Semi-decarbonized to fully decarbonized
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We have a 60,000 tons/year joint alcohol synthesis ammonia production line. We are currently using pressure swing adsorption semi-decarbonization. We want to change the semi-decarbonization system to full decarbonization with a CO2 content of less than 1.0. Could you please recommend a manufacturer for sub-system design? Thank you.
The pressure swing adsorption gas loss is large. We have changed it many times and it is finally OK.
Let’s look at Sichuan Tianyi. It is the leader in pressure swing adsorption, but I’m afraid I’m too young to take it. I contacted you at the early stage, but it was difficult.
:) In fact, some designs do not require a very professional design institute, otherwise it will only be laborious and costly. If necessary, please contact me at 13506448334
The raw gas is semi-water gas, which is sent to the full decarbonization section after desulfurization and conversion sections. The gas volume is less than 35,000 standard cubic meters, the inlet system pressure is 0.86MPA, the existing pipeline diameter is 350, and the CO2 content of the decarbonization system is required to be less than 1.0%, and the recovery of CO2 The purity reaches 98%, and the pressure difference of the entire system is not less than 0.05MPA. The back-end sections are activated carbon fine desulfurization section, joint alcohol section, ammonia synthesis section, and membrane hydrogenation section. There is now a semi-decarbonized PSA device with a gas processing capacity of about 15,000. It is hoped that it can be transformed on this basis.