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US 2025/0186934 A1Published application
Integrated hydrogen production and carbon dioxide recovery process
AssigneeUop LLC
InventorsLin Jin, John D. Wilkinson, Bradley Russell, Oluwaseyi Kayode, Erick J. Bennett, III, Shubhra J. Bhadra
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Abstract
Integrated processes for hydrogen production and carbon dioxide recovery are described. The processes use a chilling stream in a cryogenic carbon dioxide recovery unit. The chilling stream chills a working fluid which chills the hydrogen-depleted tail gas stream from a hydrogen pressure swing adsorption (PSA) unit to form a carbon dioxide product stream.
Claims20
An integrated process for hydrogen production and carbon dioxide recovery comprising:
- introducing a feed stream comprising hydrocarbons or a carbonaceous feedstock to a synthesis gas production zone comprising a syngas reactor to produce a synthesis gas stream comprising hydrogen, carbon dioxide, carbon monoxide, and methane;
- separating the synthesis gas stream in a hydrogen pressure swing adsorption (PSA) unit to form a high-pressure hydrogen product stream enriched in hydrogen and a hydrogen-depleted tail gas stream;
- chilling a working fluid stream with a chilling stream in a first heat exchanger forming a chilled working fluid stream and a warmed chilling stream;
- chilling the hydrogen-depleted tail gas stream with the chilled working fluid stream in a main heat exchanger in a cryogenic carbon dioxide separation unit forming a chilled dried hydrogen-depleted tail gas stream and a warmed working fluid stream, and separating the chilled hydrogen-depleted tail gas stream into a carbon dioxide product stream comprising carbon dioxide, and an overhead stream;
- and
- passing the warmed working fluid stream to the first heat exchanger.
3 more elements
An integrated process for hydrogen production and carbon dioxide recovery comprising:
- introducing a feed stream comprising hydrocarbons or a carbonaceous feedstock to a synthesis gas production zone comprising a syngas reactor to produce a synthesis gas stream comprising hydrogen, carbon dioxide, carbon monoxide, and methane;
- separating the synthesis gas stream in a hydrogen pressure swing adsorption (PSA) unit to form a high-pressure hydrogen product stream enriched in hydrogen and a hydrogen-depleted tail gas stream;
- compressing and drying the hydrogen-depleted tail gas stream to form a dried compressed tail gas stream;
- chilling a working fluid stream with a chilling stream comprising liquefied natural gas, or liquid nitrogen, or liquid ammonia, or liquid hydrogen, or combinations thereof in a first heat exchanger forming a chilled working fluid stream and a warmed chilling stream;
- chilling the dried compressed tail gas stream with the chilled working fluid stream in a main heat exchanger in a cryogenic carbon dioxide separation unit forming a chilled dried hydrogen-depleted tail gas stream and a warmed working fluid stream, and separating the chilled hydrogen-depleted tail gas stream into a carbon dioxide product stream comprising carbon dioxide, and an overhead stream;
- passing the warmed working fluid stream to the first heat exchanger;
- separating the overhead stream in an overhead separation unit to form a low-pressure carbon dioxide stream enriched in carbon dioxide and an off-gas stream enriched in hydrogen and at least one of carbon monoxide and methane;
- and
- optionally recycling the low-pressure carbon dioxide stream to the cryogenic carbon dioxide separation unit.
6 more elements
Dependencies are inferred from the claim text.