公开(公告)号：US5976361A

公开(公告)日：1999-11-02

申请号：US910102

申请日：1997-08-13

申请人： Richard L. Hood ,  Phillip B. Rettger ,  Randall S. Goldstein ,  Lucien Y. Bronicki ,  Benjamin Doron ,  Joseph Sinai

发明人： Richard L. Hood ,  Phillip B. Rettger ,  Randall S. Goldstein ,  Lucien Y. Bronicki ,  Benjamin Doron ,  Joseph Sinai

IPC分类号： C10G55/04 ,  C10C3/00

CPC分类号： C10G55/04

摘要： 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.

摘要翻译： 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。

公开(公告)号：US06274032B1

公开(公告)日：2001-08-14

申请号：US09349493

申请日：1999-07-09

申请人： Richard L. Hood ,  Phillip B. Rettger ,  Randall S. Goldstein ,  Lucien Y. Bronicki

发明人： Richard L. Hood ,  Phillip B. Rettger ,  Randall S. Goldstein ,  Lucien Y. Bronicki

IPC分类号： C10G2100

摘要： A hydrocarbon source feed is upgraded using a solvent deasphalting (SDA) unit employing a solvent having a critical temperature Tc by initially separating from a first hydrocarbon input stream fractions with an atmospheric equivalent boiling temperature less than about Tf° F. for producing a stream of Tf−fractions and a residue stream (Tf+ stream), where Tf is greater than about Tc−50° 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.