28.02.2013 Views

Handbook of Solvents - George Wypych - ChemTech - Ventech!

Handbook of Solvents - George Wypych - ChemTech - Ventech!

Handbook of Solvents - George Wypych - ChemTech - Ventech!

SHOW MORE
SHOW LESS

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

22.1 Absorptive solvent recovery 1527<br />

Figure 22.1.12. Pressure drop for various activated carbon types.<br />

Figure 22.1.13. Adsorption isotherm <strong>of</strong> tetrahydr<strong>of</strong>uran for several temperatures.<br />

bed also a temperature front follows in the same direction. To deal with the adsorption heat<br />

the inlet solvent concentration is usually limited to about 50 g/m 3 .<br />

The adsorption capacity <strong>of</strong> the adsorbent increases with pressure because the partial<br />

pressure <strong>of</strong> the solvent increases. An increase in adsorber temperature causes a reduction in<br />

adsorption capacity. Because the equilibrium capacity is lower at higher temperatures, the<br />

dynamic capacity (working capacity) <strong>of</strong> the activated carbon adsorber will also be lower. To<br />

enhance adsorption, the inlet temperature <strong>of</strong> the adsorber should be in the range <strong>of</strong> 20-40°C.<br />

In Figure 22.1.13 the adsorption isotherms <strong>of</strong> tetrahydr<strong>of</strong>uran on activated carbon D43/3 for<br />

several temperatures are shown. 13

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!