How should the low-pressure startup method be used in the CO2 stripping process, and what issues need to be considered?
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According to the design, the low-pressure start-up method should be used for the CO2 stripping process. I would like to ask: how should the low-pressure start-up method be implemented in the CO2 stripping process, and what issues need to be taken into consideration? Thank you!
There is a paper online that specifically discusses driving at low pressure; you can download it. If you can’t find it, I can also send it to you.
ttlkk: Brother, thank you so much! Please send the information to me; my email address is ymtuegj12@163.com. Thank you again! :lol
It has been sent to your email; please check it. If you don’t receive it, please contact me.
I have received the materials, thank you! ! ! ! ! ! ! ! :lol
Elder brother: Could you send it to me? I am currently working on coordinating the process design for urea production using the 300,000-ton carbon dioxide method. My email address is musijun@126.com