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RU2008143262A - Состав топлива - Google Patents

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Publication number
RU2008143262A
RU2008143262A RU2008143262/04A RU2008143262A RU2008143262A RU 2008143262 A RU2008143262 A RU 2008143262A RU 2008143262/04 A RU2008143262/04 A RU 2008143262/04A RU 2008143262 A RU2008143262 A RU 2008143262A RU 2008143262 A RU2008143262 A RU 2008143262A
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RU
Russia
Prior art keywords
vol
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fuel composition
fraction obtained
hydrocarbon mixture
Prior art date
Application number
RU2008143262/04A
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English (en)
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RU2414502C2 (ru
Inventor
Масанори ХИРОСЕ (JP)
Масанори ХИРОСЕ
Хидеси ИКИ (JP)
Хидеси ИКИ
Original Assignee
Ниппон Йол Корпорейшн (Jp)
Ниппон Йол Корпорейшн
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Publication of RU2008143262A publication Critical patent/RU2008143262A/ru
Application granted granted Critical
Publication of RU2414502C2 publication Critical patent/RU2414502C2/ru

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
    • C10L1/08—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for compression ignition
    • 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
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • C10G47/12—Inorganic carriers
    • C10G47/16—Crystalline alumino-silicate carriers
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/06—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • C10G45/08—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
    • 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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/14—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural parallel stages only
    • 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
    • C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
    • C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
    • C10G69/04—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one step of catalytic cracking in the absence of hydrogen
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/16—Hydrocarbons
    • 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
    • C10G2300/10—Feedstock materials
    • C10G2300/1022—Fischer-Tropsch products
    • 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
    • C10G2300/10—Feedstock materials
    • C10G2300/1096—Aromatics or polyaromatics
    • 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
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/301—Boiling range

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)
  • Crystallography & Structural Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Abstract

1. Состав топлива с точкой вспышки 45°C или выше, содержащий синтетическую нефть Фишера-Тропша и углеводородную смесь А на основе нефти, имеющий следующие свойства от (1) до (5) в количестве от 10 до 30 об.% на основе общей массы состава: ! (1) плотность при 15°С: 800 кг/см3 или выше и 900 кг/м3 или ниже; ! (2) температура перегонки 10 об.% (T10): 150°C или выше и 200°C или ниже; ! (3) температура перегонки 97 об.% (T97): 270°C или ниже; ! (4) содержание ароматических соединений: 40 об.% или выше и 70 об.% или ниже; и ! (5) содержание серы: 30 частей на миллион по массе или ниже. ! 2. Состав топлива по п.1, в котором углеводородная смесь А на основе нефти представляет собой фракцию, полученную посредством установки каталитического крекинга. ! 3. Состав топлива по п.1, в котором углеводородная смесь А на основе нефти представляет собой фракцию, полученную гидродесульфуризацией фракции, полученной посредством установки каталитического крекинга при условиях, где температура реакции составляет 250°C или выше и 310°C или ниже, давление водорода составляет 5 МПа или выше и 10 МПа или ниже, LHSV составляет 0,5 ч-1 или выше и 3,0 ч-1 или ниже, и объемное отношение водород/углеводород составляет 0,15 или выше и 0,6 или ниже, используя катализатор, содержащий любой из Ni-W, Ni-Mo, Co-Mo, Co-W или Ni-Co-Mo.

Claims (3)

