AR118591A1 - Proceso para la conversión de hidrocarburos y equipamiento para realizar reacciones químicas utilizado en el mismo - Google Patents

Proceso para la conversión de hidrocarburos y equipamiento para realizar reacciones químicas utilizado en el mismo

Info

Publication number
AR118591A1
AR118591A1 ARP200100949A ARP200100949A AR118591A1 AR 118591 A1 AR118591 A1 AR 118591A1 AR P200100949 A ARP200100949 A AR P200100949A AR P200100949 A ARP200100949 A AR P200100949A AR 118591 A1 AR118591 A1 AR 118591A1
Authority
AR
Argentina
Prior art keywords
catalyst
stream
particulate
particulate catalyst
conversion
Prior art date
Application number
ARP200100949A
Other languages
English (en)
Inventor
Rama Rao Marri
Peter Loezos
Liang Chen
Bryan Tomsula
Original Assignee
Lummus Technology Inc
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 Lummus Technology Inc filed Critical Lummus Technology Inc
Publication of AR118591A1 publication Critical patent/AR118591A1/es

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
    • C10G61/00—Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen
    • C10G61/02—Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen plural serial stages only
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • B01J8/0025—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor by an ascending fluid
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/005—Separating solid material from the gas/liquid stream
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/005—Separating solid material from the gas/liquid stream
    • B01J8/0055—Separating solid material from the gas/liquid stream using cyclones
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0095—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes in which two different types of particles react with each other
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/087—Heating or cooling the reactor
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1818—Feeding of the fluidising gas
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1818—Feeding of the fluidising gas
    • B01J8/1827—Feeding of the fluidising gas the fluidising gas being a reactant
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1845—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with particles moving upwards while fluidised
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1845—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with particles moving upwards while fluidised
    • B01J8/1863—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with particles moving upwards while fluidised followed by a downward movement outside the reactor and subsequently re-entering it
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1872—Details of the fluidised bed reactor
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/26—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
    • 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
    • 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
    • C10G35/00—Reforming naphtha
    • C10G35/04—Catalytic reforming
    • C10G35/10—Catalytic reforming with moving catalysts
    • C10G35/14—Catalytic reforming with moving catalysts according to the "fluidised-bed" technique
    • 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
    • C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
    • C10G51/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only
    • C10G51/026—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only only catalytic cracking steps
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/02—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising gravity
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00743—Feeding or discharging of solids
    • B01J2208/00752—Feeding
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00743—Feeding or discharging of solids
    • B01J2208/00761—Discharging
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796—Details of the reactor or of the particulate material
    • B01J2208/00823—Mixing elements
    • B01J2208/00831—Stationary elements
    • B01J2208/0084—Stationary elements inside the bed, e.g. baffles
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796—Details of the reactor or of the particulate material
    • B01J2208/00938—Flow distribution elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00—Washing granular, powdered or lumpy materials; Wet separating
    • B03B5/28—Washing granular, powdered or lumpy materials; Wet separating by sink-float separation
    • B03B5/30—Washing granular, powdered or lumpy materials; Wet separating by sink-float separation using heavy liquids or suspensions
    • B03B5/32—Washing granular, powdered or lumpy materials; Wet separating by sink-float separation using heavy liquids or suspensions using centrifugal force
    • 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
    • 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
    • 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
    • C10G2300/70—Catalyst aspects

Abstract

Los procesos y sistemas para la conversión de hidrocarburos en la presente pueden incluir separar un efluente de un reactor de lecho móvil, el efluente que incluye el producto de reacción, primer catalizador particulado, y segundo catalizador particulado. La separación puede recuperar una primera corriente que incluye el producto de reacción y el primer catalizador particulado y una segunda corriente que incluye el segundo catalizador particulado. La segunda corriente se puede mezclar con una corriente de catalizador regenerado que incluye tanto el primero como el segundo catalizador particulado a una temperatura elevada. La mezcla puede producir un catalizador mixto a una temperatura relativamente uniforme menor que la temperatura elevada del catalizador regenerado, donde la temperatura es más ventajosa para el contacto de la nafta liviana y la nafta pesada dentro del reactor de lecho móvil para producir el efluente que incluye el producto de reacción, el primer catalizador particulado, y el segundo catalizador particulado.
ARP200100949A 2019-04-03 2020-04-03 Proceso para la conversión de hidrocarburos y equipamiento para realizar reacciones químicas utilizado en el mismo AR118591A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US201962828836P 2019-04-03 2019-04-03

