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Title: Coal gasification pilot plant support studies. Subtask 3-2. Phase equilibrium studies as applied to treatment of raw bases from coal gasification. [122 to 403/sup 0/F and 590 to 2800 psia]

Technical Report ·
DOI:https://doi.org/10.2172/7182250· OSTI ID:7182250

Several methods to predict the phase equilibrium behavior of gas mixtures at different temperatures and pressures appear in the literature. In this study, four of these correlations have been evaluated using experimentally derived vapor-liquid equilibrium compositions and phase densities. The experiments were conducted with simulated coal gasification product gas-benzene mixtures over a temperature range of 122/sup 0/ to 403/sup 0/F and pressure range of 590 to 2800 psia. The four correlations evaluated were the Peng-Robinson, the Soave Redlich-Kwong, the Redlich-Kwong Chao-Seader, and the Redlich-Kwong Grayson-Streed. Interaction coefficients for several of the components of interest for use in the Peng-Robinson equation of state were also determined from available binary vapor-liquid equilibrium data. Of the four available vapor-equilibrium correlations evaluated, the Peng-Robinson correlation provided the closest approximation to the experimental results. The next closest correlations were the Soave Redlich-Kwong, the Redlich-Kwong Chao-Seader, and the Redlich-Kwong Grayson-Streed.

Research Organization:
Institute of Gas Technology, Chicago, IL (United States)
DOE Contract Number:
AC21-78ET11330
OSTI ID:
7182250
Report Number(s):
FE-2306-15
Country of Publication:
United States
Language:
English