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    • 3. 发明申请
    • PROCESS FOR OLEFIN PRODUCTION
    • 油脂生产工艺
    • WO2008131336A1
    • 2008-10-30
    • PCT/US2008/061020
    • 2008-04-21
    • EXXONMOBIL CHEMICAL PATENTS INC.MCCOY, James, N.ANNAMALAI, Subramanian
    • MCCOY, James, N.ANNAMALAI, Subramanian
    • C10G9/00C10G9/36C10G51/06
    • C10G9/00C10G2400/20
    • A system and process for processing a hydrocarbon feed to produce one or more olefins therefrom is provided. In at least one specific embodiment, the process includes a hydrocarbon feed that can be preheated to a temperature sufficient to selectively separate the hydrocarbon feed into a heavy cut stream and a light cut stream, wherein at least a portion of the preheating is provided by heat from either the heavy cut stream or the light cut stream. The heavy cut stream can be heated at conditions sufficient to provide a heated heavy cut stream having a vapor phase and a liquid phase. The vapor phase can be separated from the liquid phase to provide a vapor phase stream and a liquid phase stream. The vapor phase stream can then be thermally cracked to provide a first product stream comprising one or more olefins.
    • 提供了一种用于处理烃进料以从其生产一种或多种烯烃的系统和方法。 在至少一个具体实施方案中,该方法包括可以预热到足以选择性地将烃进料分离成重馏分流和轻馏分流的温度的烃进料,其中预热的至少一部分由热量 从重切割流或轻馏分流。 可以在足以提供具有气相和液相的加热重馏分流的条件下加热重馏分流。 气相可以与液相分离以提供气相流和液相流。 然后可以将气相物流热裂化以提供包含一种或多种烯烃的第一产物流。
    • 7. 发明申请
    • PROCESS FOR CRACKING A HEAVY HYDROCARBON FEEDSTREAM
    • 破碎重质烃生物反应器的方法
    • WO2010077461A1
    • 2010-07-08
    • PCT/US2009/064995
    • 2009-11-18
    • EXXONMOBIL CHEMICAL PATENTS INC.SPICER, David, B.ANNAMALAI, SubramanianFRYE, James, M.SCHERER, Caleb, M.
    • SPICER, David, B.ANNAMALAI, SubramanianFRYE, James, M.SCHERER, Caleb, M.
    • C10G9/16
    • C10G9/16
    • A process for cracking a hydrocarbon feedstream containing non-volatile components in a hydrocarbon cracking furnace having upper and lower convection heating sections within a flue of the furnace, a radiant heating section downstream of and connected to said lower convection heating section, a transfer line exchanger downstream of and connected to said radiant heating section, a furnace box containing furnace burners and said radiant heating section, and a vapor/liquid separator vessel connected between the upper and lower convection heating sections, the process comprising (a) passing said hydrocarbon feedstream into said upper convection section to heat said hydrocarbon feedstream to a first temperature sufficient to flash at least a portion of the hydrocarbons within said hydrocarbon feedstream into a vapor phase to form a vapor/liquid stream; (b) passing said vapor/liquid stream out of said upper convection section and into said vapor/liquid separator to separate said vapor/liquid stream into a hydrocarbon-containing vapor phase and a hydrocarbon-containing liquid phase within said vapor/liquid separator; (c) collecting said liquid phase into a bottoms liquid within said vapor/liquid separator; (d) passing said vapor phase into said radiant heating section and cracking hydrocarbons in said vapor phase to form an olefms-containing effluent stream; and (e) periodically injecting an air- steam mixture into said convection heating section, then through said vapor/liquid separator to incinerate coke formed and passing an incinerated coke residue/air-steam mixture so-formed between the furnace burners within the furnace box.
    • 一种在含有炉内烟道内的上下对流加热段的碳氢化合物裂解炉中裂化含有非挥发成分的烃类进料流的方法,在下方对流加热段下游并与之连接的辐射加热段, 在所述辐射加热部分的下游并连接到所述辐射加热部分,包含炉燃烧器和所述辐射加热部分的炉箱以及连接在上部和下部对流加热部分之间的蒸汽/液体分离器容器,所述方法包括(a)使所述烃进料流进入 所述上部对流部分将所述烃进料流加热至足以将所述烃进料流中的至少一部分烃闪蒸成气相以形成蒸汽/液体流的第一温度; (b)使所述蒸汽/液体流从所述上部对流部分流出并进入所述气/液分离器,以将所述气/液流分离成所述气/液分离器内的含烃气相和含烃液相; (c)将所述液相收集到所述蒸汽/液体分离器内的底部液体中; (d)使所述气相进入所述辐射加热段,并在所述气相中裂解烃,以形成含烯烃的流出物流; 并且(e)将空气 - 蒸汽混合物周期性地注入所述对流加热段,然后通过所述蒸汽/液体分离器焚烧形成的焦炭并通过在炉箱内的炉燃烧器之间形成的焚烧焦炭残渣/空气 - 蒸汽混合物 。