JP2007514844A5 - - Google Patents

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Publication number
JP2007514844A5
JP2007514844A5 JP2006545519A JP2006545519A JP2007514844A5 JP 2007514844 A5 JP2007514844 A5 JP 2007514844A5 JP 2006545519 A JP2006545519 A JP 2006545519A JP 2006545519 A JP2006545519 A JP 2006545519A JP 2007514844 A5 JP2007514844 A5 JP 2007514844A5
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crude product
product according
catalysts
boiling point
mpa
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JP2006545519A
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JP2007514844A (en
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Priority claimed from PCT/US2004/042638 external-priority patent/WO2005063932A2/en
Publication of JP2007514844A publication Critical patent/JP2007514844A/en
Publication of JP2007514844A5 publication Critical patent/JP2007514844A5/ja
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Claims (11)

それぞれ原油生成物１ｇ当たり、残留物を０．０５ｇ以下、沸点範囲分布が０．１０１ＭＰａにおいて２０４℃（４００°Ｆ）以下の炭化水素を０．００１ｇ以上、沸点範囲分布が０．１０１ＭＰａにおいて２０４〜３００℃の炭化水素を０．００１ｇ以上、沸点範囲分布が０．１０１ＭＰａにおいて３００〜４００℃の炭化水素を０．００１ｇ以上、沸点範囲分布が０．１０１ＭＰａにおいて４００〜５３８℃（１０００°Ｆ）の炭化水素を０．００１ｇ以上、及び触媒の少なくとも１種が１種以上のアルカリ金属を含有する１種以上の触媒を、０ｇを超え０．０１ｇ未満、含有する、ＳＴＰにおいて液体である原油生成物。 For each 1 g of crude product, the residue is 0.05 g or less, the boiling point range distribution is 0.001 g or more at 204 ° C. (400 ° F.) or less at a boiling point range distribution of 0.101 MPa, and the boiling point range distribution is 204 to 1 at 0.101 MPa. 0.001 g or more of hydrocarbon at 300 ° C., 0.001 g or more of hydrocarbon at 300 to 400 ° C. at boiling point range distribution of 0.101 MPa, and 400 to 538 ° C. (1000 ° F.) at boiling point range distribution of 0.101 MPa Crude oil product that is liquid in STP , containing more than 0.001 g hydrocarbon and more than 0 g and less than 0.01 g of at least one catalyst containing one or more alkali metals. . 触媒の少なくとも１種は、５０〜５００℃の温度範囲で放出ガスの放出ガス変曲点〔生成物の時間分析（ＴＡＰ）で測定〕を示し、及び／又は触媒の少なくとも１種は、２００〜５００℃の温度範囲で解離熱（示差走査熱量測定法により１分当たり１０℃の加熱速度で測定）を示す請求項１に記載の原油生成物。   At least one of the catalysts exhibits an outgassing inflection point (measured by product time analysis (TAP)) in the temperature range of 50-500 ° C. and / or at least one of the catalysts is 200- The crude product according to claim 1, which exhibits a heat of dissociation (measured at a heating rate of 10 ° C per minute by differential scanning calorimetry) in a temperature range of 500 ° C. 触媒の少なくとも１種は、更に遷移金属を含有する請求項１又は２に記載の原油生成物。   The crude product according to claim 1 or 2, wherein at least one of the catalysts further contains a transition metal. 触媒の少なくとも１種は、更に遷移金属硫化物を含有する請求項１〜３のいずれか１項に記載の原油生成物。   The crude product according to any one of claims 1 to 3, wherein at least one of the catalysts further contains a transition metal sulfide. アルカリ金属対遷移金属の原子比が、０を超え１以下である請求項４に記載の原油生成物。   The crude product of claim 4, wherein the atomic ratio of alkali metal to transition metal is greater than 0 and less than or equal to 1. アルカリ金属が、ナトリウム、カリウム、ルビジウム、セシウム又はそれらの混合物を含む請求項１〜５のいずれか１項に記載の原油生成物。   The crude product according to any one of claims 1 to 5, wherein the alkali metal comprises sodium, potassium, rubidium, cesium or a mixture thereof. 触媒の少なくとも１種が、バートナイトを含有する請求項１〜６のいずれか１項に記載の原油生成物。   The crude product according to any one of claims 1 to 6, wherein at least one of the catalysts contains barnite. 触媒の少なくとも１種が、更にアルカリ土類金属及び／又は亜鉛を含有する請求項１〜７のいずれか１項に記載の原油生成物。   The crude product according to any one of claims 1 to 7, wherein at least one of the catalysts further contains an alkaline earth metal and / or zinc. 請求項１〜８のいずれか１項に記載の原油生成物又は該原油生成物と原油とのブレンドを処理する工程を含む、輸送用燃料、加熱用燃料、潤滑剤又は化学薬品の製造方法。   A method for producing a transportation fuel, a heating fuel, a lubricant or a chemical, comprising a step of treating the crude product according to any one of claims 1 to 8 or a blend of the crude product and crude oil. 処理工程が原油生成物又はブレンドを１種以上の蒸留物フラクションに蒸留する工程を含む請求項９に記載の方法。   The method of claim 9, wherein the treating step comprises distilling the crude product or blend into one or more distillate fractions. 処理工程が水素化処理工程を含む請求項９又は１０に記載の方法。
The method according to claim 9 or 10, wherein the treatment step includes a hydrotreatment step.
JP2006545519A 2003-12-19 2004-12-16 System and method for producing crude product Pending JP2007514844A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US53150603P 2003-12-19 2003-12-19
US61879904P 2004-10-14 2004-10-14
PCT/US2004/042638 WO2005063932A2 (en) 2003-12-19 2004-12-16 Systems and methods of producing a crude product

