AR109885A1 - Reactores catalíticos fluidos que incluyen directores de flujo - Google Patents

Reactores catalíticos fluidos que incluyen directores de flujo

Info

Publication number
AR109885A1
AR109885A1 ARP170102968A ARP170102968A AR109885A1 AR 109885 A1 AR109885 A1 AR 109885A1 AR P170102968 A ARP170102968 A AR P170102968A AR P170102968 A ARP170102968 A AR P170102968A AR 109885 A1 AR109885 A1 AR 109885A1
Authority
AR
Argentina
Prior art keywords
elevator
lower reactor
fluid catalytic
including flow
catalytic reactors
Prior art date
Application number
ARP170102968A
Other languages
English (en)
Inventor
Brien A Stears
Madhusudhan Kodam
Ben J Freireich
Mark W Stewart
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 AR109885A1 publication Critical patent/AR109885A1/es

Links

Classifications

    • 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
    • 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
    • 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
    • B01J8/0065—Separating solid material from the gas/liquid stream by impingement against stationary members
    • 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
    • B01J8/34—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 stationary packing material in the fluidised bed, e.g. bricks, wire rings, baffles
    • 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
    • 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
    • B01J2208/00008—Controlling the process
    • B01J2208/00548—Flow
    • 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
    • B01J2208/00823—Mixing elements
    • B01J2208/00831—Stationary elements
    • B01J2208/00849—Stationary elements outside 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

De acuerdo con una o más formas de realización, un reactor catalítico fluido puede incluir un elevador, una porción del reactor inferior, una porción de transición, y un director de flujo. El elevador puede incluir un área transversal, y la porción del reactor inferior puede incluir un área transversal. La porción de transición puede fijar el elevador a la porción del reactor inferior. El área transversal del elevador puede ser menor que el área transversal de la porción del reactor inferior de modo que la porción de transición se estrecha hacia adentro de la porción del reactor inferior al elevador. El director de flujo se puede ubicar al menos dentro de una región interior de la porción de transición. El director de flujo puede incluir un cuerpo que afecta el perfil de velocidad de fluidos que se mueven. de la porción del reactor inferior al elevador.
ARP170102968A 2016-11-02 2017-10-25 Reactores catalíticos fluidos que incluyen directores de flujo AR109885A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US201662416553P 2016-11-02 2016-11-02

Publications (1)

Publication Number Publication Date
AR109885A1 true AR109885A1 (es) 2019-01-30

Family

ID=60451171

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP170102968A AR109885A1 (es) 2016-11-02 2017-10-25 Reactores catalíticos fluidos que incluyen directores de flujo

Country Status (8)

Country Link
US (1) US10589242B2 (es)
EP (1) EP3535053B1 (es)
CN (1) CN110099741B (es)
AR (1) AR109885A1 (es)
BR (1) BR112019008808B1 (es)
CA (1) CA3042006A1 (es)
RU (1) RU2754860C2 (es)
WO (1) WO2018085084A1 (es)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112708447B (zh) * 2019-10-24 2022-12-23 天津市职业大学 一种降低边壁区返混的提升管反应器

