Stirring extraction from the pressurized side stream of a single tower – the energy consumption issue in single-tower systems
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How is the steam consumption calculated in the acidic water stripping process with single-tower pressurized side-stream extraction? I earnestly ask all the experts for their guidance! Thank you
120-160kg/t water
These are just rough figures; is there a specific method for calculation?
It mainly depends on the properties of your acidic water; our hydrogen sulfide level is 30+ G/L, ammonia level is 45+ G/L. The temperature at the bottom of the feed tower is controlled at 161 degrees, and the purified water meets the required standards. It is heated using steam at 1.0 MPA, with a flow rate of 5 T/H
It mainly depends on the properties of your acidic water and the quality of the gas vapor