Hi to everybody
I'm working in hydrogen production unit that works with steam reforming process.
after changing of unit catalysts we have some problems!!!
the first that conductivity in deaerator is higher than normal range ( 120 micros/cm )!!
second that seems is relative with first problem is that in the out let of high temperature shift conversion reactor we have less hydrogen percentage than inlet of reactor!! that means in this reactor we have hydrogen consumption !!! please help me with your comments ...
for example : refromer outlet : H2=79, Methane=2, CO=4, CO2=14, N2=1 mol%
HTSC outlet : H2=73, Methane=2, CO=.2, CO2=23.8, N2=1 mol%