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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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1532 Klaus-Dirk Henning<br />

Figure 22.1.18. Supersorbon � process for toluene recovery (After reference 30).<br />

Solvent-laden air is exhausted at the three rotogravure printing presses by several fans<br />

operating in parallel and is routed in an upward flow through four adsorbers packed with<br />

Supersorbon � activated carbon. The solvent contained in the air is adsorbed on the activated<br />

carbon bed. Adsorption continues until breakthrough, when the full retentive capacity <strong>of</strong> the<br />

adsorbent for solvent vapors is used up.<br />

The purity <strong>of</strong> the clean exhaust air complies with the regulation for emission level <strong>of</strong><br />

less than 50 mg/m 3 . Regeneration <strong>of</strong> the adsorbent takes place by desorbing the solvent with<br />

a countercurrent flow <strong>of</strong> steam. The mixture <strong>of</strong> water and toluene vapors is condensed and<br />

the toluene, being almost insoluble in water, is separated by reason <strong>of</strong> its different density in<br />

a gravity separator. The recovered toluene can be re-used in the printing presses without further<br />

treatment. Very small amounts <strong>of</strong> toluene dissolved in the wastewater are removed by<br />

stripping with air and returned to the adsorption system inlet together with the stripping air<br />

flow. The purified condensate from the steam is employed as make-up water in the cooling<br />

towers.<br />

Operating experience<br />

The adsorption system is distinguished by an extremely economical operation with a<br />

good ratio <strong>of</strong> energy consumption to toluene recovery. Solvent recovery rate is about 99.5<br />

%.<br />

22.1.5.2 Packaging printing industry<br />

In the packaging printing industry solvents like ethyl acetate, ethanol, ketones,<br />

tetrahydr<strong>of</strong>uran (THF), hexane and toluene are used in printing. The solvent laden air generally<br />

contains between 2 and 15 g/m 3 <strong>of</strong> solvent and, depending on the season, 5-18 g/m 3 <strong>of</strong><br />

water.<br />

Adsorptive recovery with steam desorption was widely used for many years but its<br />

disadvantage is that the solvents are recovered in various mixtures containing large amounts<br />

<strong>of</strong> water. The recovery <strong>of</strong> solvents is complicated because most solvents produce azeotropes<br />

with water which are not easily separated and, consequently, the waste water fails to<br />

meet the more stringent environmental regulations. In the last 10 years the adsorbent regen-

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