EA201070311A1 - Реактор синтеза углеводородов типа барботажной колонны и содержащая его реакционная система синтеза углеводородов - Google Patents

Реактор синтеза углеводородов типа барботажной колонны и содержащая его реакционная система синтеза углеводородов

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Publication number
EA201070311A1
EA201070311A1 EA201070311A EA201070311A EA201070311A1 EA 201070311 A1 EA201070311 A1 EA 201070311A1 EA 201070311 A EA201070311 A EA 201070311A EA 201070311 A EA201070311 A EA 201070311A EA 201070311 A1 EA201070311 A1 EA 201070311A1
Authority
EA
Eurasian Patent Office
Prior art keywords
reactor
synthesis
hydrocarbon
slurry
synthesis gas
Prior art date
Application number
EA201070311A
Other languages
English (en)
Other versions
EA017888B1 (ru
Inventor
Ясухиро Ониси
Юдзуру Като
Энити Ямада
Original Assignee
Ниппон Стил Инджиниринг Ко., Лтд.
Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн
Инпекс Корпорейшн
Ниппон Ойл Корпорейшн
Джапан Петролеум Эксплорейшн Ко., Лтд.
Космо Ойл Ко., Лтд.
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 Ниппон Стил Инджиниринг Ко., Лтд., Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн, Инпекс Корпорейшн, Ниппон Ойл Корпорейшн, Джапан Петролеум Эксплорейшн Ко., Лтд., Космо Ойл Ко., Лтд. filed Critical Ниппон Стил Инджиниринг Ко., Лтд.
Publication of EA201070311A1 publication Critical patent/EA201070311A1/ru
Publication of EA017888B1 publication Critical patent/EA017888B1/ru

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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
    • B01J8/20—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
    • 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
    • B01J2208/00141—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
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00327—Controlling the temperature by direct heat exchange
    • B01J2208/00336—Controlling the temperature by direct heat exchange adding a temperature modifying medium to the reactants
    • B01J2208/00353—Non-cryogenic fluids
    • B01J2208/00362—Liquid
    • 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
    • B01J2208/00327—Controlling the temperature by direct heat exchange
    • B01J2208/00336—Controlling the temperature by direct heat exchange adding a temperature modifying medium to the reactants
    • B01J2208/00353—Non-cryogenic fluids
    • B01J2208/00371—Non-cryogenic fluids gaseous
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002—Chemical plants
    • B01J2219/00004—Scale aspects
    • B01J2219/00006—Large-scale industrial plants
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00245—Avoiding undesirable reactions or side-effects
    • B01J2219/00259—Preventing runaway of the chemical reaction
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00245—Avoiding undesirable reactions or side-effects
    • B01J2219/00272—Addition of reaction inhibitor

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Combustion & Propulsion (AREA)
  • General Chemical & Material Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

Предлагается реактор синтеза углеводородов типа барботажной колонны, который синтезирует углеводородное соединение путем химической реакции синтез-газа, содержащего водород и моноксид углерода в качестве основных компонентов, и суспензии, содержащей суспензированные в ней частицы твердого катализатора. Реактор синтеза углеводородов включает в себя основное тело реактора, которое вмещает суспензию, секцию подачи синтез-газа, которая подает синтез-газ в суспензию, и вводную часть, которая вводит охлаждающую текучую среду, имеющую более низкую температуру, чем температура суспензии, в основное тело реактора.
EA201070311A 2007-09-27 2008-09-26 Реактор синтеза углеводородов типа барботажной колонны и содержащая его реакционная система синтеза углеводородов EA017888B1 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2007252521 2007-09-27
PCT/JP2008/067469 WO2009041604A1 (ja) 2007-09-27 2008-09-26 気泡塔型炭化水素合成反応器及びこれを備える炭化水素合成反応システム

Publications (2)

Publication Number Publication Date
EA201070311A1 true EA201070311A1 (ru) 2010-10-29
EA017888B1 EA017888B1 (ru) 2013-03-29

Family

ID=40511484

Family Applications (1)

