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公开(公告)号:US09845435B2
公开(公告)日:2017-12-19
申请号:US14387608
申请日:2013-03-27
申请人: Japan Oil, Gas and Metals National Corporation , Inpex Corporation , JX Nippon Oil & Energy Corporation , Japan Petroleum Exploration Co., Ltd. , Cosmo Oil Co., Ltd. , Nippon Steel & Sumikin Engineering Co., Ltd.
发明人: Takuya Niitsuma , Marie Iwama
IPC分类号: C10G67/00 , C10L1/06 , C10L10/16 , C10L10/14 , C10G65/14 , C10L1/08 , C10G45/58 , C10G47/00 , C10G2/00
CPC分类号: C10G67/00 , C10G2/30 , C10G45/58 , C10G47/00 , C10G65/14 , C10G2300/1022 , C10G2300/4081 , C10L1/06 , C10L1/08 , C10L10/14 , C10L10/16 , C10L2200/0492 , C10L2270/026 , C10L2290/10
摘要: Provided is a hydrotreating step (A) containing a hydroisomerization step (A1) that obtains a hydroisomerized oil (a1) by bringing a FT synthesis oil into contact with a hydroisomerization catalyst and/or a hydrocracking step (A2) that obtains a hydrocracked oil (a2) by bringing it into contact with a hydrocracking catalyst, and a fractionation step (B) that transfers at least a portion of the hydrotreated oil (a) composed of the hydroisomerized oil (a1) and/or the hydrocracked oil (a2) to a fractionator and, at the very least, obtains a middle distillate (b1) with a 5% distillation point of 130 to 170° C. and a 95% distillation point of 240 to 300° C., and a heavy oil (b2) that is heavier than the middle distillate (b1).
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2.
公开(公告)号:US20150065761A1
公开(公告)日:2015-03-05
申请号:US14387608
申请日:2013-03-27
申请人: Japan Oil, Gas and Metals National Corporation , Inpex Corporation , JX Nippon Oil & Energy Corporation , Japan Petroleum Exploration Co., Ltd. , Cosmo Oil Co., Ltd. , Nippon Steel & Sumikin Engineering Co., Ltd.
发明人: Takuya Niitsuma , Marie Iwama
CPC分类号: C10G67/00 , C10G2/30 , C10G45/58 , C10G47/00 , C10G65/14 , C10G2300/1022 , C10G2300/4081 , C10L1/06 , C10L1/08 , C10L10/14 , C10L10/16 , C10L2200/0492 , C10L2270/026 , C10L2290/10
摘要: Provided is a hydrotreating step (A) containing a hydroisomerization step (A1) that obtains a hydroisomerized oil (a1) by bringing a FT synthesis oil into contact with a hydroisomerization catalyst and/or a hydrocracking step (A2) that obtains a hydrocracked oil (a2) by bringing it into contact with a hydrocracking catalyst, and a fractionation step (B) that transfers at least a portion of the hydrotreated oil (a) composed of the hydroisomerized oil (a1) and/or the hydrocracked oil (a2) to a fractionator and, at the very least, obtains a middle distillate (b1) with a 5% distillation point of 130 to 170° C. and a 95% distillation point of 240 to 300° C., and a heavy oil (b2) that is heavier than the middle distillate (b1).
摘要翻译: 本发明提供含有通过使FT合成油与加氢异构化催化剂和/或获得加氢裂化油的加氢裂化工序(A2)接触而得到加氢异构化油(a1)的加氢精制工序(A1)的加氢处理工序(A) a2),将加氢裂化催化剂与加氢异构化油(a1)和/或加氢裂化油(a2)组成的加氢处理油(a)的至少一部分转移至 并且至少得到具有130至170℃的5%蒸馏点和240至300℃的95%蒸馏点的中间馏分(b1)和重油(b2) 比中间馏分(b1)重。
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公开(公告)号:US20150052803A1
公开(公告)日:2015-02-26
申请号:US14389597
申请日:2013-02-20
发明人: Takuya Niitsuma , Marie Iwama , Kazuya Nasuno , Tsukasa Kousaka
CPC分类号: C10L10/16 , C10G2300/1022 , C10G2300/202 , C10G2300/302 , C10G2400/30 , C10L1/04 , C10L1/1963 , C10L2200/04 , C10L2200/0492 , C10L2270/026
摘要: To provide a gas oil composition providing superior low temperature performance as compared with the conventional techniques.The gas oil composition, wherein a sulfur content is 1 ppm by mass or less, an aromatic content is 1% by mass or less, a C5-C15 paraffin content is 30% to 85% by mass, a C20-C27 paraffin content is 3% to 20% by mass, and a isoparaffin content is 50% to 75% by mass, contains a cold flow improver at 20 ppm to 1000 ppm by mass.
