首页> 外国专利> Hydrocracking of carbonaceous feeds with molten salt catalyst - using molten metal halide as continuous liq. phase

Hydrocracking of carbonaceous feeds with molten salt catalyst - using molten metal halide as continuous liq. phase

机译:用熔融盐催化剂对含碳原料进行加氢裂化-使用熔融金属卤化物作为连续液体。相

摘要

Hydrocracking of carbonaceous feeds (e.g. petroleum residua, tar, coal, coal liqs., tar-sand oil or shale oil) is carried out by contacting the feed with H2 at elevated temp. and pressure in the presence of a molten metal halide (I) forming a continuous liq. phase, where (I) is SbCl3, SbBr3, SbI3, AsBr3, AsI3, BiCl3, BiBr3, GaBr3, HgBr2, HgI2, SnBr2 and/or TiI3. The (I)/feed wt. ratio is pref. more than 3. The process is pref. carried out at 200-550 (esp. 275-400) deg. C and an H2 partial pressure of at least 17.2 (esp. at least 55) bar. The reaction can be promoted by an inorganic acid which is stable under the reaction conditions, esp. a hydrohalic acid, pyrophosphoric acid or H2SO4. The process gives high yields of gasoline-range hydrocarbons.
机译:含碳进料(例如石油渣油,焦油,煤,煤液,焦油砂油或页岩油)的加氢裂化是通过使进料与H2在高温下接触来进行的。在熔融金属卤化物(I)存在下形成连续液体的压力和压力。相,其中(I)为SbCl 3,SbBr 3,SbI 3,AsBr 3,AsI 3,BiCl 3,BiBr 3,GaBr 3,HgBr 2,HgI 2,SnBr 2和/或TiI 3。 (I)/进料重量比例是优选的。大于3。该过程是优选的。在200-550度(尤其是275-400度)进行C和H2分压至少为17.2(特别是至少55)巴。可以通过在反应条件下稳定的无机酸促进反应,特别是在反应条件下。氢卤酸,焦磷酸或硫酸。该方法可产生高产率的汽油范围的烃。

著录项

  • 公开/公告号NL8103650A

    专利类型

  • 公开/公告日1981-12-01

    原文格式PDF

  • 申请/专利号NL19810003650

  • 发明设计人

    申请日1981-08-03

  • 分类号C10G47/08;B01J27/08;B01J35/12;

  • 国家 NL

  • 入库时间 2022-08-22 13:42:25

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