EA201390250A1 - Способ изготовления углеводородного масла и система для изготовления углеводородного масла - Google Patents

Способ изготовления углеводородного масла и система для изготовления углеводородного масла

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Publication number
EA201390250A1
EA201390250A1 EA201390250A EA201390250A EA201390250A1 EA 201390250 A1 EA201390250 A1 EA 201390250A1 EA 201390250 A EA201390250 A EA 201390250A EA 201390250 A EA201390250 A EA 201390250A EA 201390250 A1 EA201390250 A1 EA 201390250A1
Authority
EA
Eurasian Patent Office
Prior art keywords
oil
catalyst
hydrocarbon oil
fraction
storage tank
Prior art date
Application number
EA201390250A
Other languages
English (en)
Other versions
EA023903B1 (ru
Inventor
Марие Ивама
Казухико Тасака
Юити Танака
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 EA201390250A1 publication Critical patent/EA201390250A1/ru
Publication of EA023903B1 publication Critical patent/EA023903B1/ru

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/009—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in combination with chemical reactions
    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • 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
    • B01J8/007—Separating solid material from the gas/liquid stream by sedimentation
    • 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
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/02—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
    • C07C1/04—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
    • 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
    • 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
    • C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
    • 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
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/201—Impurities
    • C10G2300/208—Sediments, e.g. bottom sediment and water or BSW

Landscapes

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

Abstract

Предложен способ изготовления углеводородного масла, в котором можно задерживать мелкие частицы катализатора, образующиеся из катализатора для синтеза FT, от поступления в реакционную систему на стадии повышения качества синтетического масла FT. Данный способ изготовления углеводородного масла включает проведение синтеза Фишера-Тропша с использованием реактора с суспензионным слоем (С2), в котором находится жидкая углеводородная суспензия, содержащая суспендированный катализатор, в результате чего получается углеводородное масло, которое содержит мелкие частицы катализатора, образующиеся из катализатора; фракционирование углеводородного масла на дистиллированное масло и кубовую фракцию масла, содержащую мелкие частицы катализатора, с помощью ректификационной колонны (С4); поступление, по меньшей мере, некоторой части кубовой фракции масла в накопительный резервуар (Т2); осаждение мелких частиц катализатора на дне накопительного резервуара (Т2) и сбор осажденных частиц; поступление остатка кубовой фракции масла из ректификационной колонны (С4) в установку гидрокрекинга (С6) и/или поступление надосадочной кубовой фракции масла, из которой мелкие частицы катализатора были собраны посредством накопительного резервуара (Т2), из накопительного резервуара (Т2) в установку гидрокрекинга (С6); и гидрокрекинг остатка кубовой фракции масла и/или надосадочной кубовой фракции масла с помощью установки гидрокрекинга (С6).
EA201390250A 2010-08-19 2011-08-12 Способ и система для изготовления углеводородного масла EA023903B1 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2010184085A JP5764307B2 (ja) 2010-08-19 2010-08-19 炭化水素油の製造方法及び炭化水素油の製造システム
PCT/JP2011/068481 WO2012023527A1 (ja) 2010-08-19 2011-08-12 炭化水素油の製造方法及び炭化水素油の製造システム

Publications (2)

Publication Number Publication Date
EA201390250A1 true EA201390250A1 (ru) 2013-07-30
EA023903B1 EA023903B1 (ru) 2016-07-29

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
EA201390250A EA023903B1 (ru) 2010-08-19 2011-08-12 Способ и система для изготовления углеводородного масла

Country Status (10)

Country Link
US (2) US8906969B2 (ru)
EP (1) EP2607454B1 (ru)
JP (1) JP5764307B2 (ru)
CN (1) CN103228765B (ru)
AU (1) AU2011291804B2 (ru)
BR (1) BR112013003872A2 (ru)
CA (1) CA2806285C (ru)
EA (1) EA023903B1 (ru)
MY (1) MY163361A (ru)
WO (1) WO2012023527A1 (ru)

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JP5757704B2 (ja) 2010-08-19 2015-07-29 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及び炭化水素油の製造システム
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US9562200B2 (en) 2012-03-30 2017-02-07 Jx Nippon Oil & Energy Corporation Method for producing lubricant base oil
EP3144369A1 (de) * 2015-09-18 2017-03-22 Linde Aktiengesellschaft Verfahren und anlage zur trenntechnischen bearbeitung eines kohlenwasserstoffe und schwefelverbindungen enthaltenden stoffgemischs

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Also Published As

Publication number Publication date
BR112013003872A2 (pt) 2016-06-07
EP2607454A4 (en) 2014-04-30
CA2806285C (en) 2016-12-06
MY163361A (en) 2017-09-15
JP2012041450A (ja) 2012-03-01
US8906969B2 (en) 2014-12-09
EP2607454A1 (en) 2013-06-26
AU2011291804B2 (en) 2016-03-10
JP5764307B2 (ja) 2015-08-19
AU2011291804A1 (en) 2013-02-14
CN103228765B (zh) 2015-07-22
EA023903B1 (ru) 2016-07-29
CA2806285A1 (en) 2012-02-23
EP2607454B1 (en) 2015-10-07
US20140377142A1 (en) 2014-12-25
CN103228765A (zh) 2013-07-31
WO2012023527A1 (ja) 2012-02-23
US20130143971A1 (en) 2013-06-06

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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