Energy Efficiency of Gas Separation Pressure Swing Adsorption

PDF Publication Title:

Energy Efficiency of Gas Separation Pressure Swing Adsorption ( energy-efficiency-gas-separation-pressure-swing-adsorption )

Previous Page View | Next Page View | Return to Search List

Text from PDF Page: 071

3.2.4 Purge Step During the purge step, pure product is throttled to low pressure and used to purge the remaining heavy gas from the adsorbent bed. As with the blowdown step, work is only required if PL < Po; otherwise, the gas is allowed to escape to the atmosphere. During the purge step, a simple wave develops because the mole fraction of the product is less than the mole fraction of the gas in the bed (see Figure 3.7). In this section we develop a mathematical understanding of the purge process in order to calculate the number of moles of pure product necessary to purge the bed (Npu), the number of moles that are purged out of the bed (Nw), and the work required to purge an adsorbent bed. The method of characteristics is used to solve the equations relating to the simple wave. This method is more fully developed by Knaebel and Hill (1985) and states that at constant pressure, the composition is constant along the characteristics. This means that the axial position in the bed with mole fraction y and distance from the product end of the bed z, moves with speed (Equation (10) in Knaebel and Hill, 1985): *= f*u =Constant ^ dt l+ (B-\)y This includes the position at the far right of the simple wave, which has mole fraction zero (point A in Figure 3.7). It is important at this point to note that the velocity of the characteristic (the position with mole fraction y = constant) is related to, but not equal to the velocity of the gas at that axial position in the bed. For this reason, Figure 3.7 makes a distinction between these two velocities; UAis the velocity of the gas through the adsorbent bed at 55

PDF Image | Energy Efficiency of Gas Separation Pressure Swing Adsorption

PDF Search Title:

Energy Efficiency of Gas Separation Pressure Swing Adsorption

Original File Name Searched:

ubc_1997-0009.pdf

DIY PDF Search: Google It | Yahoo | Bing

CO2 Organic Rankine Cycle Experimenter Platform The supercritical CO2 phase change system is both a heat pump and organic rankine cycle which can be used for those purposes and as a supercritical extractor for advanced subcritical and supercritical extraction technology. Uses include producing nanoparticles, precious metal CO2 extraction, lithium battery recycling, and other applications... More Info

Heat Pumps CO2 ORC Heat Pump System Platform More Info

CONTACT TEL: 608-238-6001 Email: greg@infinityturbine.com (Standard Web Page)