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process and appears for the hydro treatment of a petroleum fraction liquid
process and appears for the hydro treatment of a petroleum fraction liquid
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机译:工艺,并出现在石油馏分液体的加氢处理中
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1511514 Catalyst bed arrangements SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ BV 7 May 1975 [9 May 1974] 19180/75 Heading C5E [Also in Division B1] In a process for hydro treating, e.g. at 455‹C and 175 atm, a liquid petroleum fraction, e.g. deasphalted Basrah oil, by passing it downwardly in the presence of hydrogen through a reactor containing spaced apart fixed catalyst beds and means for the supply of cold hydrogen-rich gas above each bed, at least one catalyst bed is covered with a lower layer of inert ceramic particles of 1-10 mm diameter, and an upper layer of inert ceramic particles of a 10mm diameter, the layers together occupying at most 20% of the height of catalyst bed covered thereby. The 10mm diameter particles may be Raschig rings or paddle-shaped. The beds may be vertically spaced with each bed covered by the particles, and the means for supplying cold hydrogen-rich gas may do so above each bed except the top one.
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机译:1511514催化剂床布置SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ BV 1975年5月7日[1974年5月9日] 19180/75税号C5E [也属于B1部门]在加氢处理过程中,例如:在455°C和175atm的温度下,石油馏分,例如脱沥青的巴士拉(Basrah)油,是在有氢气的情况下使它向下通过一个反应器,该反应器包含间隔开的固定催化剂床和在每个床上方提供冷富氢气体的装置,至少一个催化剂床覆盖有一层惰性下层直径为1-10毫米的陶瓷颗粒和直径大于10毫米的惰性陶瓷颗粒的上层,这些层在一起最多占被其覆盖的催化剂床层高度的20%。直径大于10mm的颗粒可以是Raschig环或桨形。这些床可以垂直间隔开,每个床都被颗粒覆盖,并且用于供应冷富氢气体的装置可以在除顶部床之外的每个床上方进行。
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