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    • 51. 发明授权
    • Catalytic reforming process
    • 催化重整过程
    • US4415435A
    • 1983-11-15
    • US422675
    • 1982-09-24
    • William E. Lewis
    • William E. Lewis
    • C10G35/09C10G69/08C10G35/06
    • C10G35/09C10G69/08
    • A process for the optomization of the amount of sulfur introduced into a cyclic, or semi-cyclic reforming unit consistant with the dual objective of sulfiding a sulfur-sensitive polymetallic platinum catalyst, and minimizing the average sulfur present in the unit during an operating cycle. In accordance with such process, a sulfur-containing naphtha feed between reactor swings is first hydrofined to reduce the sulfur content of the feed, the product therefrom is then passed through a guard bed or reactor and contacted with a sulfur adsorbent essentially completely remove the feed sulfur to maximize catalyst activity, catalyst stability and C.sub.5.sup.+ liquid yield. At the time of, or just prior to, swinging on-stream a reactor which contains an unsulfided fresh, or unsulfided regenerated, reactivated sulfur-sensitive polymetallic platinum catalyst, the series of reactors is by-passed around the hydrofiner and guard chamber and the product from the hydrofiner fed directly into the series of reactors to sulfide the catalyst.
    • 用于将引入到环状或半循环重整单元中的硫的量的光学化的方法与硫敏感多金属铂催化剂的双重目标相一致,并且在操作循环期间使存在于该单元中的平均硫最小化。 根据这种方法,首先将反应器摆动之间的含硫石脑油进料加热,以减少进料的硫含量,然后使其产物通过保护床或反应器并与硫吸附剂接触,基本上完全除去进料 硫以最大化催化剂活性,催化剂稳定性和C5 +液体产率。 在或者在之前或之前摆放包含未硫化的新鲜或未硫化的再生的再生的硫敏感多金属铂催化剂的反应器的时候,该系列反应器绕过氢化提炼机和保护室,并且 来自加氢精制剂的产物直接进料到反应器系列中以硫化催化剂。