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    • 5. 发明授权
    • Method of and means for upgrading hydrocarbons containing metals and
asphaltenes
    • 用于升级含有金属和沥青质的烃的方法和方法
    • US5976361A
    • 1999-11-02
    • US910102
    • 1997-08-13
    • Richard L. HoodPhillip B. RettgerRandall S. GoldsteinLucien Y. BronickiBenjamin DoronJoseph Sinai
    • Richard L. HoodPhillip B. RettgerRandall S. GoldsteinLucien Y. BronickiBenjamin DoronJoseph Sinai
    • C10G55/04C10C3/00
    • C10G55/04
    • A hydrocarbon source feed is upgraded using a solvent deasphalting (SDA) unit employing a solvent having a critical temperature T.sub.c by initially separating from a first hydrocarbon input stream fractions with an atmospheric equivalent boiling temperature less than about T.sub.f .degree. F. for producing a stream of T.sub.f.sup.- fractions and a residue stream (T.sub.f.sup.+ stream), where T.sub.f is greater than about T.sub.c -50.degree. F. In the SDA unit, a second hydrocarbon input stream which includes the residue stream is deasphalted for producing a first product stream of substantially solvent-free asphaltenes, and a second product stream containing substantially solvent-free deasphalted oil (DAO). The source feed may be included in either the first or second input streams. The DAO in the second product stream is thermally cracked for producing an output stream that includes thermally cracked fractions and by-product asphaltenes produced by thermally cracking the DAO. Finally, at least some the said thermally cracked fractions are included in the first input stream.
    • 使用具有临界温度Tc的溶剂的溶剂脱沥青(SDA)单元将烃源进料升级,首先从大气当量沸点低于约Tf F F的第一烃输入流馏分分离,以产生 Tf-级分和残余物流(Tf +流),其中Tf大于约Tc-50°F。在SDA单元中,包含残余物流的第二烃输入流被脱沥青以产生基本溶剂的第一产物流 - 无沥青质和含有基本上无溶剂的脱沥青油(DAO)的第二产物流。 源馈送可以包括在第一或第二输入流中。 第二产物流中的DAO被热裂化以产生包含热裂解馏分和通过热裂化DAO产生的副产物沥青质的输出流。 最后,至少一些所述热裂解馏分包括在第一输入流中。
    • 7. 发明授权
    • Solvent deasphalting unit capable of generating power
    • 能发电的溶剂脱沥青装置
    • US5843302A
    • 1998-12-01
    • US764264
    • 1996-12-12
    • Richard L. Hood
    • Richard L. Hood
    • C10C3/08C10G21/00C10C3/00B01D11/00
    • C10G21/003C10C3/08
    • Solvent deasphalting apparatus includes a separator that receives two inputs, a heavy hydrocarbon feed and a solvent feed; and the apparatus produces two outputs, an asphaltene/solvent stream and a deasphalted oil/solvent stream. A solvent recovery unit of the apparatus receives the two output streams and produces mainly a substantially solvent-free deasphalted oil product stream, a substantially solvent-free asphaltene product stream, and a recovered solvent stream which is returned to a solvent drum. A pump pumps a substantially constant volume of solvent from the solvent drum into a by-pass line connecting the pump to the solvent drum, and into a connection line connecting the pump to the separator. The amount of solvent flow in the connection line is functionally related to the level of heavy hydrocarbon feed so that solvent in excess of that flowing into the connection line and spills back to the solvent drum through the by-pass line. Finally, a power generator generates power in response to the flow of solvent in the by-pass line. The power generator includes a vaporizer for vaporizing solvent in the by-pass line, an organic vapor turbine responsive to vaporized solvent for expanding the vaporized solvent and producing expanded vaporized solvent, and generating power, a condenser for condensing the expanded vaporized solvent and producing condensed solvent, and a pump for returning the condensed solvent to the drum.
    • 溶剂脱沥青装置包括接收两个输入的分离器,重质烃进料和溶剂进料; 并且该装置产生两个输出,沥青质/溶剂流和脱沥青油/溶剂流。 该设备的溶剂回收单元接收两个输出流并主要产生基本上无溶剂的脱沥青油产物流,基本上无溶剂的沥青质产物流和回流的溶剂流,该溶剂流返回到溶剂鼓中。 泵将基本上恒定体积的溶剂从溶剂鼓泵送到将泵连接到溶剂桶的旁路管线中,并将泵连接到分离器的连接线中。 连接线中的溶剂流量在功能上与重质烃进料的水平相关,使得超过流入连接管线的溶剂超过通过旁路管线溢出回溶剂鼓。 最后,发电机响应于旁路线路中的溶剂流而发电。 发电机包括用于蒸发旁路管线中的溶剂的汽化器,响应蒸发溶剂的有机汽轮机,用于膨胀蒸发的溶剂并产生膨胀的汽化溶剂和发电;冷凝器,用于冷凝膨胀的汽化溶剂并产生冷凝 溶剂和用于使冷凝的溶剂返回到滚筒的泵。