Abstract

The sour waters from the synthetic fuel industries will contain substantial percentages of carbon dioxide, phenolics, hydrogen cyanide, acetic, and other carboxylic acids. The use of multi-component-dependent stage efficiencies for sour-water stripper caluclations is discussed. It was established from actual operating data on sour-water strippers that the more volatile a component in a mixture, the lower the stage efficiency of that compound. (JMT)

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