stimate the total volumetric flow rate gas and the total mass emission rate of the particles in Fig 4.3.

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Estimate the total volumetric flow rate gas and the total mass emission rate of the particles in Fig 4.3.

Gas velocity
Emission
Gas velocity
Emission
1.2 1.2 1.2 1.2
1.3 1.3 1.3 1.3
1.3 1.3 1.3 1.3
0.2 0.2 0.2 0.2
1.1 1.1 1.2 1.9
0.9 1.2 1.6 1.8
0.9 0.9 1.3 1.7
0.1 0.1 0.1 0.1
1.1 1.1 1.1 1.1
1.1 1.0
1.0 0.9
1.1 0.7 0.8 1.0
1.1 0.8 0.9 1.4
1.0 0.7 1.0 1.0
0.9 0.9 1.2 1.5
1.1 1.2
1.0 1.1
0.8 0.6 0.9 0.9
8'-0"-
6'-0"
To main flue
2'-0"
36'-0"
Average gas velocity = 39 f/s
Average emission per unit area =
1.2 lb/ft2-hr
From No. 2
From No. 1
I.D. fan
I.D. fan
FIGURE 4.3
Measured velocities and particle mass flow rates (velocity concentration) in a complex duct. The values
shown are the ratio of the observed value to the average value for the whole duct. For example, near the bend,
where the velocity is shown as 1.2, the measured velocity was 1.2 - 39 f/s = 47 f/s = 14.3 m/s [2].
Transcribed Image Text:Gas velocity Emission Gas velocity Emission 1.2 1.2 1.2 1.2 1.3 1.3 1.3 1.3 1.3 1.3 1.3 1.3 0.2 0.2 0.2 0.2 1.1 1.1 1.2 1.9 0.9 1.2 1.6 1.8 0.9 0.9 1.3 1.7 0.1 0.1 0.1 0.1 1.1 1.1 1.1 1.1 1.1 1.0 1.0 0.9 1.1 0.7 0.8 1.0 1.1 0.8 0.9 1.4 1.0 0.7 1.0 1.0 0.9 0.9 1.2 1.5 1.1 1.2 1.0 1.1 0.8 0.6 0.9 0.9 8'-0"- 6'-0" To main flue 2'-0" 36'-0" Average gas velocity = 39 f/s Average emission per unit area = 1.2 lb/ft2-hr From No. 2 From No. 1 I.D. fan I.D. fan FIGURE 4.3 Measured velocities and particle mass flow rates (velocity concentration) in a complex duct. The values shown are the ratio of the observed value to the average value for the whole duct. For example, near the bend, where the velocity is shown as 1.2, the measured velocity was 1.2 - 39 f/s = 47 f/s = 14.3 m/s [2].
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Given data:

At section 1 and section 2, the measured velocities and particle flow rates are as follows:

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