Residue hydrocracking processing
A technology for hydrocracking and residual oil hydrogenation, applied in the field of residual oil and other heavy hydrocarbon fraction hydrocracking, can solve the problems of being limited to about 35% to 40%, limited conversion rate, etc.
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[0047] In the following example, a 40k BPSD Arabian heavy vacuum residue was first processed in the SDA unit at 73 vol% lift. The properties of the resulting DAO and SDA pitches are summarized in Table 1. The DAO contained 4.27wt% sulfur, 10wt% CCR and 47wppm Ni+V and was then processed in an RDS unit to reduce the sulfur content of the feed by 85 to 87wt%. At the same time the resid fraction in the feed was converted by 35 to 45%. In this example, the RDS effluent was then hydrocracked in a single ebullating bed reactor that was closely coupled to the RDS reactor, increasing the overall conversion to 85 vol% and increasing the overall HDS to 91.8 wt%. The resulting unconverted oil (UCO) was estimated to have a sulfur content and API degree of approximately 1.0 wt% and 11.9°, respectively. It is envisaged that the UCO from this reaction system will meet the low sulfur fuel oil specification without adding any additional cutterstock. The overall space velocity required to a...
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