Naphtha copper sheet corrosion issue
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What are the general requirements for naphtha copper sheet corrosion (for gasoline and diesel hydrogenation)? Operating point of the stripping tower. Any suggestions appreciated
Personally, I feel that for a stripping tower, the key factors are steam partial pressure, feed oil temperature, and the density of the crude oil. I hope to have more exchanges and welcome any criticism or suggestions.
Isn’t the stripper used to remove hydrogen sulfide and ammonia? Is it related to the key operating points? . . . For example, the bottom and top temperatures of the stripping tower, as well as the pressure in the stripping tower? Isn’t low pressure and high temperature favorable for removal? How much is generally controlled? Give me a suggestion. Thank you