How to optimize the operation of a shift stripper? Thanks for your replies!
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How can the operation of a shift stripper be optimized to improve its stripping efficiency? Please share the operating parameters of your company’s strippers, as well as the pH, total alkalinity, and total hardness of the low-temperature, low-pressure shift condensate. I hope everyone will participate actively and offer as much help as possible. Thank you.
Please provide a detailed description of what kind of tray it is. If possible, without changing the existing setup and as long as the operating conditions permit, try to reduce the operating pressure and increase both the temperature inside the tower and the temperature at the tower outlet!
In a sieve plate tower, pressure and temperature are matched; if the pressure is low, how can the temperature increase?
Reducing pressure is to ensure the gas flow rate and temperature exiting the tower. Raising the temperature is intended to ensure better separation of ammonia nitrogen in the condensate; what I mean is finding a balance between temperature and pressure.
It is usually low pressure and high temperature; for nitrogen, it is generally used to maintain pressure in the system during shutdown.