Publications (1)

Publication Number Publication Date
AR118591A1 true AR118591A1 (es) 2021-10-20

Family

ID=72662131

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP200100949A AR118591A1 (es) 2019-04-03 2020-04-03 Proceso para la conversión de hidrocarburos y equipamiento para realizar reacciones químicas utilizado en el mismo

Country Status (13)

Country Link
US (1) US11377602B2 (es)
EP (1) EP3947604A4 (es)
JP (1) JP7436503B2 (es)
KR (1) KR102635041B1 (es)
CN (1) CN113661228A (es)
AR (1) AR118591A1 (es)
AU (1) AU2020254703B2 (es)
CA (1) CA3135178C (es)
MX (1) MX2021012037A (es)
SG (1) SG11202110638PA (es)
TW (1) TW202104562A (es)
WO (1) WO2020206081A1 (es)
ZA (1) ZA202107534B (es)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115501823B (zh) * 2021-06-23 2024-03-26 中国石油化工股份有限公司 流化床反应器和制备低碳烯烃的装置以及制备低碳烯烃的方法
CN116020573A (zh) * 2021-10-26 2023-04-28 中国石油化工股份有限公司 流化床催化剂粒度分布的调控装置及其调控方法

Family Cites Families (45)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0987220A1 (en) 1998-09-17 2000-03-22 Technische Universiteit Delft Mesoporous amorphous silicate materials and process for the preparation thereof
US5053204A (en) * 1988-12-30 1991-10-01 Mobil Oil Corporation Multiple feed point catalytic cracking apparatus using elutriable catalyst mixture
US5009769A (en) * 1989-02-06 1991-04-23 Stone & Webster Engineering Corporation Process for catalytic cracking of hydrocarbons
EP0382289B1 (en) * 1989-02-06 1994-03-30 Stone & Webster Engineering Corporation Process for catalytic cracking of hydrocarbons
US5043522A (en) 1989-04-25 1991-08-27 Arco Chemical Technology, Inc. Production of olefins from a mixture of Cu+ olefins and paraffins
US5154818A (en) 1990-05-24 1992-10-13 Mobil Oil Corporation Multiple zone catalytic cracking of hydrocarbons
US5314610A (en) 1992-05-29 1994-05-24 Abb Lummus Crest Inc. Staged catalytic cracking process
US5534135A (en) 1994-03-07 1996-07-09 Abb Lummus Global Inc. Synthesis of zeolites
US5637207A (en) 1995-04-14 1997-06-10 Abb Lummus Global Inc. Fluid catalytic cracking process
JP2906086B2 (ja) 1995-04-27 1999-06-14 エービービー ルーマス グローバル インコーポレイテッド 使用済みｆｃｃ触媒を使用するオレフィン系炭化水素の転化法
US5888921A (en) 1995-10-25 1999-03-30 Abb Lummus Global Inc. Binary molecular sieves having a core and shell of different structures and compositions
US5846402A (en) 1997-05-14 1998-12-08 Indian Oil Corporation, Ltd. Process for catalytic cracking of petroleum based feed stocks
EP0921179A1 (en) 1997-12-05 1999-06-09 Fina Research S.A. Production of olefins
US6106697A (en) 1998-05-05 2000-08-22 Exxon Research And Engineering Company Two stage fluid catalytic cracking process for selectively producing b. C.su2 to C4 olefins
US5944982A (en) 1998-10-05 1999-08-31 Uop Llc Method for high severity cracking
US6869521B2 (en) 2002-04-18 2005-03-22 Uop Llc Process and apparatus for upgrading FCC product with additional reactor with thorough mixing
US6930219B2 (en) 1999-09-07 2005-08-16 Abb Lummus Global Inc. Mesoporous material with active metals
EP1190019A1 (en) 2000-02-16 2002-03-27 Indian Oil Corporation Limited A multi stage selective catalytic cracking process and a system for producing high yield of middle distillate products from heavy hydrocarbon feedstocks
