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