PL404311A1 - Aparat z faza zawiesinowa - Google Patents

Aparat z faza zawiesinowa

Info

Publication number
PL404311A1
PL404311A1 PL404311A PL40431111A PL404311A1 PL 404311 A1 PL404311 A1 PL 404311A1 PL 404311 A PL404311 A PL 404311A PL 40431111 A PL40431111 A PL 40431111A PL 404311 A1 PL404311 A1 PL 404311A1
Authority
PL
Poland
Prior art keywords
partition
suspension
vessel
pressure
suspension body
Prior art date
Application number
PL404311A
Other languages
English (en)
Inventor
Andrè Peter Steynberg
Evert Phillippus Kleynhans
Marshall Stephen Lee
Hermanus Gerhardus Nel
Jako Louw
Original Assignee
Sasol Technology (Proprietary) Limited
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 Sasol Technology (Proprietary) Limited filed Critical Sasol Technology (Proprietary) Limited
Publication of PL404311A1 publication Critical patent/PL404311A1/pl

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
    • 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
    • B01J8/1809—Controlling 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
    • B01J8/18—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
    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • 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
    • C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
    • C10G2/34—Apparatus, reactors
    • C10G2/342—Apparatus, reactors with moving solid catalysts
    • 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
    • C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
    • C10G2/34—Apparatus, reactors
    • C10G2/342—Apparatus, reactors with moving solid catalysts
    • C10G2/344—Apparatus, reactors with 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
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00132—Tubes
    • 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
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00141—Coils
    • 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
    • B01J2208/00539—Pressure
    • 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
    • B01J2208/00884—Means for supporting the bed of particles, e.g. grids, bars, perforated plates
    • 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
    • B01J2208/00893—Feeding means for the reactants
    • B01J2208/00902—Nozzle-type feeding elements
    • 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
    • B01J2208/00893—Feeding means for the reactants
    • B01J2208/00911—Sparger-type feeding elements
    • 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
    • B01J2208/00991—Disengagement zone in fluidised-bed reactors

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Combustion & Propulsion (AREA)
  • General Chemical & Material Sciences (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Consolidation Of Soil By Introduction Of Solidifying Substances Into Soil (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

Wynalazek dotyczy sposobu obslugiwania aparatu (10) z faza zawiesinowa, obejmujacego doprowadzanie jednego lub wiecej gazowych odczynników do zawiesinowego korpusu (37) lub stalego materialu drobnoziarnistego zawieszonego w plynie zawiesinowym zawartym wewnatrz naczynia (12). Ten jeden lub wiecej odczynników doprowadza sie do zawiesinowego korpusu (37) poprzez dystrybutor gazowy (14), majacy zwrócone do dolu otwory wylotowe (32) gazu, a takze doprowadza sie je do nieprzepuszczalnej dla plynu przegrody (18) rozpietej w naczyniu (12) ponizej dystrybutora gazowego (14). Ta przegroda (18) dzieli naczynie (12) na przestrzen zawiesinowa (19) powyzej przegrody (18) oraz przestrzen dolna (36) ponizej przegrody (18). Róznica cisnien jest utrzymywana na przegrodzie (18) pomiedzy pewnymi uprzednio zdefiniowanymi granicami, poprzez dokonywanie manipulacji lub poprzez umozliwienie wstepowania zmian cisnienia w przestrzeni dolnej (36) w wyniku zastosowania przenoszacego cisnienie korytarza (34), ustanawiajacego przeplyw lub komunikacje cisnieniowa pomiedzy przestrzenia dolna (36) a przestrzenia górna (40) powyzej korpusu zawiesinowego (37).
PL404311A 2010-12-13 2011-12-12 Aparat z faza zawiesinowa PL404311A1 (pl)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US42245710P 2010-12-13 2010-12-13
ZA201008969 2010-12-13

Publications (1)

Publication Number Publication Date
PL404311A1 true PL404311A1 (pl) 2014-03-03

Family

ID=45491643

Family Applications (1)

Application Number Title Priority Date Filing Date
PL404311A PL404311A1 (pl) 2010-12-13 2011-12-12 Aparat z faza zawiesinowa

Country Status (12)

