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    • 27. 发明授权
    • Process for decoking a furnace for cracking a hydrocarbon feed
    • 用于对用于裂化烃进料的炉进行脱焦的方法
    • US07977524B2
    • 2011-07-12
    • US11953307
    • 2007-12-10
    • James N. McCoyRichard Charles Stell
    • James N. McCoyRichard Charles Stell
    • C07C4/00
    • C10G9/20C10G9/16
    • A process for decoking a convection section of a furnace for cracking a hydrocarbon feed, the furnace comprising a radiant section having burners that generate radiant heat and hot flue gas, and the convection section having at least one heat exchange tube for conveying the hydrocarbon feed. The process includes the step of establishing a flue gas temperature within the convection section of the furnace immediately adjacent the at least one convection section heat exchange tube so as to effect a film surface temperature of less than about 540° C. (about 1000° F.) within at least one convection section heat exchange tube, wherein said flue gas temperature establishing step is effective to decoke the at least one convection section heat exchange tube. A process for cracking hydrocarbon feed in a furnace is also provided.
    • 一种用于对用于裂化烃进料的炉的对流部分进行除焦的方法,该炉包括具有产生辐射热和热烟道气的燃烧器的辐射部分,以及具有用于输送烃进料的至少一个热交换管的对流部分。 该方法包括在紧邻至少一个对流段热交换管的炉子的对流段内建立烟气温度的步骤,以便实现小于约540℃的膜表面温度(约1000°F 在至少一个对流段热交换管内,其中所述烟道气温度建立步骤有效地剔除至少一个对流段热交换管。 还提供了一种用于在炉中裂化烃进料的方法。
    • 30. 发明授权
    • Process for upgrading tar
    • 升级tar的过程
    • US07744743B2
    • 2010-06-29
    • US11589453
    • 2006-10-30
    • James N. McCoyPaul F. KeusenkothenAlok Srivastava
    • James N. McCoyPaul F. KeusenkothenAlok Srivastava
    • C10G3/00C10G1/00
    • C10G55/04C10G21/003
    • A feedstream comprising tar is fed to a solvent deasphalter wherein it is contacted with a deasphalting solvent or fluid to produce a composition comprising a mixture or slurry of solvent containing a soluble portion of the tar, and a heavy tar fraction comprising the insoluble portion of the tar. These fractions may be separated in the deasphalter apparatus, such as by gravity settling wherein the heavy tar fraction is taken off as bottoms, and the solvent-soluble fraction taken as overflow or overheads with the solvent. The overflow or overheads is sent to a solvent recovery unit, such as a distillation apparatus, wherein solvent is recovered as overheads and a deasphalted tar fraction is taken off as a sidestream or bottoms. The solvent or a portion thereof, recovered as overheads, may be then be recycled to the solvent deasphalter, or in a preferred embodiment, at least a portion of the solvent is steam cracked to produce a product comprising light olefins.
    • 将包含焦油的进料流进料到溶剂脱沥青器中,其中其与脱沥青溶剂或流体接触以产生包含含有焦油的可溶部分的溶剂的混合物或浆料的组合物,以及包含不溶部分的重焦油馏分 柏油。 这些级分可以在脱沥青装置中分离,例如通过重力沉降,其中重焦油馏分作为塔底馏分取出,溶剂可溶部分用溶剂作为溢流或塔顶馏出物。 将溢出物或塔顶馏出物送入溶剂回收装置,例如蒸馏装置,其中将溶剂回收为塔顶馏出物,脱沥青焦油馏分作为侧流或塔底馏分脱除。 然后将作为塔顶馏出物回收的溶剂或其一部分再循环到溶剂脱沥青中,或者在一个优选的实施方案中,至少一部分溶剂被蒸汽裂化以产生包含轻质烯烃的产物。