RU2008143258A - METHOD FOR PRODUCING LIQUID BASIC FUEL - Google Patents

METHOD FOR PRODUCING LIQUID BASIC FUEL Download PDF

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Publication number
RU2008143258A
RU2008143258A RU2008143258/04A RU2008143258A RU2008143258A RU 2008143258 A RU2008143258 A RU 2008143258A RU 2008143258/04 A RU2008143258/04 A RU 2008143258/04A RU 2008143258 A RU2008143258 A RU 2008143258A RU 2008143258 A RU2008143258 A RU 2008143258A
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RU
Russia
Prior art keywords
base fuel
liquid base
producing
fuel according
hydrocracking
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RU2008143258/04A
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Russian (ru)
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RU2428456C2 (en
Inventor
Хироюки СЕКИ (JP)
Хироюки СЕКИ
Масахиро ХИГАСИ (JP)
Масахиро ХИГАСИ
Хирофуми КОННО (JP)
Хирофуми КОННО
Original Assignee
Ниппон Ойл Корпорейшн (Jp)
Ниппон Ойл Корпорейшн
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Application filed by Ниппон Ойл Корпорейшн (Jp), Ниппон Ойл Корпорейшн filed Critical Ниппон Ойл Корпорейшн (Jp)
Publication of RU2008143258A publication Critical patent/RU2008143258A/en
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Publication of RU2428456C2 publication Critical patent/RU2428456C2/en

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    • 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
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/10—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y containing iron group metals, noble metals or copper
    • B01J29/12—Noble metals
    • B01J29/126—Y-type faujasite
    • 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
    • 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
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/10—After treatment, characterised by the effect to be obtained
    • B01J2229/20—After treatment, characterised by the effect to be obtained to introduce other elements in the catalyst composition comprising the molecular sieve, but not specially in or on the molecular sieve itself
    • 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
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/30—After treatment, characterised by the means used
    • B01J2229/42—Addition of matrix or binder particles
    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst

Abstract

1. Способ производства жидкого базового топлива, который содержит гидрокрекинг парафинового углеводорода в присутствии катализатора гидрокрекинга, который содержит USY цеолит, имеющий средний размер частиц 0,8 мкм или менее, чтобы достичь скорости разложения от 75 до 90 мас.%, как определяется следующим уравнением (1) ! ! 2. Способ производства жидкого базового топлива по п.1, в котором катализатор гидрокрекинга содержит USY цеолит, имеющий средний размер частиц 0,5 мкм или менее. ! 3. Способ производства жидкого базового топлива по п.1 или 2, в котором катализатор гидрокрекинга содержит алюмоборный окисный катализатор. ! 4. Способ производства жидкого базового топлива по п.1 или 2, в котором парафиновый углеводород представляет собой парафин, приготовленный посредством синтеза Фишера-Тропша. 1. A method of manufacturing a liquid base fuel that contains hydrocracking a paraffin hydrocarbon in the presence of a hydrocracking catalyst that contains a USY zeolite having an average particle size of 0.8 μm or less, to achieve a decomposition rate of 75 to 90 wt.%, As determined by the following equation (one) ! ! 2. A method for producing a liquid base fuel according to claim 1, wherein the hydrocracking catalyst comprises a USY zeolite having an average particle size of 0.5 microns or less. ! 3. A method of manufacturing a liquid base fuel according to claim 1 or 2, in which the hydrocracking catalyst contains alumina oxide catalyst. ! 4. A method for producing a liquid base fuel according to claim 1 or 2, wherein the paraffin hydrocarbon is paraffin prepared by Fischer-Tropsch synthesis.

Claims (4)

1. Способ производства жидкого базового топлива, который содержит гидрокрекинг парафинового углеводорода в присутствии катализатора гидрокрекинга, который содержит USY цеолит, имеющий средний размер частиц 0,8 мкм или менее, чтобы достичь скорости разложения от 75 до 90 мас.%, как определяется следующим уравнением (1)1. A method of producing a liquid base fuel that contains hydrocracking a paraffin hydrocarbon in the presence of a hydrocracking catalyst that contains a USY zeolite having an average particle size of 0.8 μm or less, to achieve a decomposition rate of 75 to 90 wt.%, As determined by the following equation (one)
Figure 00000001
Figure 00000002
Figure 00000001
Figure 00000002
 2. Способ производства жидкого базового топлива по п.1, в котором катализатор гидрокрекинга содержит USY цеолит, имеющий средний размер частиц 0,5 мкм или менее.2. A method for producing a liquid base fuel according to claim 1, wherein the hydrocracking catalyst comprises a USY zeolite having an average particle size of 0.5 microns or less. 3. Способ производства жидкого базового топлива по п.1 или 2, в котором катализатор гидрокрекинга содержит алюмоборный окисный катализатор.3. A method of manufacturing a liquid base fuel according to claim 1 or 2, in which the hydrocracking catalyst contains alumina oxide catalyst. 4. Способ производства жидкого базового топлива по п.1 или 2, в котором парафиновый углеводород представляет собой парафин, приготовленный посредством синтеза Фишера-Тропша. 4. A method for producing a liquid base fuel according to claim 1 or 2, wherein the paraffin hydrocarbon is paraffin prepared by Fischer-Tropsch synthesis.
RU2008143258/04A 2006-03-31 2007-03-13 Method of producing liquid base fuel RU2428456C2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2006100182A JP2007270061A (en) 2006-03-31 2006-03-31 Method for producing liquid fuel base
JP2006-100182 2006-03-31

Publications (2)

Publication Number Publication Date
RU2008143258A true RU2008143258A (en) 2010-05-10
RU2428456C2 RU2428456C2 (en) 2011-09-10

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Country Status (6)

Country Link
JP (1) JP2007270061A (en)
CN (1) CN101410488B (en)
AU (1) AU2007231962B2 (en)
MY (1) MY148342A (en)
RU (1) RU2428456C2 (en)
WO (1) WO2007114003A1 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8345890B2 (en) 2006-01-05 2013-01-01 Audience, Inc. System and method for utilizing inter-microphone level differences for speech enhancement
US8744844B2 (en) 2007-07-06 2014-06-03 Audience, Inc. System and method for adaptive intelligent noise suppression
US8143620B1 (en) 2007-12-21 2012-03-27 Audience, Inc. System and method for adaptive classification of audio sources
JP5730104B2 (en) * 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 Support selection method and hydrotreating catalyst production method

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4919786A (en) * 1987-12-18 1990-04-24 Exxon Research And Engineering Company Process for the hydroisomerization of was to produce middle distillate products (OP-3403)
US5814109A (en) * 1997-02-07 1998-09-29 Exxon Research And Engineering Company Diesel additive for improving cetane, lubricity, and stability
AU2003266527A1 (en) * 2002-09-24 2004-04-19 Nippon Oil Corporation Hydrocracking catalyst and process for production of liquid hydrocarbons
JP4047206B2 (en) * 2003-03-20 2008-02-13 株式会社ジャパンエナジー Environment-friendly diesel oil and method for producing the same
JP4313237B2 (en) * 2004-03-29 2009-08-12 新日本石油株式会社 Hydrocracking catalyst and method for producing liquid hydrocarbon

Also Published As

Publication number Publication date
AU2007231962B2 (en) 2011-09-01
JP2007270061A (en) 2007-10-18
WO2007114003A1 (en) 2007-10-11
MY148342A (en) 2013-03-29
AU2007231962A1 (en) 2007-10-11
CN101410488A (en) 2009-04-15
RU2428456C2 (en) 2011-09-10
CN101410488B (en) 2013-08-21

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