The problem of compressors compressing the gas at the top of the tower
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The screw compressors in the atmospheric and vacuum distillation unit compress the low-pressure gas at the top of the tower, which is then sent to the pipeline network. I want to calculate how much heat can be released by the compressed gas, and how much water can be cooled to the desired temperature range. Knowing the pressure and temperature of the gas as it enters and exits the compressor, how can one calculate the heat released by the compressed gas?
Does no one know? Q:Q:Q:Q:Q:Q