Application Number Title Priority Date Filing Date
EA201070311A EA017888B1 (ru) 2007-09-27 2008-09-26 Реактор синтеза углеводородов типа барботажной колонны и содержащая его реакционная система синтеза углеводородов

Country Status (11)

Country Link
US (1) US20100247392A1 (ru)
EP (1) EP2199368B8 (ru)
JP (1) JP5220755B2 (ru)
CN (1) CN101918514A (ru)
AU (1) AU2008304826B8 (ru)
BR (1) BRPI0817733A2 (ru)
CA (1) CA2700098C (ru)
EA (1) EA017888B1 (ru)
MY (1) MY152110A (ru)
WO (1) WO2009041604A1 (ru)
ZA (1) ZA201002078B (ru)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5802397B2 (ja) * 2011-01-31 2015-10-28 独立行政法人石油天然ガス・金属鉱物資源機構 温度制御システム
JP5950500B2 (ja) * 2011-03-17 2016-07-13 独立行政法人石油天然ガス・金属鉱物資源機構 炭化水素の製造装置及び炭化水素の製造方法
JP5808559B2 (ja) 2011-03-31 2015-11-10 独立行政法人石油天然ガス・金属鉱物資源機構 炭化水素油の製造方法、フィッシャー・トロプシュ合成反応装置及び炭化水素油の製造システム
JP5815324B2 (ja) * 2011-08-05 2015-11-17 独立行政法人石油天然ガス・金属鉱物資源機構 温度制御システム
US8889747B2 (en) * 2011-10-11 2014-11-18 Bp Corporation North America Inc. Fischer Tropsch reactor with integrated organic rankine cycle
CN103285784B (zh) * 2013-06-13 2016-03-23 神华集团有限责任公司 费托合成三相浆态床及其反应器
JP6518480B2 (ja) * 2015-03-30 2019-05-22 株式会社クボタ 気泡塔型スラリー床反応装置
JP6518108B2 (ja) * 2015-03-30 2019-05-22 株式会社クボタ 気泡塔型スラリー床反応装置
CN113563923A (zh) * 2021-08-19 2021-10-29 中国石油化工股份有限公司 一种汽油加氢方法及汽油加氢装置

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2161974A (en) * 1937-01-21 1939-06-13 Standard Oil Dev Co Method of controlling exothermic reactions
US5900159A (en) * 1996-02-29 1999-05-04 Shell Oil Company Method for separating liquid from a slurry
US6160026A (en) * 1997-09-24 2000-12-12 Texaco Inc. Process for optimizing hydrocarbon synthesis
JP2004511619A (ja) * 2000-10-13 2004-04-15 ビーピー　エクスプロレーション　オペレーティング　カンパニー　リミテッド フィッシャートロプシュ合成法
US20030129110A1 (en) * 2001-12-04 2003-07-10 Sasol Technology (Proprietary) Limited Slurry phase apparatus
US6822006B1 (en) * 2003-07-02 2004-11-23 Chevron U.S.A. Inc. Methods of controlling the temperature of an exothermic reaction
JP2007252521A (ja) 2006-03-22 2007-10-04 Daiichi Shokai Co Ltd 遊技機

Also Published As

Publication number Publication date
JP5220755B2 (ja) 2013-06-26
AU2008304826A1 (en) 2009-04-02
EA017888B1 (ru) 2013-03-29
WO2009041604A1 (ja) 2009-04-02
CN101918514A (zh) 2010-12-15
ZA201002078B (en) 2011-05-25
EP2199368A1 (en) 2010-06-23
CA2700098A1 (en) 2009-04-02
EP2199368B8 (en) 2013-09-11
JPWO2009041604A1 (ja) 2011-01-27
US20100247392A1 (en) 2010-09-30
AU2008304826B8 (en) 2011-10-27
CA2700098C (en) 2013-04-30
AU2008304826B2 (en) 2011-09-08
BRPI0817733A2 (pt) 2015-03-31
MY152110A (en) 2014-08-15
EP2199368A4 (en) 2011-12-14
EP2199368B1 (en) 2013-06-05

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MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): AM AZ BY KG MD TJ

MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): KZ TM RU