首页> 外国专利> Increasing yield of diesel fuel from Fischer-Tropsch process - by hydrocracking and oligomerising prim. fractions

Increasing yield of diesel fuel from Fischer-Tropsch process - by hydrocracking and oligomerising prim. fractions

机译:通过加氢裂化和低聚底漆,可提高费-托工艺的柴油收率。分数

摘要

Mfr. of diesel fuel from coal (i) gasifies it with O2 and H2O; (ii) converts synthesis gas from (i) by the Fischer-Tropsch process; (iii) treats the primary prod. of (ii) separately by (iiia) and (iiib) to increase the yield of diesel fraction; (iiia) hydrocracks the fraction of b.pt. above 320 deg. C, pref. at 100-150 atmos. over a catalyst of noble metal supported on a Li or Ba zeolite, and pref. having first satd. the olefins in this fraction by H2 over a Ni-contg. catalyst at 100-150 atmos.; and (iiib) oligomerises the olefins of b.pt. below 140 deg. C, pref. treating the C3's and C4's separately, and hydrogenates the oligomerisate over a Ni-contg. catalyst. The yield of diesel fuel is increased to 61% of the Fischer- Tropsch prim. prods., and it is of good quality (cetane number 59). In contrast to coal hydrogenation methods, coals of high ash content may be used.
机译:制造商煤制得的柴油(i)用O2和H2O气化; (ii)通过费-托法将(i)的合成气转化; (iii)对待主要产品。 (ii)由(iiia)和(iiib)分别增加柴油馏分的收率; (iiia)加氢裂化b.pt.高于320度C,首选项在100-150 atmos。负载在锂或钡沸石上的贵金属催化剂上,并优选。第一次坐。在Ni-contg上通过H2分离该馏分中的烯烃。催化剂在100-150个大气压下; (iiib)使b.pt的烯烃低聚。低于140度C,首选项分别处理C3和C4,并在Ni-contg上氢化低聚物。催化剂。柴油的收率提高到了费托基础的61%。产品,并且质量好(十六号)。与煤氢化方法相反,可以使用高灰分含量的煤。

著录项

  • 公开/公告号DE3030998A1

    专利类型

  • 公开/公告日1982-04-01

    原文格式PDF

  • 申请/专利权人 METALLGESELLSCHAFT AG;

    申请/专利号DE19803030998

  • 发明设计人 GAENSSLENHANS;EISENLOHRK.H.DR.;

    申请日1980-08-16

  • 分类号C10G1/06;

  • 国家 DE

  • 入库时间 2022-08-22 12:42:43

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