Hydrogen and carbon dioxide coproduction

Chemistry of inorganic compounds – Carbon or compound thereof – Oxygen containing

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55 26, 55 62, 55 68, 422190, 422198, 423650, B01D 5304, C01B 324, C01B 3120

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active

049633392

ABSTRACT:
Highly purified gaseous hydrogen and liquid carbon dioxide are produced from a steam reformer/shift converter by passing the effluent from the latter through a multibed hydrogen PSA unit followed by an uncoupled carbon dioxide PSA unit. The carbon dioxide PSA unit produces a hydrogen-rich stream which is recycled to the feed to the steam reformer, a carbon dioxide-rich recycle stream which is recycled to the carbon dioxide PSA unit feed and a carbon dioxide-rich product stream which is introduced under pressure to a liquifier. A waste stream from the liquifier is recylced to the carbon dioxide PSA unit feed. A portion of the carbon dioxide-rich product stream is withdrawn from the compressor at a stage such that its pressure is higher than that of the carbon dioxide PSA unit and returned thereto as a cocurrent purge preceding bed regeneration to obtain product.

REFERENCES:
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patent: 3643451 (1972-02-01), Foucar
patent: 4460395 (1984-07-01), Nobles et al.
patent: 4726816 (1988-02-01), Fuderer
patent: 4778670 (1988-10-01), Pinto
patent: 4869894 (1989-09-01), Wang et al.
Kirk-Othmer, Encyclopedia of Chemical Technology, Third Edition, vol. 4, John Wiley & Sons (1978) pp. 725, 737, 738.

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