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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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21.1 Supercritical solvents 1439<br />

Inherent characteristics <strong>of</strong> systems<br />

@ supercritical conditions<br />

Sensitivity <strong>of</strong> responses to process<br />

variables<br />

High pressure<br />

Dominance <strong>of</strong> physical characteristic<br />

on solvency over chemical<br />

Figure 21.1.12. A generic process flow sheet.<br />

Resulting promise Challenges to be met<br />

Effective recovery <strong>of</strong> solvents, and<br />

innovative fractionation possibilities<br />

Expansion <strong>of</strong> solvent spate to environmentally<br />

benign, inexpensive,<br />

and non flammable solvents and<br />

their mixtures<br />

Control and optimization<br />

High capital cost and need for<br />

recovery <strong>of</strong> mechanical energy<br />

There have been many useful attempts made to classify separation technologies.<br />

Supercritical fluids are applicable with both intra-phase and inter-phase separations. Due to<br />

the ease and flexibility in which a new phase can be formed for regeneration <strong>of</strong> the solvent,<br />

inter-phase is the more common. Furthermore, material solubility and swelling problems,<br />

particularly with organic-component based membranes, limit inter-phase separations. This<br />

is due to the enhanced solubility <strong>of</strong> these components in supercritical solvents.<br />

Generic steps involved in a typical chemical process are shown in Figure 21.1.12, with<br />

each separation sub task type identified. Environmental processes are usually dominated by<br />

feed preparation tasks while biochemical processes utilize all <strong>of</strong> the four subtasks. Blending<br />

is considered a finishing task while splitting is considered a feed preparation task. The objective<br />

criteria used for the separation may vary according to the subtask. For example, in<br />

feed preparation, technical feasibility such as removal <strong>of</strong> the fines is more appropriate while<br />

the usual economic objectives subject to technical feasibility constraints become the goal<br />

for the purification and finishing stages.<br />

The feed preparation task involves removal <strong>of</strong> insoluble components and at times<br />

non-condensable compounds. The technology selection and the scheduling <strong>of</strong> tasks are con-

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