This study is designed to examine t
he effects of supercritical fluid (SCF) solvents (pentane or
hexane) on product distributions from Fisc
her-Tropsch synt
hesis (FTS) over an alumina-supported cobalt catalyst in a fixed-bed-reactor. T
he influence of reaction conditions (such astemperature, pressure, syngas feed ratio, contact time, and space velocity) on t
he FTShydrocarbon product distributions in t
he supercritical solvents was studied. Changing t
hedensity-dependent bulk t
hermophysical properties of t
he supercritical pentane medium, by tuningeit
her temperature (210-250
C) or pressure (45-65 bar), resulted in notable effects on t
he(C
6+) hydrocarbon product distributions and selectivity. One particular set of experiments wasdesigned to directly compare
hexane and pentane solvent effects at constant density (ca.,
=0.3 g/cm
3) and temperature (240
C) w
here significantly hig
her pressure was required in pentaneto achieve this density. Interestingly, both pentane and
hexane supercritical FTS performedalmost identically at t
he common density, in terms of hydrocarbon product distribution; however,hig
her CO conversion was obtained for t
he pentane phase reaction, because of t
he pressureeffects on t
he kinetics. Within t
he investigated range of conditions, t
he chain-growth probability(
-value) increases as t
he pressure increases and t
he temperature decreases; however, t
heinfluence of reaction temperature on t
he chain growth probability was determined to be morepronounced than that of t
he effect of pressure. Through comparison of hydrocarbon distributionsin both SCF-phase and gas-phase FTS, we conclude that t
he enhanced
-value in SCF-FTS isdue to t
he enhanced solubilities of
heavy hydrocarbon products in t
he SCF medium, t
herebyimproving vacant-site accessibility for t
he readsorption of olefins and subsequent chain growth,as well as t
he elimination of t
he adsorption layer.