Family Cites Families (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2084292A5 (es) * 1970-03-06 1971-12-17 Dresser Ind
US4579716A (en) 1983-09-06 1986-04-01 Mobil Oil Corporation Closed reactor FCC system with provisions for surge capacity
US4717467A (en) * 1987-05-15 1988-01-05 Mobil Oil Corporation Process for mixing fluid catalytic cracking hydrocarbon feed and catalyst
US5190650A (en) 1991-06-24 1993-03-02 Exxon Research And Engineering Company Tangential solids separation transfer tunnel
US6069012A (en) 1997-05-23 2000-05-30 Kayser Technology, Inc. Versatile fluidized bed reactor
CN1073883C (zh) * 1998-05-15 2001-10-31 中国石油化工总公司 一种采用管壁补气与排气实现循环流化床多段化操作的方法及其装置
US6166282A (en) 1999-08-20 2000-12-26 Uop Llc Fast-fluidized bed reactor for MTO process
US7169293B2 (en) 1999-08-20 2007-01-30 Uop Llc Controllable space velocity reactor and process
JP2002022643A (ja) * 2000-07-05 2002-01-23 Tonichi Computer Applications Kk 粒度分布測定装置
US6894183B2 (en) * 2001-03-26 2005-05-17 Council Of Scientific And Industrial Research Method for gas—solid contacting in a bubbling fluidized bed reactor
US6655664B2 (en) * 2002-04-30 2003-12-02 Shuo Wei Chuang Adjustable bubble generator practical for use as a relief valve
US7396971B2 (en) 2002-08-01 2008-07-08 Exxonmobil Chemical Patents Inc. Two stage hydrocarbon conversion reaction system
CN2568299Y (zh) * 2002-09-24 2003-08-27 中国科学院过程工程研究所 超细及粘性颗粒气固相反应用的循环流化床反应器
US20120211402A1 (en) 2003-10-27 2012-08-23 Etx Systems Inc. Process for converting a liquid feed material into a vapor phase product
US7429363B2 (en) 2005-02-08 2008-09-30 Stone & Webster Process Technology, Inc. Riser termination device
GB0509742D0 (en) 2005-05-13 2005-06-22 Ashe Morris Ltd Variable heat flux heat exchangers
US7758817B2 (en) 2006-08-09 2010-07-20 Uop Llc Device for contacting high contaminated feedstocks with catalyst in an FCC unit
US7902416B2 (en) 2006-12-28 2011-03-08 Uop Llc Fluidized bed reactor with back-mixing for dehydrogenation of light paraffins
WO2008080357A1 (en) * 2006-12-29 2008-07-10 Accelergy Shanghai R & D Center Co., Ltd. High throughput catalytic process mass transfer investigation method
US20100320121A1 (en) 2006-12-29 2010-12-23 Bauman Richard F High throughput development method for catalytic hydroprocessing of dirty feedstocks
US8349170B2 (en) * 2008-05-14 2013-01-08 Exxonmobil Research And Engineering Company FCC reactor and riser design for short contact-time catalytic cracking of hydrocarbons
CN101590385A (zh) * 2008-05-28 2009-12-02 北京紫光英力化工技术有限公司 一种高效超声波环流式反应装置
CN101322924B (zh) * 2008-07-28 2010-06-02 中国石油化工集团公司 一种催化剂混合设备
CN101850226B (zh) * 2010-01-21 2012-12-12 中国石油天然气股份有限公司 一种浓相段进料用于流化催化转化的提升管反应器
CN201988373U (zh) * 2010-12-31 2011-09-28 洛阳惠生石化工程股份有限公司 可以改善催化剂分布的预提升器
EP2535105A1 (en) 2011-06-14 2012-12-19 Corning Incorporated Systems and methods for scale-up of microreactors
US8815082B2 (en) * 2011-12-12 2014-08-26 Uop Llc Process and apparatus for mixing two streams of catalyst
US8936758B2 (en) * 2012-03-20 2015-01-20 Uop Llc Process and apparatus for mixing two streams of catalyst
US8911673B2 (en) * 2012-06-27 2014-12-16 Uop Llc Process and apparatus for distributing hydrocarbon feed to a catalyst stream
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
US9725382B2 (en) 2013-11-12 2017-08-08 Dow Global Technologies Llc Catalytic dehydrogenation process
US9815040B2 (en) 2015-06-26 2017-11-14 Dow Global Technologies Llc Fluid solids contacting device
CN204999622U (zh) * 2015-09-14 2016-01-27 中国成达工程有限公司 冷氢化流化床反应器气体分布板

Also Published As

Publication number Publication date
RU2754860C2 (ru) 2021-09-08
EP3535053B1 (en) 2022-07-27
BR112019008808B1 (pt) 2022-07-19
US10589242B2 (en) 2020-03-17
BR112019008808A2 (pt) 2019-07-16
RU2019115139A3 (es) 2020-12-14
CN110099741B (zh) 2022-03-01
CN110099741A (zh) 2019-08-06
RU2019115139A (ru) 2020-11-17
US20190255498A1 (en) 2019-08-22
WO2018085084A1 (en) 2018-05-11
EP3535053A1 (en) 2019-09-11
CA3042006A1 (en) 2018-05-11

Similar Documents

Publication Publication Date Title
ES2665593T3 (es) Herramienta para aplicar un fluido
CL2015002533A1 (es) Válvula de dispositivo de transferencia
MX2022010519A (es) Conjunto de cateter de seguridad de control de sangre multiusos.
EP4268947A3 (en) Improved process-intensified flow reactor
AR103387A1 (es) Dispositivo de fluido que emula una fractura en una formación y se utiliza para analizar el flujo de un fluido de tratamiento en el dispositivo
BR112017017871A2 (pt) emissor configurado para ser unido a uma superfície da parede interna de um tubo, e tubo de irrigação gotejante
AR098157A1 (es) Montaje de regulación de válvula de control que tiene una jaula con aberturas rómbicas
MX2017012685A (es) Válvula de punto de inicio.
BR112015018621A2 (pt) reator
AR110547A1 (es) Elemento de separación por flujo tangencial que integra canales flexuosos
EA201691551A1 (ru) Установка для получения энергии от потока текучей среды
CO2019000182A2 (es) Dispositivo de ajuste a presión
MY175457A (en) Flow reactor vessels and reactor systems
CH710182A8 (de) Turbinenkomponente mit gestuften Öffnungen.
MX2016014159A (es) Regulador de fluidos con dispositivo de campo con cierre brusco y convertible.
AR100138A1 (es) Colector para caudalímetro con soporte de indexación
BR112017004099A2 (pt) conjunto de fundo de poço, dispositivo de telemetria à base de fluido e método
MX2017012757A (es) Contenedor tubular.
RU2016143142A (ru) Устройство изменения скорости в проточном канале для регулирующего клапана
RU2015139936A (ru) Композиционный динамический уплотнительный узел клапана для высокотемпературных управляющих клапанов
BR112017013287A2 (pt) conjunto de completação, e, métodos para manutenção de pressão dentro de uma zona de produção de várias zonas e para fornecimento de manutenção de pressão em uma zona de produção de várias zonas
WO2015114055A3 (en) Flow control device
AR109885A1 (es) Reactores catalíticos fluidos que incluyen directores de flujo
PL419732A1 (pl) Prowadnik do maszyny górniczej
AR122757A2 (es) Unidad de reactor catalítico fluido y componente de equipamiento comprendido en la misma

Legal Events

Date Code Title Description
FG Grant, registration