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Supercritical Carbon Dioxide Circulated EGS Combined with IGCC in New Mexico in the bed, which reduces the equilibrium nitrogen holding capacity of the adsorbent (Smith, 2001). Characteristics Separate pretreatment of the air is required in order to remove water and carbon dioxide, Oxygen purity is typically 93–95 vol%. Due to the cyclic nature of the adsorption process, bed size is the controlling factor in capital cost. Production is proportional to bed volume, capital costs increase more rapidly as a function of production rate compared to cryogenic plants. 4.2.2.2 Polymeric Membranes Figure 31: Polymeric Membranes Polymeric membranes work on the differences in rates of diffusion for oxygen and nitrogen through a membrane, which separates high-pressure and low-pressure process streams. The economics of membrane systems are determined by flux and selectivity. Flux determines the membrane surface area, and is a function of the pressure difference divided by the membrane thickness. As oxygen molecules are smaller in size compare to nitrogen, most membranes are permeable to oxygen than to nitrogen. Active or facilitated transport membranes, which incorporate an oxygen-complexing agent to increase oxygen selectivity, are a potential means to increase the oxygen purity from membrane systems, assuming oxygen compatible membrane materials are also available. Penn State University | 4.2 Air Separation Unit 56PDF Image | GREAT NECK WATER POLLUTION CONTROL DISTRICT NASSAU COUNTY, NEW YORK MICROTURBINE INSTALLATION FEASIBILITY STUDY
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