtenidos de estos
AR109657A1 (es) Proceso y aparato de craqueo catalítico fluido para maximizar la producción de olefina liviana y otras aplicaciones
CL2019000581A1 (es) Método para preparar etileno en proceso de preparación de propileno utilizando reacción por deshidrogenación de propano.
AR118474A1 (es) Un método y una materia prima para producir hidrocarburos
AR097910A1 (es) Galleta blanda con glucosa de absorción lenta
MX2017013893A (es) Metodo para inactivar un virus continuo en un microreactor.
EA201690125A1 (ru) Способ конверсии высококипящего углеводородного сырья в более легкокипящие углеводородные продукты
ECSP17018111A (es) Planta de procesamiento enzimático y método de procesamiento enzimático
CL2020001210A1 (es) Proceso para modular azúcar.
MX2015013012A (es) Isomerizacion a alta temperatura de (e)-1-cloro-3,3,3-trifluroprop eno a (z)-1-cloro-3,3,3-trifluoropropeno.
UA115098C2 (uk) Спосіб виробництва олії з мікроводоростей
AR119165A1 (es) Control de perfusión basado en biomasa automatizado en la fabricación de productos biológicos
MX2016007845A (es) Reciclaje de nafteno eficiente en energia de a traves del uso de una torre de fraccionamiento de extraccion lateral y condensacion parcial.
AR100432A1 (es) Método para modificar madera
CL2020001211A1 (es) Proceso para modulación de azúcar.
AR086127A1 (es) Proceso para la produccion de etanol utilizando un material de alimentacion utilizando un catalitico que contiene cobre
MY177141A (en) Process for increasing the yield of an isomerization zone
AR110657A1 (es) Sistema de reactores paralelos para la deshidrogenación de etilbenceno
CO2017005765A2 (es) Montajes de refinación y métodos de refinación para gas natural rico
AR095942A1 (es) Métodos y aparatos para el procesamiento de materias primas renovables
BR112018003869A2 (pt) ?processos para recuperação de ácido clorídrico de uma composição de lignina e para produção de um produto de lignina, e, composição de lignina particulada?.
UY36417A (es) Proceso para tratamiento de lana y productos

Legal Events

Date Code Title Description
FG Grant, registration