发明名称 |
DIESEL FUEL OR DIESEL FUEL BASE STOCK AND PRODUCTION METHOD THEREOF |
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). |
申请公布号 |
US2015065761(A1) |
申请公布日期 |
2015.03.05 |
申请号 |
US201314387608 |
申请日期 |
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 |
Niitsuma Takuya;Iwama Marie |
分类号 |
C10G67/00;C10L10/14;C10L10/16;C10L1/06 |
主分类号 |
C10G67/00 |
代理机构 |
|
代理人 |
|
主权项 |
1. A production method for a diesel fuel or a diesel fuel base stock, comprising:
a hydrotreating step (A) containing a hydroisomerization step (A1) of obtaining a hydroisomerized oil (a1) by bringing a FT synthesis oil obtained by Fischer-Tropsch synthesis reaction, which contains a middle distillate and/or a wax fraction that is heavier than the middle distillate, into contact with a hydroisomerization catalyst, and/or a hydrocracking step (A2) of obtaining a hydrocracked oil (a2) by bringing it into contact with a hydrocracking catalyst; and a fractionation step (B) of transferring at least a portion of a hydrotreated oil (a) composed of the hydroisomerized oil (a1) and/or the hydrocracked oil (a2) to a fractionator and, at the very least, obtaining 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), wherein by adjusting the hydrotreating conditions in the hydrotreating step (A) and/or the fractionation conditions in the fractionation step (B), the middle distillate (b1), in which the flash point is 30 to 40° C., and the proportion of branched paraffins accounts for 60 mass % or more of the entire amount of paraffins, is obtained as a diesel fuel or a diesel fuel base stock. |
地址 |
Tokyo JP |