Discussion on the factors influencing the selection of PSA hydrogen production adsorption tower quantities
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Gentlemen, I have a project for producing hydrogen from coke oven gas; the output of hydrogen is 2000 NM3, with a required hydrogen yield of 85%. How should this system be designed? Would a 6-2-3 process work? Is a vacuum pump needed? What is the difference from the 8-2-3 process in terms of cost and operational upstream aspects? I hope you will kindly share your insights!
Choosing 6-2-3 VPSA is more economical and yields higher results.