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Solubilities of heavy fossil fuels in compressed gases. Calculation of dew points in tar-containing gas streams. [Coal tar in methane from ambient conditions to 100 bar and 600 K]

Journal Article · · Ind. Eng. Chem. Process Des. Dev.; (United States)
DOI:https://doi.org/10.1021/i200025a006· OSTI ID:6653792
A molecular-thermodynamic model is used to establish a correlation for solubilities of heavy fossil fuels in dense gases (such as those from a coal gasifier) in the region ambient to 100 bar and 600 K. This model is then applied to calculate dew points in tar-containing gas streams. The heavy fuel is fractionated in a spinning-band column at high reflux; each fraction is considered to be a pseudocomponent. Each fraction is characterized by one vapor-pressure datum (obtained during fractionation), elemental analysis, and proton NMR spectra (to determine aromaticity). Liquid-phase properties are obtained from the SWAP equation for vapor pressure and from a density correlation. Vapor-phase properties are obtained with the virial equation of state with virial coefficients from Kaul's correlation. Experimental solubility measurements have been made for two Lurgi coal-tar fractions in dry and moist methane. Calculated and experimental solubilities agree well. The correlation is used to establish a design-oriented computer program for calculating isobaric condensation as a function of temperature as required for design of a continuous-flow heat exchanger.
Research Organization:
Lawrence Berkeley Laboratory, Univ. of California, Berkeley, CA
OSTI ID:
6653792
Journal Information:
Ind. Eng. Chem. Process Des. Dev.; (United States), Journal Name: Ind. Eng. Chem. Process Des. Dev.; (United States) Vol. 23:2; ISSN IEPDA
Country of Publication:
United States
Language:
English