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    • 23. 发明申请
    • Supercritical Water Processing of Extra Heavy Crude in a Slurry-Phase Up-Flow Reactor System
    • 超临界水处理超临界水泥浆相上升反应堆系统
    • US20070289898A1
    • 2007-12-20
    • US11424196
    • 2006-06-14
    • Dwijen K. Banerjee
    • Dwijen K. Banerjee
    • C10G31/00
    • C10G11/20C10G11/16
    • A system and method for upgrading heavy crude oil. The system comprises: a system for blending a catalyst with the heavy crude to produce a crude/catalyst slurry, a source of supercritical water, a system for blending the supercritical water with the crude/catalyst slurry, infecting the feed slurry into the bottom of an tip-flow reactor, carrying out a reaction between the water and the crude to produce treated hydrocarbons, and separating the treated hydrocarbons into a heavy stream and a light stream. The first separator is in fluid communication with the tipper half of the reactor. A second separator receives the light stream and separates it into gases, liquid hydrocarbons, and water. A system and method of generating hydrogen for the process through in situ shift reaction, generating carbon monoxide either in situ through the injection of air inside the reactor or externally by gasification of unreacted resid or produced gases.
    • 一种重质原油升级的制度和方法。 该系统包括:用于将催化剂与重质原油混合以产生粗/催化剂浆料的系统,超临界水源,用于将超临界水与粗/催化剂浆料混合的系统,将进料浆料感染到 尖端流动反应器,在水和粗产物之间进行反应以产生经处理的烃,并将经处理的烃分离成重流和轻质流。 第一分离器与反应器的自卸车一半流体连通。 第二分离器接收轻质流并将其分离成气体,液体烃和水。 通过原位转移反应产生氢气的系统和方法,通过在反应器内注入空气或通过未反应的残留物或产生的气体的气化在外部产生一氧化碳。
    • 24. 发明授权
    • Combined thermal and catalytic treatment of heavy petroleum in a slurry phase counterflow reactor
    • 在淤浆相逆流反应器中对重石油进行联合热处理和催化处理
    • US06755962B2
    • 2004-06-29
    • US09852107
    • 2001-05-09
    • Dwijen K. Banerjee
    • Dwijen K. Banerjee
    • C10G4700
    • C10G65/10B01J8/0035B01J8/22B01J8/228B01J2208/00256B01J2208/00274B01J2208/00283B01J2208/00539B01J2208/0061B01J2208/0084C10G47/22
    • A slurry phase reactor is designed to treat extra heavy petroleum crude in a combination of thermal-zone and catalytic-zone in a counterflow system where liquid feed is added to the top and hydrogen at the bottom. Feed enters the gas-phase thermal zone, where it passes to a liquid-phase thermal zone. In the liquid-phase thermal zone, the hydrocarbon is thermally cracked and the unreacted liquid is further passed to a catalytic-zone below in communication with the thermal-zone. Catalyst can be added or removed as required in a continuous mode without shutting down the system. The heat generated inside the catalytic cracking zone is distributed to the entire reactor as the gaseous product flows upward. Feed is brought to the reaction conditions by the heat recovered from the gas-phase zone. Reaction temperature could be controlled by feed temperature.
    • 浆料相反应器被设计成在反向流动系统中处理热区域和催化区域的组合中的额外重质石油原油,其中液体进料添加到顶部,底部加氢。 进料进入气相热区,在那里它进入液相热区。 在液相热区中,烃被热裂化,并且未反应的液体进一步传递到与热区连通的下游催化区。 可以根据需要在连续模式下添加或除去催化剂,而无需关闭系统。 当气体产物向上流动时,催化裂化区内产生的热分布到整个反应器中。 通过从气相区回收的热量将进料送入反应条件。 反应温度可以通过进料温度控制。