Nitrogen purity control in the air separation unit of an IGCC power generation system
AssigneeAir Products and Chemicals, Inc.
InventorDavid Miller Espie
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AssigneeAir Products and Chemicals, Inc.
InventorDavid Miller Espie
Estimating the term…
A cryogenic air separation system which is subject to periods of significant changes in product demand is controlled during such periods to minimize the impact of transient operation on product purity. A double-column distillation system is utilized in which a nitrogen-rich liquid is withdrawn from the higher-pressure column and introduced into the lower-pressure column as reflux. An inventory of this liquid is maintained in a holdup tank for storage or withdrawal during periods of transient operation. In addition, nitrogen vapor product from the lower-pressure column is recycled to the higher-pressure column, and the nitrogen vapor recycle rate is controlled as a function of the liquid level in the holdup tank. The flow rate of nitrogen-rich liquid withdrawn from the higher-pressure column is controlled as a function of its composition. The flow ratio of the nitrogen vapor recycle to the nitrogen-rich liquid reflux is controlled as a function of the composition of the nitrogen vapor withdrawn from the lower-pressure column. A feedforward control system increases the flow rate of the nitrogen-rich liquid withdrawn from the higher-pressure column during periods of increasing product demand and decreases the flow rate during periods of decreasing product demand.
In a process for the separation of air wherein an air feed stream is introduced into a multiple-column cryogenic distillation system comprising at least a higher-pressure column and a lower-pressure column, wherein a nitrogen-enriched vapor stream is withdrawn from the lower-pressure column, and wherein a nitrogen-enriched liquid stream is withdrawn from the higher-pressure column, reduced in pressure, and introduced into the lower-pressure column as a reduced-pressure nitrogen-enriched liquid reflux stream, a method of operating the cryogenic distillation system which comprises:
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