Incorporation of a valve equation into the simulation of a pressure swing adsorption process
โ Scribed by Cheng-Tung Choi; Huang Wen-Chung
- Publisher
- Elsevier Science
- Year
- 1994
- Tongue
- English
- Weight
- 891 KB
- Volume
- 49
- Category
- Article
- ISSN
- 0009-2509
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โฆ Synopsis
A valve equation is incorporated into the simulation to consider dynamic change of the bed pressure and mass transfer between the gas phase and solid phase during the pressurization and blowdown steps of a simple two-bed air separation pressure swing adsorption (PSA) process. The valve equation approach is shown to provide a good representation of the cyclic steady state results and approach behavior of residual oxygen concentration in the product to cyclic steady state value, experimentally measured by Hassan et al. (1986) for an air-carbon molecular sieve (CMS) system. The influence on product purity of the pressure-changing steps was also studied by this approach. For two PSA systems, air_CMS for producing nitrogen and air-5A zeolite for producing oxygen, the theoretical results obtained with the valve equation included are compared with those obtained from the assumption of a frozen solid phase and with the assumption of a linear pressure change.
๐ SIMILAR VOLUMES
The numerical model, originally developed to simulate the kinetic separation of air in a carbon molecular sieve pressure swing adsorption unit, has been extended and applied to the equilibrium selective separation of air over a zeolite adsorbent in which nitrogen is preferentially adsorbed, Leaving
## Abstract In this study, trends from an adsorption process simulator are compared against experimental results obtained from a Rapid Pressure Swing Adsorption (RPSA) pilot plant for the separation of air over a packed bed of LiLSX pellets. The primary purpose of this study was to examine the impa