CAPE-OPEN

Dear Jasper, The attached flowsheet is simulation of PFR for methanol synthesis from CO,CO2 and H2O. The wall heat transfer coefficient is set to zero and tube heat transfer coefficient have been set to 500 W/m2.K . On running the simulation, it is found that the enthalpyF balance is not zero. Can y...

The data which i have used and what i intend to do is given here
http://www.ep.liu.se/ecp/119/015/ecp15119015.pdf

my fsd file is also attached.

Sir what about the reactions happening in fixed conversion reactor which I actually want to carry out in cstr & gibbs, and remove the fixed conversion reactor?

Hello, in the attached file can i eliminate fixed conversion reactor and carry out the reactions currently happening in fixed conversion reactor to take place in CSTR and gibbs used ahead itself ....as it shows some equilibrium error?

No longer facing this issue thank you.

I have attached my file, it has warnings regarding equilibrium calculation can you tell me more about it and how can i remove those warnings?

Hello , I am carrying out the below mentioned reactions in a fixed bed reactor
C + H2O ---> CO + H2
C + C02 ---> 2CO

Is it possible to carry out these reactions in CSTR too? If yes then how?

hello i am using a fixed conversion reactor and the reaction taking place is: C + 2 H2 -----> CH4 graphite plus hydrogen giving methane , graphite in solid phase whereas hydrogen and methane in vapour. ( specifications: input stream H2= 0.8267 kg/h inlet temperature , pressure is 800 degrees celsius...