EP1195424A1 (en) 2000-10-05 2002-04-10 ATOFINA Research A process for cracking an olefin-rich hydrocarbon feedstock
US6809055B2 (en) 2000-10-20 2004-10-26 Abb Lummus Global, Inc. Zeolites and molecular sieves and the use thereof
US20030127358A1 (en) 2002-01-10 2003-07-10 Letzsch Warren S. Deep catalytic cracking process
US7314963B2 (en) 2002-03-26 2008-01-01 Uop Llc Spherical catalysts to convert hydrocarbons to light olefins
US6866771B2 (en) * 2002-04-18 2005-03-15 Uop Llc Process and apparatus for upgrading FCC product with additional reactor with catalyst recycle
US7179427B2 (en) 2002-11-25 2007-02-20 Abb Lummus Global Inc. Apparatus for countercurrent contacting of gas and solids
US7128827B2 (en) 2004-01-14 2006-10-31 Kellogg Brown & Root Llc Integrated catalytic cracking and steam pyrolysis process for olefins
US7268265B1 (en) 2004-06-30 2007-09-11 Uop Llc Apparatus and process for light olefin recovery
BRPI0403184B1 (pt) 2004-07-30 2015-04-07 Petroleo Brasileiro Sa Processo para alterar a distribuição de produtos de craqueamento catalítico fluido de hidrocarbonetos
WO2006020547A1 (en) 2004-08-10 2006-02-23 Shell Internationale Research Maatschappij B.V. Method and apparatus for making a middle distillate product and lower olefins from a hydrocarbon feedstock
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
US20070205139A1 (en) 2006-03-01 2007-09-06 Sathit Kulprathipanja Fcc dual elevation riser feed distributors for gasoline and light olefin modes of operation
CN101205475B (zh) * 2006-12-22 2012-01-25 中国石油化工股份有限公司 一种制取低烯烃含量汽油的烃类催化转化方法
US7611622B2 (en) * 2006-12-29 2009-11-03 Kellogg Brown & Root Llc FCC process for converting C3/C4 feeds to olefins and aromatics
US8067656B2 (en) * 2008-11-26 2011-11-29 Chevron U.S.A. Inc. Liquid-liquid separation process via coalescers
ES2645694T3 (es) 2008-12-10 2017-12-07 Reliance Industries Limited Procedimiento de craqueo catalítico en lecho fluidizado (FCC) para fabricar propileno y etileno con un rendimiento aumentado
SG178159A1 (en) 2009-08-06 2012-03-29 Shell Int Research Method for revamping an hf or sulphuric acid alkylation unit
US20140034551A1 (en) 2011-04-15 2014-02-06 Petroleo Brasileiro S.A. - Petrobras Fcc process for maximizing diesel
US8920755B2 (en) * 2011-09-12 2014-12-30 Chevron U.S.A. Inc. Conversion of HF alkylation units for ionic liquid catalyzed alkylation processes
US9656185B2 (en) 2012-07-11 2017-05-23 Merichem Company Contactor and separation apparatus and process of using same
US9452404B2 (en) 2012-07-12 2016-09-27 Lummus Technology Inc. Fluid cracking process and apparatus for maximizing light olefins or middle distillates and light olefins
WO2015138055A1 (en) * 2014-03-12 2015-09-17 Exxonmobil Upstream Research Company Split flow pipe separator with sand trap
KR20150122310A (ko) * 2014-04-22 2015-11-02 삼성중공업 주식회사 수직형 유체 이송관을 구비한 삼상 분리기
US9522859B2 (en) 2014-12-11 2016-12-20 Uop Llc Methods for recovering ionic liquid fines from a process stream
KR102305664B1 (ko) * 2016-09-16 2021-09-28 루머스 테크놀로지 엘엘씨 경질 올레핀 수율을 최대화하기 위한 유동 촉매 분해 공정 및 장치 및 다른 응용 분야
CN110997876A (zh) * 2017-07-18 2020-04-10 鲁姆斯科技有限责任公司 烯烃生产的一体化热裂化和催化裂化
CN109385300B (zh) * 2017-08-08 2021-01-01 中国石油天然气股份有限公司 一种增产汽油和提高汽油辛烷值的催化转化方法

