Application of Pressure Swing Adsorption to Impurities Removal

• Published in: KAGAKU KOGAKU RONBUNSHU Vol. 13; no. 5; pp. 548 - 553
• Main Authors: Tomomura, Masaomi, Nogita, Shunsuke, Someya, Kazuo
• Format: Journal Article
• Language: English; Japanese
• Published: The Society of Chemical Engineers, Japan 1987
• Subjects: Adsorbent; Carbon Dioxide Removal; Cryogenic Air Sepatation; Impurity Removal; Pressure Swing Adsorption; Thermal Swing Adsorption
• ISSN: 0386-216X; 1349-9203
• DOI: 10.1252/kakoronbunshu.13.548

Pressure swing adsorption was applied to carbon dioxide and water removal instead of thermal swing adsorption as a pretreatment of compressed air for a cryogenic air separation plant. Due to use of a two-layer-column method, with zeolite and activated alumina packed in two separate layers, the concentration of carbon dioxide in purified air is decreased from 340 ppm to 1 ppm. The electric power unit for a pressure swing adsorption process was about 85% of that for a thermal swing adsorption process because no refrigerating heater or refrigerator was required. The carbon dioxide concentration of purified air is expressed as C=86SV2 (Pa/Pd) -1.3x-2 where C is the carbon dioxide concentration of purified air, SV is the space velocity of purified air, Pa is the adsorption pressure, Pd is the desorption pressure and x is the purge ratio.