β Scribed by W. Wang; R. Z. Wang; Y. X. Xu; J. Y. Wu; Y. B. Gui
No coin nor oath required. For personal study only.
This paper describes an experimental investigation of adsorption refrigeration with a single generator (adsorbent bed) in a basic cycle, which verifies the previous theoretical conclusions that the cycle time and the maximum desorption temperature (corresponding to the maximum temperature of external heat source) are key factors with various influences to the COP and the cooling capacity of a cycle on a prototype machine. Moreover, in order to investigate the difference between theoretical and real cycles, a new physical parameter, the packing coefficient, is introduced to the adsorption cycle 1998 John Wiley & Sons Ltd.
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A numerical study on heat and mass transfer in an annular adsorbent bed filled with adsorbent granules for an isobaric adsorption process is performed. In order to reduce the number of independent parameters that influences heat and mass transfer in the bed, the governing equations and related initi
## Abstract Streamline Direct CST I is a new type of ion exchanger with multiβmodal functional groups, specially designed for an expanded bed adsorption (EBA) process, which can capture directly the proteins from the high ionic strength feedstocks with a high binding capacity. In this study, an exp
Lysozyme adsorption and purification by expanded bed chromatography of a customized Nd-Fe-B alloy-densified agarose (NFBA) gel modified with Cibacron Blue 3GA (CB) were investigated, and the results were compared with those obtained with CB-modified Streamline gel (CB-Streamline). The NFBA gel had a
The adsorption of dimethylglyoxime (DMG) on six commercial activated carbons and on lignite was investigated with the aim to manufacture a modified adsorbent which is capable of separating palladium selectively from metal ion mixtures in nitric acid solutions. The DMG adsorption isotherms and the pa