MATERIAL BALANCE
MATERIAL BALANCE
MATERIAL BALANCE
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OutputHydrogen (H2) 6474.9 kmol/hrCarbon monoxide (CO) 31.7 kmol/hrCarbon dioxide (CO2) 1879.0 kmol/hrMethane (CH4) 19.0 kmol/hrNitrogen (N2) 2148,4 kmol/hrInerts (Ar +others) 9.5 kmol/hrSteam (H2O) 4289.5 kmol/hrCondenserThe exit stream from the Low temperature Converter is sent into a condenser toremove the steam present which would be an additional excess load on theAbsorberWithin the condenser all the water is removed as condensate. Only water isremoved and the exit stream from this goes to the AbsorberInputHydrogen (H2) 6474.9 kmol/hrCarbon monoxide (CO) 31.7 kmol/hrCarbon dioxide (CO2) 1879.0 kmol/hrMethane (CH4) 19.0 kmol/hrNitrogen (N2) 2148,4 kmol/hrInerts (Ar +others) 9.5 kmol/hrSteam (H2O) 4289.5 kmol/hrOutputHydrogen (H2) 6474.9 kmol/hrCarbon monoxide (CO) 31.7 kmol/hrCarbon dioxide (CO2) 1879.0 kmol/hrMethane (CH4) 19.0 kmol/hrNitrogen (N2) 2148,4 kmol/hrInerts (Ar +others) 9.5 kmol/hr
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