A gaseous feed stream at T=35 C and 2000 kpa
The idea is to design a Pressure Swing Absorber (PSA) Unite to purify hydrogen
a/choose an adsorbent that can perform the duty . State its adsorbent properties?
b/ Determine the amount of the absorbent needed ?
C/Determine the size of the adsorption vessels?
D/Determine the pressure and temperature and compositions for the product stream and the purge stream ?
F/ determine the number of the vessels needed to complete the cycle?
G / Find the saturation time and the regeneration time?
Please provide equations and sources for any used data.
Please use clear hand writing
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