The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Oct. 23, 1984

Filed:

Feb. 22, 1983
Applicant:
Inventor:

Partha S Ganguli, Lawrenceville, NJ (US);

Assignee:

HRI, Inc., Gibbsboro, NJ (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G / ;
U.S. Cl.
CPC ...
208 59 ; 208 96 ; 208102 ;
Abstract

A process for high hydroconversion of heavy hydrocarbon liquid feedstocks such as petroleum residua containing at least about 50 V % material boiling above 975.degree. F. to produce lower boiling hydrocarbon liquid and gas products, wherein heavy RCR materials and metals compounds are removed in-situ from the reactor effluent liquid by solvent vapor extraction using a process-derived solvent vapor at supercritical conditions. In the process, the feedstock is catalytically hydroconverted at 780.degree.-860.degree. F. temperature, and the resulting liquid fraction is contacted with a process-derived solvent vapor fraction having a normal boiling range of 250.degree.-400.degree. F. and heated to supercritical temperature to dissolve and extract substantially all the hydrocarbon liquid fractions, and separate heavy RCR materials and the metals compounds contained therein. The resulting supercritical solvent vapor with dissolved liquid fraction is pressure-reduced and distilled to recover the needed solvent fraction and to provide a hydrocarbon liquid fraction product. The hydrogenation step preferably uses an ebullated catalytic bed. Also, if desired, the supercritical solvent vapor extraction step can be used intermediate two hydroconversion reaction zones connected in series to produce additional desired lower boiling desulfurized hydrocarbon liquid fraction products.


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