A two stage PSA process for argon and hydrogen recovery from ammonia p
urge gas was developed. Appropriate adsorbents were selected by consid
ering adsorption equilibrium and regeneration possibility. A continuou
s process, which can treat about 100 Nm(3)/h of ammonia purge gas, was
designed by applying the adsorption equilibrium and breakthrough test
results. The continuous process consists of 2 stage PSA with 4 beds r
espectively. Product hydrogen (>99%) can be obtained from the first st
age during first period of adsorption step, and also from the second s
tage. An intermediate product, argon and hydrogen mixture, is obtained
from the first stage during the second period of adsorption step, and
this is sent to the second stage to be separated into high purity arg
on and hydrogen respectively. From the raw purge gas containing about
6% argon, argon is concentrated upto 14% through the first stage, and
upto 97% through the second stage PSA.