EA201690266A1 - Реактор для синтеза углеводородов - Google Patents

Реактор для синтеза углеводородов

Info

Publication number
EA201690266A1
EA201690266A1 EA201690266A EA201690266A EA201690266A1 EA 201690266 A1 EA201690266 A1 EA 201690266A1 EA 201690266 A EA201690266 A EA 201690266A EA 201690266 A EA201690266 A EA 201690266A EA 201690266 A1 EA201690266 A1 EA 201690266A1
Authority
EA
Eurasian Patent Office
Prior art keywords
reactor
main body
synthesis gas
supply line
distribution pipe
Prior art date
Application number
EA201690266A
Other languages
English (en)
Other versions
EA032167B1 (ru
Inventor
Кентароу Морита
Казуки Мурахаси
Еиити Ямада
Юдзуру Като
Йосиюки Саиваи
Ацуси Мурата
Original Assignee
Ниппон Стил Энд Сумикин Инджиниринг 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 Энд Сумикин Инджиниринг Ко., Лтд. filed Critical Ниппон Стил Энд Сумикин Инджиниринг Ко., Лтд.
Publication of EA201690266A1 publication Critical patent/EA201690266A1/ru
Publication of EA032167B1 publication Critical patent/EA032167B1/ru

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
    • B01J8/20—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
    • 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
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
    • B01J4/004—Sparger-type 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
    • 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
    • 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
    • C10G2/343—Apparatus, reactors with moving solid catalysts according to the "moving-bed" method
    • 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
    • B01J2208/00796—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

Landscapes

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

Abstract

Настоящее изобретение относится к реактору, который включает основной корпус (4) реактора, имеющий трубчатую форму с осью (О) по центру, в котором находится суспензия (S); линия 10 для подачи газа, предназначенная для введения синтез-газа (G) в основной корпус (4) реактора; и барботажная часть (5), расположенная в нижней части основного корпуса (4) реактора, которая сообщается с линией 10 для подачи газа и обеспечивает распыление синтез-газа (G). Барботажная часть (5) включает распределительную трубу (15), в которой имеется множество отверстий, отделенных друг от друга в первом направлении, через которые распыляется синтез-газ (G), и пару поверхностных частей стенки, которые выступают из распределительной трубы (15) на противоположных сторонах от множества отверстий в направлении, перпендикулярном первому направлению.
EA201690266A 2013-07-30 2014-07-15 Реактор для синтеза углеводородов EA032167B1 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2013157820A JP6145348B2 (ja) 2013-07-30 2013-07-30 炭化水素合成用の反応器
PCT/JP2014/068802 WO2015016060A1 (ja) 2013-07-30 2014-07-15 炭化水素合成用の反応器

Publications (2)

Publication Number Publication Date
EA201690266A1 true EA201690266A1 (ru) 2016-06-30
EA032167B1 EA032167B1 (ru) 2019-04-30

Family

ID=52431600

Family Applications (1)

Application Number Title Priority Date Filing Date
EA201690266A EA032167B1 (ru) 2013-07-30 2014-07-15 Реактор для синтеза углеводородов

Country Status (7)

Country Link
US (1) US9687805B2 (ru)
JP (1) JP6145348B2 (ru)
AP (1) AP2016009024A0 (ru)
AU (1) AU2014297501B2 (ru)
CA (1) CA2918676C (ru)
EA (1) EA032167B1 (ru)
WO (1) WO2015016060A1 (ru)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
CN108794294B (zh) 2017-04-27 2020-12-11 中国科学院大连化学物理研究所 流化床气体分布器、应用其的反应器及生产对二甲苯联产低碳烯烃的方法
CN108786669B (zh) 2017-04-27 2021-01-12 中国科学院大连化学物理研究所 流化床气体分布器、应用其的反应器及生产对二甲苯联产低碳烯烃的方法
KR20220037214A (ko) * 2020-09-17 2022-03-24 주식회사 엘지화학 스파저 및 이를 포함하는 반응기

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5569434A (en) * 1994-10-10 1996-10-29 Amoco Corporation Hydrocarbon processing apparatus and method
GB0013793D0 (en) * 2000-06-06 2000-07-26 Bp Amoco Plc Process
US7448601B2 (en) 2004-03-08 2008-11-11 Shell Oil Company Gas distributor for a reactor
GB2412612B (en) * 2004-04-02 2008-10-29 Statoil Asa Slurry bubble column reactor
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
CA2738058C (en) 2008-09-30 2015-04-28 Cosmo Oil Co., Ltd. Liquid-fuel synthesizing method and liquid-fuel synthesizing apparatus
GB2465554B (en) * 2008-11-18 2013-03-13 Gtl F1 Ag Slurry bubble column reactor

Also Published As

Publication number Publication date
JP2015027963A (ja) 2015-02-12
AU2014297501A1 (en) 2016-02-18
CA2918676A1 (en) 2015-02-05
AP2016009024A0 (en) 2016-02-29
JP6145348B2 (ja) 2017-06-07
AU2014297501B2 (en) 2017-09-07
CA2918676C (en) 2018-07-17
WO2015016060A1 (ja) 2015-02-05
US9687805B2 (en) 2017-06-27
US20160160129A1 (en) 2016-06-09
EA032167B1 (ru) 2019-04-30

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Legal Events

Date Code Title Description
TC4A Change in name of a patent proprietor in a eurasian patent
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 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