1. Состав топлива с точкой вспышки 45°C или выше, содержащий синтетическую нефть Фишера-Тропша и углеводородную смесь А на основе нефти, имеющий следующие свойства от (1) до (5) в количестве от 10 до 30 об.% на основе общей массы состава:
(1) плотность при 15°С: 800 кг/см3 или выше и 900 кг/м3 или ниже;
(2) температура перегонки 10 об.% (T10): 150°C или выше и 200°C или ниже;
(3) температура перегонки 97 об.% (T97): 270°C или ниже;
(4) содержание ароматических соединений: 40 об.% или выше и 70 об.% или ниже; и
(5) содержание серы: 30 частей на миллион по массе или ниже.
2. Состав топлива по п.1, в котором углеводородная смесь А на основе нефти представляет собой фракцию, полученную посредством установки каталитического крекинга.
3. Состав топлива по п.1, в котором углеводородная смесь А на основе нефти представляет собой фракцию, полученную гидродесульфуризацией фракции, полученной посредством установки каталитического крекинга при условиях, где температура реакции составляет 250°C или выше и 310°C или ниже, давление водорода составляет 5 МПа или выше и 10 МПа или ниже, LHSV составляет 0,5 ч-1 или выше и 3,0 ч-1 или ниже, и объемное отношение водород/углеводород составляет 0,15 или выше и 0,6 или ниже, используя катализатор, содержащий любой из Ni-W, Ni-Mo, Co-Mo, Co-W или Ni-Co-Mo.
RU2008143262/04A 2006-03-31 2007-02-22 Состав топлива RU2414502C2 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2006-099603 2006-03-31
JP2006099603A JP4829660B2 (ja) 2006-03-31 2006-03-31 燃料組成物

Publications (2)

Publication Number Publication Date
RU2008143262A true RU2008143262A (ru) 2010-05-10
RU2414502C2 RU2414502C2 (ru) 2011-03-20

Family

ID=38563232

Family Applications (1)

Application Number Title Priority Date Filing Date
RU2008143262/04A RU2414502C2 (ru) 2006-03-31 2007-02-22 Состав топлива

Country Status (9)

Country Link
US (1) US7914593B2 (ru)
EP (1) EP2006358B1 (ru)
JP (1) JP4829660B2 (ru)
KR (1) KR101291421B1 (ru)
CN (1) CN101410496B (ru)
AU (1) AU2007232008B2 (ru)
MY (1) MY144535A (ru)
RU (1) RU2414502C2 (ru)
WO (1) WO2007113960A1 (ru)

Families Citing this family (4)

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Publication number Priority date Publication date Assignee Title
KR101360487B1 (ko) 2006-03-31 2014-02-07 제이엑스 닛코닛세키에너지주식회사 경유조성물
JP4863772B2 (ja) * 2006-05-31 2012-01-25 Ｊｘ日鉱日石エネルギー株式会社 軽油組成物
US8361309B2 (en) * 2008-06-19 2013-01-29 Chevron U.S.A. Inc. Diesel composition and method of making the same
JP6008534B2 (ja) * 2012-03-28 2016-10-19 独立行政法人石油天然ガス・金属鉱物資源機構 ディーゼル燃料又はディーゼル燃料基材の製造方法

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Publication number Priority date Publication date Assignee Title
RU2149888C1 (ru) * 1999-04-07 2000-05-27 Уфимский государственный нефтяной технический университет Способ получения судового маловязкого топлива
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US6663767B1 (en) * 2000-05-02 2003-12-16 Exxonmobil Research And Engineering Company Low sulfur, low emission blends of fischer-tropsch and conventional diesel fuels
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MY140444A (en) 2002-04-25 2009-12-31 Shell Int Research Diesel fuel compositions
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JP4580152B2 (ja) * 2003-06-12 2010-11-10 出光興産株式会社 ディーゼルエンジン用燃料油

Also Published As

Publication number Publication date
AU2007232008B2 (en) 2011-02-17
KR101291421B1 (ko) 2013-07-30
EP2006358A2 (en) 2008-12-24
JP2007270035A (ja) 2007-10-18
CN101410496B (zh) 2014-09-17
EP2006358B1 (en) 2014-12-03
EP2006358A4 (en) 2013-03-13
US20090126264A1 (en) 2009-05-21
RU2414502C2 (ru) 2011-03-20
KR20090026122A (ko) 2009-03-11
EP2006358A9 (en) 2009-07-15
AU2007232008A1 (en) 2007-10-11
CN101410496A (zh) 2009-04-15
WO2007113960A1 (ja) 2007-10-11
JP4829660B2 (ja) 2011-12-07
US7914593B2 (en) 2011-03-29
MY144535A (en) 2011-09-30

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Effective date: 20190223