Treatment of condensate from the conversion unit
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The volume fraction of components in this liquid is 2.35% CO2, 2.94% NH3, 0.13% H2S; the rest is water. What can be done about this? Seeking advice
The single-tower low-pressure full-blowout acidic water stripping process is adopted, with the gas at the top of the tower being sent to a sulfur furnace for combustion.
The volume is very low, only 3 t/h, and the CO2 content is high while the H2S content is low – is that acceptable?