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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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18.2 Prediction <strong>of</strong> organic solvents emission 1231<br />

18.2.7 RELATIONSHIPS BETWEEN EMISSION AND TECHNOLOGICAL<br />

PARAMETERS<br />

Emission <strong>of</strong> solvents depends on the evaporation rate <strong>of</strong> the solvent in the process. The<br />

evaporation rate from the surface depends on the concentration in the layer on the surface<br />

and the coefficient <strong>of</strong> mass transfer on the air-side. This relation is approximately true for<br />

degreasing operations using both liquid and vapors <strong>of</strong> organic solvents.<br />

The concentration <strong>of</strong> solvent in a saturated vapor layer depends on temperature and<br />

vapor pressure. The coefficient <strong>of</strong> mass transfer on the air-side depends on the air velocity in<br />

the layer on the surface and Schmidt�s number (includes dynamic vapor viscosity, vapor<br />

density, and diffusion coefficient). Emissions are measured in mass unit per unit <strong>of</strong> time and<br />

the amount depends on surface area and the rate <strong>of</strong> evaporation, which, in turn, depends on<br />

temperature, air velocity over the surface <strong>of</strong> solvent and the mass <strong>of</strong> solvent carried out on<br />

the wetted parts which have been degreased.<br />

18.2.7.1 Laboratory test stand<br />

A thin-metal, flat dish 6 cm in diameter was filled with solvent up to 2-3 mm from the upper<br />

edge and placed on a laboratory balance (Figure 18.2.3). The amount <strong>of</strong> evaporated solvent<br />

was measured with (precision 0.1 mg) as the difference between the mass <strong>of</strong> the dish and<br />

solvent at the start <strong>of</strong> the test and the mass <strong>of</strong> the dish with solvent after pre-determined period<br />

<strong>of</strong> time. The test was repeated under different conditions <strong>of</strong> temperature and air velocity<br />

near the surface <strong>of</strong> the solvent. The results were reported as the evaporated mass per 1<br />

minute.<br />

18.2.7.2 The influence <strong>of</strong> temperature on emission<br />

Temperature was measured with a mercury thermometer with a range from 0 to 30 o C. Air<br />

velocity was 0.3 to 0.4 m/s in this temperature region. The relationship is linear and the<br />

equations expressing emission [g/m 3 /h] relative to temperature [ o C] for different solvents<br />

are:<br />

trichloroethylene E= 63.6 × t + 699.6<br />

naphtha solvent E= 9.3 × t + 4.9<br />

naphtha anti-corrosive E= 0.55 × t + 5.65<br />

1-butanol E= 6.29 × t + 16.9<br />

1,1,1- trichloroethane E= 94.7 × t + 805.6<br />

extraction naphtha E= 49.5 × t + 1147<br />

petroleum(mineral) spirits E= 11.9 × t + 76.7<br />

wood preservatives E= 2.0 × t+42<br />

Figure 18.2.3. Test laboratory stand.

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