1997
DOI: 10.1002/aic.690431013
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Study of a six‐bed pressure swing adsorption process

Abstract: A mathematical model of a six-bed, ten-step PSA operation is developed. The process cycle considered resembles an industrial hydrogen recovery process from the refinery fuel gas. Three hydrocarbon impurities (methane, ethane, and propane)

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Cited by 40 publications
(32 citation statements)
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“…This is similar to processes described in Malek and Farooq (1997) and Waldron and Sircar (2000). The adsorbent bed is packed with APHP and UOP 5A zeolite occupying one third and two thirds of the bed, respectively.…”
Section: Process Descriptionsupporting
confidence: 66%
“…This is similar to processes described in Malek and Farooq (1997) and Waldron and Sircar (2000). The adsorbent bed is packed with APHP and UOP 5A zeolite occupying one third and two thirds of the bed, respectively.…”
Section: Process Descriptionsupporting
confidence: 66%
“…The dual-sorbent PSA process was operated with the same cycle sequence adopted in the previous single-sorbent study (Malek and Farooq, 1997b). Therefore, the assumptions of the extended model are broadly similar to those made in the previous study.…”
Section: Simulation Of Dual-sorbent Psa Processmentioning
confidence: 97%
“…The equilibrium isotherm parameters and mass-and wall heat-transfer parameters used in (Malek and Farooq, 1997b) and compiled in Table 2 of that publication are used in the present study without any change. The additional equilibrium and mass-transfer parameters required in the extended dualsorbent model presented here are given in Table 2.…”
Section: Simulation Of Dual-sorbent Psa Processmentioning
confidence: 99%
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