Country Link
US (2) US9937476B2 (pl)
CN (1) CN103354764B (pl)
AP (1) AP3958A (pl)
AR (1) AR084260A1 (pl)
AU (1) AU2011342806B2 (pl)
BR (1) BR112013014824B1 (pl)
CA (1) CA2819813C (pl)
NZ (1) NZ611549A (pl)
PE (1) PE20140504A1 (pl)
PL (1) PL404311A1 (pl)
RU (1) RU2566406C2 (pl)
WO (1) WO2012080933A1 (pl)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2011342806B2 (en) * 2010-12-13 2016-05-26 Sasol Technology (Proprietary) Limited Slurry phase apparatus
ITMI20131137A1 (it) * 2013-07-05 2015-01-06 Eni Spa Procedimento per la raffinazione del greggio
WO2015087211A1 (en) 2013-12-11 2015-06-18 Sasol Technology Proprietary Limited A method of shutting down an operating three-phase slurry bubble column reactor
CN105542848B (zh) * 2014-10-29 2017-12-22 中国石油化工股份有限公司 一种重油浆态床加氢反应装置和应用方法
CN105617950B (zh) * 2014-10-29 2018-04-13 中国石油化工股份有限公司 一种重油加氢浆态床反应器及其应用方法
CN105623728A (zh) * 2014-10-29 2016-06-01 中国石油化工股份有限公司 一种两段重油浆态床加氢装置和应用方法
CN105623730B (zh) * 2014-10-29 2017-12-22 中国石油化工股份有限公司 一种重油浆态床加氢的设备和方法
CN106147848B (zh) * 2015-04-21 2019-03-08 中国石油化工股份有限公司 一种两段重油浆态床加氢设备和方法
CN106147849B (zh) * 2015-04-21 2019-03-08 中国石油化工股份有限公司 一种两段重油浆态床加氢设备和方法
CN106147850B (zh) * 2015-04-23 2018-08-28 中国石油化工股份有限公司 一种重油浆态床加氢反应装置和应用方法
CN106147851B (zh) * 2015-04-23 2018-08-28 中国石油化工股份有限公司 一种重油浆态床加氢反应装置和应用方法
CN209247188U (zh) 2018-07-04 2019-08-13 Wika亚历山大·威甘德欧洲股份两合公司 热电偶结构和用于在容器中固定热电偶的结构
FR3097139A1 (fr) * 2019-06-14 2020-12-18 IFP Energies Nouvelles Reacteur triphasique a compartiments verticaux en serie avec separateurs intermediaires et procede d’hydroconversion de charges petrolieres lourdes
FR3097138A1 (fr) * 2019-06-14 2020-12-18 IFP Energies Nouvelles Reacteur triphasique a compartiments verticaux en serie et procede d’hydroconversion de charges petrolieres lourdes
CN112546968B (zh) * 2020-12-02 2022-04-19 中国科学院广州能源研究所 一种应用于生物航油加氢脱氧炼制的三相反应器与方法

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3644192A (en) * 1970-08-28 1972-02-22 Sik U Li Upflow three-phase fluidized bed coal liquefaction reactor system
GB9203958D0 (en) * 1992-02-25 1992-04-08 Norske Stats Oljeselskap Catalytic multi-phase reactor
GB9301723D0 (en) * 1993-01-28 1993-03-17 Norske Stats Oljeselskap Solid/liquid treatment apparatus and catalytic multi-phase reactor
GB2410906B (en) 2001-12-04 2006-07-12 Sasol Technology Slurry phase apparatus
DE602004015984D1 (de) * 2003-05-16 2008-10-02 Sasol Tech Pty Ltd Verfahren zur herstellung von flüssigen und gegebenenfalls gasförmigen produkten aus gasförmigen reaktanten
JPWO2005008470A1 (ja) 2003-07-16 2006-09-07 コニカミノルタフォトイメージング株式会社 プリンタ制御装置及びプリントシステム並びにプリント出力制御方法
CN1233454C (zh) 2003-09-28 2005-12-28 上海兖矿能源科技研发有限公司 一种用于三相浆态床反应器的气体分布器
WO2005084790A1 (en) 2004-03-08 2005-09-15 Shell Internationale Research Maatschappij B.V. Gas distributor for a reactor
GB2412612B (en) 2004-04-02 2008-10-29 Statoil Asa Slurry bubble column reactor
WO2007069317A1 (ja) * 2005-12-14 2007-06-21 Nippon Steel Engineering Co., Ltd. 気泡塔型フィッシャー・トロプシュ合成スラリー床反応システム
JP2007197636A (ja) * 2006-01-30 2007-08-09 Nippon Steel Engineering Co Ltd 気泡塔型炭化水素合成反応器
JP4874660B2 (ja) 2006-01-30 2012-02-15 新日鉄エンジニアリング株式会社 気泡塔型炭化水素合成反応器
BRPI0817732A2 (pt) * 2007-09-27 2015-03-31 Nippon Steel Eng Co Ltd Reator de síntese de hidrocarboneto tipo coluna de bolha, e processo de detecção de nível de pasta
CN101396647B (zh) 2007-09-29 2011-03-16 中科合成油技术有限公司 用于费-托合成的气-液-固三相悬浮床反应器及其应用
AU2011342806B2 (en) * 2010-12-13 2016-05-26 Sasol Technology (Proprietary) Limited Slurry phase apparatus
WO2015087211A1 (en) * 2013-12-11 2015-06-18 Sasol Technology Proprietary Limited A method of shutting down an operating three-phase slurry bubble column reactor

