发明名称 PROCEDEU DE REFORMARE CATALITICA A HIDROCARBURILOR
摘要 <p>* * * * MULTIPLE-STAGE HYDROCARBON CONVERSION WITH GRAVITY-FLOWING CATALYST PARTICLES A multiple-stage catalytic conversion system in which a hydrocarbonaceous charge stock and hydrogen flow serially through a plurality of catalytic reaction zones in each of which the catalyst particles are movable via gravity-flow. The flow of the product effluent from at least one reaction zone is restricted. This technique increases the pressure drop within the entire reactor circuit, and serves to alleviate the problems associated with the occurrence of stagnant catalyst areas within the reaction zone which are unable to assume a downward gravityflow pattern. Flow restriction may be effected either before, or after the inter-reaction zone heaters, preferably before.</p>
申请公布号 RO75624(A) 申请公布日期 1981.01.30
申请号 RO19780094014 申请日期 1978.05.09
申请人 UOP INC,US 发明人 PETERS,KENETH D.,US;VEINERMAN,ELLIOT,US;FELCH,DONAL E.,US
分类号 B01J8/12;C10G35/12;C10G49/14;C10G59/02;C10G65/04;C10G65/12 主分类号 B01J8/12
代理机构 代理人
主权项
地址