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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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1230 Krzyszt<strong>of</strong> M. Benczek, Joanna Kurpiewska<br />

18.2.6 VERIFICATION OF THE METHOD<br />

Emission measuring setup is given in Figure 18.2.2. Cyclohexane<br />

was pumped (with E=6.123 mg/min) into glass bottle<br />

(V=44.5 l) equipped with a fan. The air in the bottle was analyzed<br />

by gas chromatography using a flame ionization detector<br />

- OVA 118. After 20 min., when the concentration reached<br />

2.250 mg/l, the pump was stopped and the decay <strong>of</strong> concentration<br />

with time was measured.<br />

Results are given in Tables 18.2.1 and 18.2.2 (value E<br />

from the equation [18.2.2], q from the equation [18.2.4]).<br />

The standard deviation <strong>of</strong> the sample was 0.0106, <strong>of</strong> the<br />

method - 0.0102 and bias was 0.08 mg/min (1.3%).<br />

Tests were then performed in the macro-scale - emission<br />

<strong>of</strong> cyclohexane in a room, when the emission ended when the<br />

process stopped. The estimate is precise when the room vol-<br />

Figure 18.2.2. Emission measurume and ventilation flow rate are known.<br />

ing setup.<br />

The method was verified in the industrial environment in<br />

automotive plant. Here, the hazardous substances continue to<br />

be emitted to the air after the process had stopped. The concentration measured near the out-<br />

Table 18.2.1. Emission <strong>of</strong> cyclohexane<br />

t, min Ct, mg/l E, mg/min<br />

1 0.138 6.210<br />

2 0.273 6.212<br />

3 0.405 6.213<br />

4 0.533 6.201<br />

5 0.659 6.201<br />

6 0.780 6.184<br />

8 1.020 6.200<br />

10 1.250 6.212<br />

12 1.465 6.200<br />

15 1.770 6.188<br />

20 2.250 6.218<br />

E ave. - 6.203, σ n= 0.0102, σn-1= 0.0106<br />

Table 18.2.2. Ventilation flow rate<br />

t, min Ct, mg/l Q, l/min<br />

1 2.200 1.000<br />

2 2.215 1.011<br />

3 2.100 1.024<br />

4 2.055 1.008<br />

5 2.010 1.004<br />

6 1.965 0.993<br />

8 1.880 0.999<br />

10 1.800 0.992<br />

12 1.720 0.996<br />

15 1.605 1.002<br />

20 1.435 1.000<br />

q ave. = 1.0026, σn = 8.7103×10 -3 , σn-1 = 9.1354×10 -3<br />

let <strong>of</strong> exhaust was 620 mg/m 3 , and because the exhaust flow rate was known to be 50<br />

m 3 /min, the emission was precisely estimated according equation [18.2.2] as 31 g/min or<br />

312.48 kg/week. This value was comparable with the average solvent loss - 326.22<br />

kg/week.

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