Design flow for the overhead gases of the acidic water stripping tower and the solvent regeneration tower
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Regarding the design process for the overhead gases in the acidic water stripping tower and the solvent regeneration tower, is low-temperature heat recovery employed? What are the issues associated with it, such as leaks?
From our end, we go directly to the inlet of the acid gas separator in front of the main sulfur recovery furnace; the low temperature at the outlet of the acid water stripping tower is a concern, and pipeline blockages could be severe