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US 10,703,994 B2Granted
Process and apparatus for two-stage deasphalting
AssigneeUop LLC
InventorsJagannathan Govindhakannan, Hans G. Lefebvre
Life of this patent
Estimating the term…
Abstract
Solvent deasphalting (SDA) in series is used to extract deasphalted oil from heavier hydrocarbons in series. Instead of stripping the pitch material of solvent in the second stage which can stick in the pitch stripper and inhibit flow, a dryer is used to vaporize solvent for recycle to the second SDA unit and produce pitch solids.
Claims19
A process for extracting lighter hydrocarbons from heavier hydrocarbons comprising:
- deasphalting a heavy hydrocarbon feed stream with a solvent to extract a deasphalted oil stream containing a greater concentration of aliphatic compounds than in the feed stream and provide a pitch stream containing a greater concentration of aromatic compounds than in the feed stream;
- and
- heating the pitch stream in a horizontally elongated vessel to drive off a heated solvent stream from the pitch stream, said elongated vessel is a paddle dryer or a rotary kiln.
An apparatus for solvent deasphalting comprising:
- a first extraction column having a first heavy feed inlet and a first solvent inlet, a first deasphalted oil line extending from an overhead of the first extraction column and a first extraction line extending from a bottom of said first extraction column;
- a second extraction column having a second solvent inlet and a first asphalted feed inlet in downstream communication with a first pitch line and a second deasphalted oil line extending from an overhead of the second extraction column and a second extraction line extending from a bottom of the second extraction column;
- and
- a dryer in downstream communication with a second pitch line at an inlet end and having a solids outlet at an opposite end and a heated solvent outlet extending from a top of the dryer.
1 more element
A process for extracting lighter hydrocarbons from heavier hydrocarbons comprising:
- deasphalting a heavy hydrocarbon feed stream with a first solvent to extract a first deasphalted oil stream containing a greater concentration of aliphatic compounds than in the feed stream and provide a first pitch stream containing a greater concentration of aromatic compounds than in the feed stream;
- stripping said first pitch stream with an inert gas to separate a first solvent recovery stream from said first pitch stream to provide a first solvent-lean pitch stream;
- deasphalting said first solvent-lean pitch stream with a second solvent to extract a second deasphalted oil stream containing a greater concentration of aliphatic compounds than in the first solvent-lean pitch stream and provide a second pitch stream containing a greater concentration of aromatic compounds than in the stripped first pitch stream;
- heating the second pitch stream to drive off a heated second solvent stream from the second pitch product;
- and
- separating said second deasphalted oil stream into a second separated solvent stream and a second separated deasphalted oil stream.
3 more elements
Dependencies are inferred from the claim text.