Process for purification of synthesis gas
AssigneeShell Oil Company
InventorDaniel C. Baker
Life of this patent
Estimating the term…
Abstract
A process for the treatment of a gas stream derived from the gasification of coal is described, the process being characterized, in one embodimment, by stripping of the wash and cooling liquid used to cool and remove NH.sub.3 from the synthesis gas prior to reuse of the liquid in removal of residual solids from the product gas stream, thereby avoiding incompatibilities which may initiate or aggravate chemical precipitation, particularly that of CaCO.sub.3.
Claims3
A process for the purification of a synthesis gas stream containing CO.sub.2 and minor amounts of NH.sub.3 and HCN, and from which the bulk of the flyslag has been removed but which contains residual flyslag particles, comprising
- (a) passing said synthesis gas stream to a solids scrubbing zone and scrubbing said gas stream with an effective amount of an aqueous scrubbing solution and removing residual flyslag particles from said stream, producing a substantially solids-free synthesis gas stream containing HCN, CO.sub.2 and NH.sub.3 and possibly COS;
- (b) removing HCN, and possibly COS, from said solids-free synthesis gas stream;
- (c) contacting said solids-free stream with water and cooling said stream, and producing cooled synthesis gas and a solution containing NH.sub.3 and dissolved CO.sub.2 ;
- (d) stripping said solution containing ammonia and CO.sub.2 to produce a stripped aqueous solution containing a reduced concentration of ammonia and CO.sub.2 ;
- (e) utilizing the stripped aqueous solution from step (d) as at least part of the aqueous scrubbing solution of step (a).
A process for the removal of flyslag from a gas stream containing flyslag and CO.sub.2, the gas stream derived from the gasification of coal, comprising
- (a) passing said gas stream containing flyslag to a solids separation zone, and separating the bulk of the flyslag in said zone, producing solid flyslag and a gas stream having reduced flyslag content;
- (b) passing gas stream having reduced flyslag content from step (a) to a scrubbing zone and scrubbing said gas stream with an effective amount of an aqueous scrubbing solution and removing remaining flyslag particles from said stream, producing a substantially solids-free CO.sub.2 -containing synthesis gas stream;
- (c) removing HCn from said solids-free CO.sub.2 -containing synthesis gas stream;
- (d) contacting said solids-free CO.sub.2 -containing stream with water and cooling said stream, and producing cooled synthesis gas and a solution containing NH.sub.3 and dissolved CO.sub.2 ;
- (e) stripping said solution containing ammonia and CO.sub.2 to produce a stripped aqueous solution containing a reduced concentration of ammonia and CO.sub.2 ;
- (f) utilizing the stripping aqueous solution from step (e) as at least part of the aqueous scrubbing solution of step (b).
A process for the gasification of coal comprising
- (a) partially combusting particulate coal in a gasification zone comprising at least one gasification reactor, and producing a hot gaseous stream containing synthesis gas, flyslag, and minor amounts of HCN, NH.sub.3, and CO.sub.2 ;
- (b) quenching and hot cooling said gaseous stream, and removing at least the bulk of the flyslag therefrom, producing a cooled gaseous stream having reduced flyslag content;
- (c) passing gas stream having reduced flyslag content from step (b) to a scrubbing zone and scrubbing said gas stream with an effective amount of an aqueous scrubbing solution and removing remaining flyslag particles from said stream, producing a substantially solids-free CO.sub.2 -containing synthesis gas stream;
- (d) removing HCN from said solids-free CO.sub.2 -containing synthesis gas stream;
- (e) contacting said solids-free CO.sub.2 -containing stream with water and cooling said stream, and producing cooled synthesis gas and a solution containing NH.sub.3 and dissolved CO.sub.2 ;
- (f) stripping said solution containing ammonia and CO.sub.2 to produce a stripped aqueous solution containing a reduced concentration of ammonia and CO.sub.2 ;
- (g) utilizing the stripped aqueous solution from step (f) as at least part of the aqueous scrubbing solution of step (c).
Dependencies are inferred from the claim text.