EA201590702A1 - Способ запуска реакторной установки синтеза углеводородов - Google Patents

Способ запуска реакторной установки синтеза углеводородов

Info

Publication number
EA201590702A1
EA201590702A1 EA201590702A EA201590702A EA201590702A1 EA 201590702 A1 EA201590702 A1 EA 201590702A1 EA 201590702 A EA201590702 A EA 201590702A EA 201590702 A EA201590702 A EA 201590702A EA 201590702 A1 EA201590702 A1 EA 201590702A1
Authority
EA
Eurasian Patent Office
Prior art keywords
reactor
suspension
starting
hydrocarbon synthesis
reactor installation
Prior art date
Application number
EA201590702A
Other languages
English (en)
Other versions
EA029608B1 (ru
Inventor
Такео Ито
Ацуси Мурата
Эиити Ямада
Юдзуру Като
Ясухиро Ониси
Original Assignee
Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн
Инпекс Корпорейшн
ДжейЭкс НИППОН ОЙЛ ЭНД ЭНЕРДЖИ КОРПОРЕЙШН
Джапан Петролеум Эксплорейшн Ко., Лтд.
Космо Ойл Ко., Лтд.
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 Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн, Инпекс Корпорейшн, ДжейЭкс НИППОН ОЙЛ ЭНД ЭНЕРДЖИ КОРПОРЕЙШН, Джапан Петролеум Эксплорейшн Ко., Лтд., Космо Ойл Ко., Лтд., Ниппон Стил Энд Сумикин Инджиниринг Ко., Лтд. filed Critical Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн
Publication of EA201590702A1 publication Critical patent/EA201590702A1/ru
Publication of EA029608B1 publication Critical patent/EA029608B1/ru

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
    • 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
    • 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
    • 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
    • C10G2300/4031—Start up or shut down operations

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (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)

Abstract

Способ пуска реакторной установки для синтеза углеводородов, включающий начальную стадию загрузки суспензии, на которой суспензию загружают в реактор на начальной стадии реакции синтеза Фишера-Тропша с более низкой скоростью загрузки, чем применяется для загрузки реактора в стационарном режиме работы; и стадию повышения степени конверсии СО, на которой уровень жидкости суспензии в реакторе повышается за счет добавления к суспензии углеводородов, образовавшихся на ранней стадии реакции синтеза Фишера-Тропша, так что степень конверсии СО увеличивается пропорционально повышению уровня жидкости суспензии в реакторе.
EA201590702A 2012-11-09 2013-11-06 Способ запуска реакторной установки синтеза углеводородов EA029608B1 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2012247727A JP6088214B2 (ja) 2012-11-09 2012-11-09 炭化水素合成反応装置のスタートアップ方法
PCT/JP2013/080027 WO2014073575A1 (ja) 2012-11-09 2013-11-06 炭化水素合成反応装置のスタートアップ方法

Publications (2)

Publication Number Publication Date
EA201590702A1 true EA201590702A1 (ru) 2015-08-31
EA029608B1 EA029608B1 (ru) 2018-04-30

Family

ID=50684677

Family Applications (1)

Application Number Title Priority Date Filing Date
EA201590702A EA029608B1 (ru) 2012-11-09 2013-11-06 Способ запуска реакторной установки синтеза углеводородов

Country Status (12)

Country Link
US (1) US9404047B2 (ru)
EP (1) EP2918659B1 (ru)
JP (1) JP6088214B2 (ru)
CN (1) CN104769079B (ru)
AP (1) AP2015008412A0 (ru)
AU (1) AU2013342524B2 (ru)
BR (1) BR112015009621B1 (ru)
CA (1) CA2889863C (ru)
EA (1) EA029608B1 (ru)
MY (1) MY183355A (ru)
WO (1) WO2014073575A1 (ru)
ZA (1) ZA201503757B (ru)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA3133710C (en) * 2015-11-02 2023-10-24 Pura Scents, Inc. Scent dispensation
FR3044565B1 (fr) * 2015-12-08 2017-12-01 Ifp Energies Now Chargement d'un catalyseur dans une colonne a bulles pour la synthese fischer-tropsch

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7096931B2 (en) * 2001-06-08 2006-08-29 Exxonmobil Research And Engineering Company Increased heat exchange in two or three phase slurry
GB2401112C (en) 2002-02-13 2007-01-16 Sasol Technology Process for starting up a fischer-tropsch reactor
US7855236B2 (en) * 2005-12-09 2010-12-21 Shell Oil Company Method to start a process for producing hydrocarbons from synthesis gas
EP2199369A1 (en) * 2007-09-27 2010-06-23 Nippon Steel Engineering Co., Ltd Bubbling tower hydrocarbon reactor and method of detecting slurry surface level
JP5296478B2 (ja) 2008-09-30 2013-09-25 Ｊｘ日鉱日石エネルギー株式会社 精留塔のスタートアップ方法
JP5730102B2 (ja) * 2011-03-31 2015-06-03 独立行政法人石油天然ガス・金属鉱物資源機構 気泡塔型スラリー床反応器のスタートアップ方法及びスタートアップ用溶媒並びに炭化水素油の製造方法

Also Published As

Publication number Publication date
US20150267123A1 (en) 2015-09-24
JP2014095040A (ja) 2014-05-22
BR112015009621B1 (pt) 2020-05-05
CN104769079A (zh) 2015-07-08
US9404047B2 (en) 2016-08-02
AP2015008412A0 (en) 2015-05-31
WO2014073575A1 (ja) 2014-05-15
MY183355A (en) 2021-02-18
CA2889863C (en) 2017-03-14
BR112015009621A2 (pt) 2017-07-04
EP2918659A4 (en) 2016-07-13
ZA201503757B (en) 2016-11-30
EP2918659B1 (en) 2017-08-09
JP6088214B2 (ja) 2017-03-01
AU2013342524A1 (en) 2015-05-14
CA2889863A1 (en) 2014-05-15
CN104769079B (zh) 2016-08-24
EA029608B1 (ru) 2018-04-30
AU2013342524B2 (en) 2016-01-28
EP2918659A1 (en) 2015-09-16

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Legal Events

Date Code Title Description
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