摘要翻译: 提供与常规技术相比提供优异的低温性能的瓦斯油组合物。 其中,硫含量为1质量%以下,所述芳烃含量为1质量%以下,所述C5〜C15烷烃含量为30〜85质量%,所述C 20〜C 27烷烃含量为 3质量%〜20质量%,异链烷烃含量为50〜75质量%,含有20质量%〜1000质量ppm的冷流动改进剂。
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4.
公开(公告)号:US09434902B2
公开(公告)日:2016-09-06
申请号:US14389473
申请日:2013-01-15
发明人: Takuya Niitsuma , Marie Iwama
CPC分类号: C10L10/16 , C10G2300/1022 , C10G2300/304 , C10G2300/308 , C10G2400/08 , C10L1/04 , C10L1/08 , C10L2200/0453 , C10L2200/0492 , C10L2270/04 , C10L2290/24
摘要: An object is to provide a method for producing a jet fuel composition capable of producing a jet fuel composition with excellent quality at a high yield even when a jet fuel blendstock derived from an FT synthesis oil is used, and a jet fuel composition produced by the production method. It is characterized by including a step of mixing a certain Fischer Tropsch (FT) synthesis jet fuel blendstock with a certain petroleum based jet fuel blendstock so that the ratio of the FT synthesis jet fuel blendstock in the composition ranges from 20 to 80% by volume.
摘要翻译: 本发明的目的是提供一种制造喷气燃料组合物的方法,该喷气燃料组合物能够以高产率生产具有优良品质的喷气燃料组合物,即使使用衍生自FT合成油的喷气燃料共混料,以及由 生产方式。 其特征在于包括将某些费 - 托(FT)合成喷气燃料混合物料料与某种基于石油的喷气燃料混合原料混合的步骤,使得组合物中FT合成喷气燃料共混料料的比例为20至80体积% 。
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5.
公开(公告)号:US20150090632A1
公开(公告)日:2015-04-02
申请号:US14389473
申请日:2013-01-15
发明人: Takuya Niitsuma , Marie Iwama
CPC分类号: C10L10/16 , C10G2300/1022 , C10G2300/304 , C10G2300/308 , C10G2400/08 , C10L1/04 , C10L1/08 , C10L2200/0453 , C10L2200/0492 , C10L2270/04 , C10L2290/24
摘要: An object is to provide a method for producing a jet fuel composition capable of producing a jet fuel composition with excellent quality at a high yield even when a jet fuel blendstock derived from an FT synthesis oil is used, and a jet fuel composition produced by the production method. It is characterized by including a step of mixing a certain Fischer Tropsch (FT) synthesis jet fuel blendstock with a certain petroleum based jet fuel blendstock so that the ratio of the FT synthesis jet fuel blendstock in the composition ranges from 20 to 80% by volume.
摘要翻译: 本发明的目的是提供一种制造喷气燃料组合物的方法,该喷气燃料组合物能够以高产率生产具有优良品质的喷气燃料组合物,即使使用衍生自FT合成油的喷气燃料共混料,以及由 生产方式。 其特征在于包括将某些费 - 托(FT)合成喷气燃料混合物料料与某种基于石油的喷气燃料混合原料混合的步骤,使得组合物中FT合成喷气燃料共混料料的比例为20至80体积% 。
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公开(公告)号:US09399745B2
公开(公告)日:2016-07-26
申请号:US14389473
申请日:2013-01-15
发明人: Takuya Niitsuma , Marie Iwama
摘要: An object is to provide a method for producing a jet fuel composition capable of producing a jet fuel composition with excellent quality at a high yield even when a jet fuel blendstock derived from an FT synthesis oil is used, and a jet fuel composition produced by the production method. It is characterized by including a step of mixing a certain Fischer Tropsch (FT) synthesis jet fuel blendstock with a certain petroleum based jet fuel blendstock so that the ratio of the FT synthesis jet fuel blendstock in the composition ranges from 20 to 80% by volume.
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