Also Published As

Publication number Publication date
SG11202110638PA (en) 2021-10-28
US11377602B2 (en) 2022-07-05
TW202104562A (zh) 2021-02-01
JP2022521853A (ja) 2022-04-12
ZA202107534B (en) 2022-08-31
JP7436503B2 (ja) 2024-02-21
US20200318019A1 (en) 2020-10-08
AU2020254703A1 (en) 2021-11-18
KR20210132220A (ko) 2021-11-03
MX2021012037A (es) 2021-12-10
CA3135178C (en) 2024-03-12
KR102635041B1 (ko) 2024-02-07
CN113661228A (zh) 2021-11-16
EP3947604A4 (en) 2022-12-14
WO2020206081A1 (en) 2020-10-08
CA3135178A1 (en) 2020-10-08
AU2020254703B2 (en) 2023-05-18
EP3947604A1 (en) 2022-02-09

Similar Documents

Publication Publication Date Title
SA519410038B1 (ar) دمج عملية تكسير حفزي مع عملية تحويل خام إلى مواد كيميائية
PH12019500563A1 (en) Fluid catalytic cracking process and apparatus for maximizing light olefin yield and other applications
AR118591A1 (es) Proceso para la conversión de hidrocarburos y equipamiento para realizar reacciones químicas utilizado en el mismo
TW200615256A (en) Method of producing ethylene and propylene
RU2008101551A (ru) Способ увеличения выработки легких олефинов из углеводородного сырья посредством каталитического крекинга
CO7250452A2 (es) Proceso de craqueo catalítico fluido y aparato para miximizar olefinas ligeras o destilados medios y olefinas ligeras
WO2009156433A3 (en) Process to make olefins from oxygenates
RU2009144146A (ru) Установка и способ получения средних дистиллятов и низших олефинов из углеводородного сырья
WO2009156435A3 (en) Process to make olefins and aromatics from organics
RU2014131227A (ru) Двуступенчатый реактор и способ конверсии твердой биомассы
MX2022000575A (es) Proceso y aparato de craqueo catalitico de fluidos para maximizar el rendimiento de olefinas ligeras y otras aplicaciones.
RU2018141252A (ru) Способ каталитического дегидрирования
RU2016125275A (ru) Способ гидроочистки газойля в последовательных реакторах с рециркуляцией водорода
AR111149A1 (es) Procesos para mejorar la actividad de los catalizadores híbridos
KR20130097207A (ko) 합성 가스 컨니셔닝을 수반하는 저온 내황성 타르 제거
EA201290293A1 (ru) Технология для регенерации катализаторов для конверсии углеводородов
CL2007002877A1 (es) Proceso para producir nafta desde aceite pesado o bitumen usando una unidad fcc que comprende suministrar la alimentacion a la zona de reacion de la unidad con un catalizador en razon de peso catalizador/aceite entre 4 y 10 y y operar a n° de conversion entre 40 y 60; y sistema para producir mezcla de aceite pesado y nafta.
Gerzeliev et al. Production of ethylene from ethane fraction by a method alternative to steam cracking
SA519410445B1 (ar) عملية للتكسير الحفزي للنفط باستخدام نظام مُفاعل تدفق قطري ذو طبقة متحركة
ZA202209356B (en) Production of light olefins from crude oil via fluid catalytic cracking process and apparatus
AR111124A1 (es) Métodos para fabricar olefinas ligeras a partir de corrientes de alimentación diferentes
RU2568809C1 (ru) Способ каталитической переработки легкого углеводородного сырья
JP2023516115A (ja) 水素および化学物質への直接的な原油のアップグレードのためのシステムおよび方法
TWI838559B (zh) 流體催化裂解方法以及用於使輕質烯烴產率最大化及其他應用之裝置
KR102345598B1 (ko) 플라스틱 열분해 생성물의 방향족 수율 증가 방법

Legal Events

Date Code Title Description
FG Grant, registration