Each project has two separate phases of equal cost and providing equal cash flow benefits. The board is willing to consider adopting the first phase of any project without the….
Determine the size of the adsorption vessels?
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