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    • 7. 发明授权
    • Delayed coking process
    • 延迟焦化工艺
    • US4302324A
    • 1981-11-24
    • US163835
    • 1980-06-27
    • Nai Y. ChenDennis E. Walsh
    • Nai Y. ChenDennis E. Walsh
    • C10B55/02C10G9/14
    • C10B55/02
    • A delayed coking process in which part of the coke produced is heated by partial burning and mixed with preheated coker feedstock to raise the temperature of the coking mass present in the coking drums. The rapid heat transfer thus obtained brings about some immediate flashing of volatiles and makes possible higher than usual temperatures in the coking drums. The results are a reduction of residence time in the drums and an increase in the yield of volatile products. Hot coke in excess of that required to heat the feed may be gasified. Thus, resultant net coke yields are lower than the conventional delayed coking process.
    • 延迟焦化方法,其中产生的焦炭的一部分通过部分燃烧加热并与预热的焦化器原料混合,以提高存在于焦化鼓中的焦化物质的温度。 如此获得的快速热传递导致挥发物的一些即时闪蒸,并且使得可能比焦化鼓中的通常温度高。 结果是减少了在鼓中的停留时间和挥发性产物的产率的增加。 超过加热进料所需热焦炭可能气化。 因此,得到的净焦炭产量低于常规的延迟焦化方法。
    • 9. 发明授权
    • Apparatus for FCC process with catalyst separation
    • FCC催化分离装置
    • US4971766A
    • 1990-11-20
    • US437064
    • 1989-11-16
    • Nai Y. ChenBilly K. HuhThomas E. Degnan
    • Nai Y. ChenBilly K. HuhThomas E. Degnan
    • C10G11/18
    • C10G11/18
    • An FCC or fluidized catalytic cracking process and apparatus for converting heavy metals laden crudes is disclosed. The heavy feed, conventional catalyst and an additive or vanadium getter contact the feed in a riser reactor. The additive is segregated from conventional FCC catalyst upstream of the conventional FCC regenerator. An elutriating, upflow riser reactor may be used with a coarse, rapidly settling getter. A fine, slowly settling getter may be used, with getter segregation achieved by using an elutriating cyclone on the riser outlet, an elutriating catalyst stripper, a sieve, or the like. The spent getter may be used once through, regenerated in a separate getter regenerator, or used as a source of fuel. Alumina and sponge coke are preferred getters.
    • 公开了一种FCC或流化催化裂化方法和用于转化重金属负载原油的装置。 重料,常规催化剂和添加剂或钒吸附剂在提升管反应器中接触进料。 该添加剂与常规FCC再生器上游的常规FCC催化剂分离。 淘汰式上升式提升管式反应器可与粗,快速沉降的吸气剂一起使用。 可以使用细的缓慢沉降的吸气剂,通过在提升管出口,淘洗催化剂汽提器,筛子等上使用淘洗旋风来实现吸气剂分离。 废吸气剂可以一次使用,在单独的吸气剂再生器中再生,或用作燃料来源。 氧化铝和海绵焦炭是优选的吸气剂。