Some issues with gas shift
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This post was last edited by 654262293 on 2010-8-10 at 16:53. I would like to ask fellow experts: how can the conditions of the gas at the inlet for transformation be better coordinated with those of the raw gas at the outlet of the upstream gasification process? That is, how can the temperature and pressure of the raw gas at the gasification outlet be better adapted to the gas shift unit? Thank you!
This post was last edited by 654262293 on 2010-8-17 at 14:25. The fixed-bed batch gas generation process requires that the pressure in the shift reaction stage be the outlet pressure of the second or third stage of the compressor (depending on which stage of the compressor is used for this reaction), with the temperature to be below 40 degrees Celsius. The Texaco gasification process is used; the pressure of the shift unit only needs to be 0.2–0.3 MPa lower than that of the gasification unit, and the temperature must meet the requirements specified for the water vapor ratio in the shift unit.