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US 4,762,543 AGranted
Carbon dioxide recovery
AssigneeAmoco Corporation
InventorsLeroy A. Pantermuehl, Thomas E. Krisa
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Abstract
A novel gas processing method is disclosed which is useful in separating and recovering carbon dioxide from gas streams having a high carbon dioxide content (e.g., 85-95 mol percent) and a low hydrocarbon/nitrogen content. The method is particularly useful in processing gas streams produced during carbon dioxide flooding operations for enhanced oil recovery.
Claims2
A gas processing method for separating and recovering carbon dioxide from a pressurized gaseous feed stream comprising methane and/or nitrogen and at least about 85 mol percent carbon dioxide, said method comprising:
- (a) cooling said feed stream to a temperature effective to cause at least a portion of the carbon dioxide in said feed stream to condense to a liquid;
- (b) introducing the cooled, pressurized feed stream from step (a) into a separator vessel wherein said stream is separated into a first liquid bottom fraction (consisting essentially of carbon dioxide) and a first vapor fraction (comprising methane and/or nitrogen and carbon dioxide);
- (c) recovering said first liquid bottom fraction;
- (d) taking said first vapor fraction as a first overhead gas stream from said separator vessel and conveying said first overhead gas stream to a stripper tower and introducing said overhead gas stream into the bottom portion of said stripper tower;
- (e) passing said first overhead gas stream upwardly through said stripper tower under conditions effective to separate said stream into a second liquid bottom fraction (consisting essentially of carbon dioxide) and a second vapor fraction (comprising methane and/or nitrogen and carbon dioxide);
- (f) recovering said second liquid fraction;
- (g) taking said second vapor fraction as a second overhead gas stream from said stripper tower;
- (h) cooling said second vapor fraction to a temperature effective to cause at least a portion of the carbon dioxide in said second vapor fraction to condense to a liquid;
- and
- (i) introducing the cooled second vapor fraction from (h) into a reflux accumulator vessel wherein said cooled vapor fraction is separated into (a) a third liquid bottom fraction (consisting essentially of carbon dioxide) which is recovered and reintroduced into the top portion of said stripper tower;
- and (b) a third vapor fraction (comprising methane and/or nitrogen and carbon dioxide) which is discharged or recovered.
8 more elements
Dependencies are inferred from the claim text.