PRESSURE SWING ADSORPTION PROCESSES FOR AIR SEPARATION WITH ZEOLITE

PDF Publication Title:

PRESSURE SWING ADSORPTION PROCESSES FOR AIR SEPARATION WITH ZEOLITE ( pressure-swing-adsorption-processes-for-air-separation-with- )

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

Text from PDF Page: 007

M. Mofarahi, E. J. Shokroo/Petroleum & Coal 55(3) 216-225, 2013 222 oxygen recovery has an almost the same value for two types of zeolites, while oxygen purity of zeolite 5A takes precedence over zeolite 13X when the adsorption pressure was higher than 3.5 bar. Fig. 4 Simulated concentration breakthrough curves at 6 atm adsorption pressure and 5 LSTP/min feed flow rate, (adsorption bed was initially saturated with a non-adsorptive gas at 6 atm and 298 K), a: zeolite 13X & b: zeolite 5A. Fig. 5 The differences between adsorption capacities for zeolite 5A & 13X, a: oxygen and b: nitrogen. Fig. 6 Oxygen purity and recovery as a function of P/F Fig. 7 Oxygen purity and recovery as a function of feed flow rate, (PH = 6 bar).

PDF Image | PRESSURE SWING ADSORPTION PROCESSES FOR AIR SEPARATION WITH ZEOLITE

PDF Search Title:

PRESSURE SWING ADSORPTION PROCESSES FOR AIR SEPARATION WITH ZEOLITE

Original File Name Searched:

pc_3_2013_javadi_221.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)