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Insitu fluorination of catalyst beds - with control of fluorine proportion absorbed and temp. gradient (NL201076)

机译:催化剂床层的原位氟化-控制氟的吸收比例和温度。渐变(NL201076)

摘要

fluorination of catalysts in fixed beds with provision of a constant or variable fluorine displacement (SA= wt. % of added fluorine not absorbed by the bed), opt. in combination with a positive temp. gradient along the bed, in which (a) average value of SA is =10 wt.% (b) the opt. temp. gradient (G) is =30 degrees C., (c) the product of SA and G is =1000, (d) where SA is 40 wt.%, G is =300/SA, and (e) where SA is =40 but 50, G is =3/4 (50-SA). Used for activation of catalysts for catalytic conversion of hydrocarbon fractions at elevated temps. and pressures in presence of hydrogen. a more uniform distribution of fluorine through the catalyst is achieved, with ratio of F content at the end of the bed to that at the beginning of 0.5-1.5:1.
机译:固定床中催化剂的氟化反应,提供恒定或可变的氟取代度(SA =未被床吸收的添加氟的重量%),选择。结合正温度。 (a)SA平均值> = 10 wt。%(b)opt。温度梯度(G)= 30摄氏度,(c)SA与G的乘积= 1000,(d)其中SA为40 wt。%,G> == 300 / SA,和(e)其中SA为> = 40,但50,G> = 3/4(50-SA)。用于活化催化剂,以在高温下催化转化烃馏分。和氢气存在下的压力。氟在催化剂中的分布更加均匀,床尾的F含量与开始时的F含量之比为0.5-1.5:1。

著录项

  • 公开/公告号NL7514824A

    专利类型

  • 公开/公告日1977-06-21

    原文格式PDF

  • 申请/专利号NL19750014824

  • 发明设计人

    申请日1975-12-19

  • 分类号B01J37/26;C10G35/06;

  • 国家 NL

  • 入库时间 2022-08-23 00:49:24

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