Design of utilization process of by-product hydrogen in chlor-alkali plant?
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I want to use the by-product hydrogen from a nearby chlor-alkali plant to produce hydrogenation products. Could you please help me see if the following process is reasonable? plan: Chlor-alkali plant hydrogen (0.1MPa)--flow meter-gas cabinet--compressor (outlet 10.0MPa)---high-pressure buffer tank (design 12MPa)---hydrogenation kettle problem: 1. What type of flow meter should I choose (1000 cubic meters/hour)? 2. Is it better to use a wet gas holder or a dry gas holder? Or can I use a buffer tank? How big should a gas cabinet or surge tank be? 3. Which model of compressor is best? 4. How big should the high-pressure buffer tank be? 5. What should we pay attention to in terms of safety?
I was shocked when I saw this question from the original poster. This question is enough to be researched and needs to be calculated and carefully considered. If you really want to do it, go to consult an engineering company. Everyone here will give simple answers, right or wrong, just for reference.