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U.S. Department of Energy
Office of Scientific and Technical Information

Process for increasing deasphalted oil production from upgraded residua

Patent ·
OSTI ID:6442335
This patent describes a process for increasing the production of deasphalted oil from a hydrocarbon feedstock comprising the steps of: (a) passing the hydrocarbon feedstock into a first distillation zone where the feedstock is separated into distillates and a first residuum; (b) passing the first residuum into a hydrotreating zone operating between about 315C to 425C, at an absolute pressure between 4000 to 10,000 cmHg where a hydrotreated first residuum is produced; (c) passing the hydrotreated first residuum into a second distillation zone where it is separated into distillates and a hydrotreated distillation residuum; and (d) mixing the hydrotreated distillation residuum with a solubilizing aid selected from the group consisting of catalytic cracker fractionator bottoms having an initial boiling point not less than 260C and not more than 430C (at 1 atmosphere), heavy cycle gas oil having a boiling point range of 200C to 420C (at 1 atmosphere) and heavy coker gas oil having a boiling point range of 300C to 550C (at 1 atmosphere) and feeding the resultant mixture into a deasphalting zone where the solubilizing aid comprises 30 to 60 LV% of the total feed to the deasphalting zone. The hydrotreated distillation residuum and solubilizing aid are contacted with a deasphalting solvent producing a liquid deasphalted oil extract and an asphaltic raffinate. The solubilizing aid inhibits the formation of a third asphaltic phase by promoting the solubility of the third phase in the asphaltic raffinate.
Assignee:
Exxon Research and Engineering Co., Florham Park, NJ
Patent Number(s):
US 4673485
OSTI ID:
6442335
Country of Publication:
United States
Language:
English