Publications (2)

Publication Number Publication Date
JP2007514844A JP2007514844A (en) 2007-06-07
JP2007514844A5 true JP2007514844A5 (en) 2008-02-07

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JP2006545418A Pending JP2007514829A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545388A Pending JP2007516329A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545456A Pending JP2007514839A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545527A Pending JP2007516330A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545383A Expired - Fee Related JP4712723B2 (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545416A Pending JP2007518846A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545523A Expired - Fee Related JP4768631B2 (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545519A Pending JP2007514844A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545385A Pending JP2007514825A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545380A Pending JP2007514535A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545382A Pending JP2007514822A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545525A Pending JP2007514848A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545386A Pending JP2007517091A (en) 2003-12-19 2004-12-16 System and method for producing crude product

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JP2006545418A Pending JP2007514829A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545388A Pending JP2007516329A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545456A Pending JP2007514839A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545527A Pending JP2007516330A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545383A Expired - Fee Related JP4712723B2 (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545416A Pending JP2007518846A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545523A Expired - Fee Related JP4768631B2 (en) 2003-12-19 2004-12-16 System and method for producing crude product

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JP2006545385A Pending JP2007514825A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545380A Pending JP2007514535A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545382A Pending JP2007514822A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545525A Pending JP2007514848A (en) 2003-12-19 2004-12-16 System and method for producing crude product
JP2006545386A Pending JP2007517091A (en) 2003-12-19 2004-12-16 System and method for producing crude product

Country Status (13)

Country Link
EP (13) EP1704202A2 (en)
JP (13) JP2007514829A (en)
KR (7) KR20070055994A (en)
AU (7) AU2004308916B2 (en)
BR (13) BRPI0405585A (en)
CA (13) CA2559798C (en)
EA (4) EA009091B1 (en)
MX (10) MXPA06006743A (en)
NL (12) NL1027778C2 (en)
RU (6) RU2006126089A (en)
SG (2) SG149048A1 (en)
TW (7) TW200535232A (en)
WO (13) WO2005066309A2 (en)

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