Also Published As

Publication number Publication date
CN103354764B (zh) 2016-03-16
BR112013014824A2 (pt) 2018-06-19
RU2566406C2 (ru) 2015-10-27
WO2012080933A1 (en) 2012-06-21
BR112013014824B1 (pt) 2019-12-17
AP3958A (en) 2016-12-23
US10322393B2 (en) 2019-06-18
CN103354764A (zh) 2013-10-16
NZ611549A (en) 2014-10-31
WO2012080933A8 (en) 2013-08-15
US9937476B2 (en) 2018-04-10
AP2013006960A0 (en) 2013-07-31
AR084260A1 (es) 2013-05-02
AU2011342806A1 (en) 2013-06-27
AU2011342806B2 (en) 2016-05-26
CA2819813A1 (en) 2012-06-21
US20140371334A1 (en) 2014-12-18
CA2819813C (en) 2017-11-14
RU2013132155A (ru) 2015-01-20
US20180117558A1 (en) 2018-05-03
PE20140504A1 (es) 2014-04-30

Similar Documents

Publication Publication Date Title
PL404311A1 (pl) Aparat z faza zawiesinowa
EA200900995A1 (ru) Способ сгущения и устройство для сгущения
AU2015253679A8 (en) Multiphase separation system
MY188508A (en) Flexibly adaptable membrane cartridges for the separation of fluids
MX368163B (es) Aparato para separación ciclónica de un flujo de fluido en una fase de gas y una fase líquida y contenedor proporcionado con tal aparato.
EP3000526A3 (en) Method for transferring precise small volumes of liquids
MX2016012330A (es) Sistemas y aparatos para separar fluidos y solidos de un orificio de pozo durante la produccion.
MX2013000224A (es) Columna de separacion de gas presurizado y proceso para generar un producto de gas a alta presion.
MX344465B (es) Sistema de separacion de celulas a traves de membrana por presion alternamente neumatica.
EP2132159A4 (en) HIGH SHEAR PROCESS FOR THE PRODUCTION OF CHLOROBENZENE
CA2932699C (en) A method of shutting down an operating three-phase slurry bubble column reactor
MX2016004969A (es) Sistema mejorado de separacion asistida por aire.
SG10201809230YA (en) Method for producing isobutylene from isobutanol
MY167448A (en) Multiphase separation system
MY167926A (en) Multiphase separation system cross-reference to related application
MY153988A (en) Synthesis reaction system
GB2438815A (en) Plate-type fluid bed reactor
MY182588A (en) Hydrocarbon synthesis reaction apparatus
MX2018007071A (es) Sistema de reduccion de oxigeno y metodo para operar un sistema de reduccion de oxigeno.
PH12019500105A1 (en) Apparatus and method for treating gypsum
PL406362A1 (pl) Sposób wytwarzania co najmniej jednego produktu z co najmniej jednego reagenta gazowego w złożu zawiesinowym
PL406361A1 (pl) Sposób wytwarzania co najmniej jednego produktu z co najmniej jednego reagenta gazowego w złożu zawiesinowym
RU2016140631A (ru) Способ управления статическим давлением в резервуаре сжиженного газа и в смесителе расклинивающего наполнителя
DK2479246T3 (da) Methansyntese ud fra syntesegas i en boblesøjlereaktor
MX2022003801A (es) Aparato de deposito de alimentacion, canaleta, planta y uso.