Abstract
An effect of the compressive self-heating of supercritical carbon dioxide has been observed both in the stationary and flow regimes. The effect is probably caused by fluid compression in near-adiabatic conditions during system filling and pumping. This phenomenon should be taken into account during designing and optimization of systems employing sub- and supercritical fluids for such processes as supercritical fluid extraction, chromatography, aerogel drying etc.
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