Method of producing a hydrogen-enriched product and recovering CO2 in a hydrogen production process unit
AssigneeUop LLC
InventorsAddison Cruz, Bradley Russell, Erick J. Bennett, III, Kurt Kraus, Stefano Bietto, William Cady, Kyle Cuellar, Oluwaseyi Kayode
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Abstract
A process and apparatus for producing a hydrogen-enriched product and recovering CO2 from an effluent stream from a hydrogen production process unit are described. The process utilizes a CO2 recovery system integrated with a PSA system that produces at least two product streams to recover additional hydrogen and CO2 from the tail gas stream of a hydrogen PSA unit in the hydrogen production process.
Claims20
A method of producing a hydrogen-enriched product and recovering CO2 comprising:
- processing a feed stream comprising hydrocarbons or a carbonaceous feedstock in a hydrogen production process unit to produce a synthesis gas mixture comprising hydrogen, carbon dioxide, water, and at least one of methane, carbon monoxide, nitrogen, and argon;
- separating an effluent stream comprising the synthesis gas from the hydrogen production process unit in a hydrogen pressure swing adsorption (PSA) unit into a first hydrogen stream enriched in hydrogen and a hydrogen depleted tail gas stream comprising a portion of the hydrogen, the carbon dioxide, the water, and the at least one of the methane, the carbon monoxide, the nitrogen, and the argon;
- compressing the hydrogen depleted tail gas stream in a compressor to form a compressed tail gas stream;
- separating the compressed tail gas stream in a CO2 recovery system into a CO2-enriched product stream and an overhead stream comprising the portion of the hydrogen, a portion of the carbon dioxide, and the at least one of the methane, the carbon monoxide, the nitrogen, and the argon;
- separating the overhead stream from the CO2 recovery system in a PSA system that produces at least two product streams into at least a second hydrogen stream enriched in hydrogen, and a CO2 stream enriched in carbon dioxide;
- recovering the second hydrogen stream;
- and
- optionally recycling the CO2 stream to the compressor.
A method of producing a hydrogen-enriched product and recovering CO2 comprising:
- processing a feed stream comprising hydrocarbons or a carbonaceous feedstock in a hydrogen production process unit to produce a synthesis gas mixture comprising hydrogen, carbon dioxide, water, and at least one of methane, carbon monoxide, nitrogen, and argon;
- separating an effluent stream comprising the synthesis gas mixture from the hydrogen production process unit in a hydrogen pressure swing adsorption (PSA) unit into a first hydrogen stream enriched in hydrogen and a hydrogen depleted tail gas stream comprising a portion of the hydrogen, the carbon dioxide, the water, and the at least one of the methane, the carbon monoxide, the nitrogen, and the argon;
- compressing the hydrogen depleted tail gas stream in a compressor to form a compressed tail gas stream;
- drying the compressed tail gas stream in a dryer to remove the water;
- cooling the dried tail gas stream in a chiller to a temperature of about −20° C. to about −50° C. to form a chilled tail gas stream;
- separating the chilled tail gas stream in a CO2 recovery system into a CO2-enriched product stream and an overhead stream comprising the portion of the hydrogen, a portion of the carbon dioxide, and the at least one of the methane, the carbon monoxide, the nitrogen, and the argon;
- separating the overhead stream from the CO2 recovery system in a PSA system that produces at least two product streams into at least a second hydrogen stream enriched in hydrogen, and a CO2 stream enriched in carbon dioxide;
- recovering the second hydrogen stream;
- and
- recycling the CO2 stream to the compressor.
An apparatus for producing a hydrogen-enriched product and recovering CO2 comprising:
- a hydrogen production process unit having at least one inlet and at least one outlet;
- a hydrogen PSA unit having an inlet, a hydrogen outlet, and a tail gas outlet, the hydrogen PSA unit inlet in fluid communication with the hydrogen production process unit outlet;
- a compressor having an inlet and an outlet, the compressor inlet in fluid communication with the hydrogen PSA tail gas outlet;
- a dryer having an inlet and at least one outlet, the dryer inlet in fluid communication with the compressor outlet;
- a chiller having a gas inlet, a gas outlet, a chilling fluid inlet and a chilling fluid outlet, the chiller gas inlet in fluid communication with the dryer outlet, the chiller fluid inlet in fluid communication with a source of chilling fluid;
- a CO2 recovery system having an inlet, a first outlet, and an overhead outlet, the CO2 recovery system inlet in fluid communication with the chiller gas outlet;
- and
- a PSA system having at least an inlet, a hydrogen outlet, and a CO2 outlet, the PSA system inlet in fluid communication with the CO2 recovery system overhead outlet, and the CO2 outlet in fluid communication with the compressor inlet.
Dependencies are inferred from the claim text.