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: 106

2. Evacuation. In this step, the blowdown and purge steps of the previous cycles are combine into one step, with the gas from the bed being rejected at Po by a reversible vacuum turbine. A t the end of the step, the bed is completely empty of gas. 3. Pressurization. In this step, some of the product gas is expanded through a reversible turbine and used to pressurize the bed. At the end of the cycle, the bed is at its initial condition (P = PH, y = 0). NF < WF PH Po 0 WPR > Feed Evacuation Pressurization Figure3.26IdealThree-Step:CycleWorkandMolarFlows. Np2 >WR NPR Product >WE NE, 90

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)