OBJECTIVE ο· ο·
To determine the effects of operating parameters on the efficiency of venturi scrubber. To determine the effect of liquid to gas ratio (L/G) separation efficiency.
RESULTS Water Flow Rate (LPM)
DPT03 (in H2O)
Weight Loaded, M1 (g)
Weight Retained, M2 (g)
6 8 10 13
3.625 3.625 3.625 3.625
200 200 200 200
128 158 181 159
Efficiency of Venturi Scrubber (%) 64.0 79.0 90.5 79.5
Sample Calculation:
DPT03 value = ππππ π ( βπ =
π΄1 2 β 1) π΄2 2 2 2
=
ππ π 2 0.001810π2 (10 π ) Γ 1.2 3 Γ [( ) β 1] π 0.000452π2 2 = 3.625 ππ π»2 π
Γ
0.00401865 ππ π»2 π 1 ππ
Efficiency Venturi Scrubber (K. S. Agrawal, 2007) : =
π€πππβπ‘ πππ‘πππππ ππ πππππ£ππ ππππ‘πππ’πππ‘π (π) Γ 100% πππππ‘ π€πππβπ‘ ππ ππππ‘πππ’πππ‘π πππ‘π‘ππ (π)
For 6 LPM 128 Γ 100% = 64% 200 For 8 LPM 158 Γ 100% = 79% 200 For 10 LPM 181 Γ 100% = 90.5% 200 For 13 LPM 159 Γ 100% = 79.5% 200
Liquid to Gas Ratio :
Conversion 1 LPM = 0.2641712 GPM Area of separation chamber (Education, E., n.d.) = 0.6 m Γ 2 m = 1.2 m2
For 6 LPM πππ 0.2641712 πππ 3.78 πΏ Γ πΏ 6 πΏππ Γ 1 π3 1 1 πΏππ 1 πππ = Γ Γ π 60 π πΊ 1000 πΏ 1.2π2 10 π Γ 1 πππ = 8.321 Γ 10β6
For 8 LPM πππ 0.2641712 πππ 3.78 πΏ Γ πΏ 8 πΏππ Γ 1 π3 1 1 πΏππ 1 πππ = Γ Γ π 60 π πΊ 1000 πΏ 1.2π2 10 π Γ 1 πππ = 1.11 Γ 10β5
For 10 LPM πππ 0.2641712 3.78 πΏ πππ Γ πΏ 10 πΏππ Γ 1 π3 1 1 πΏππ 1 πππ = Γ Γ π 60 π πΊ 1000 πΏ 1.2π2 10 π Γ 1 πππ = 1.387 Γ 10β5
For 13 LPM πππ 0.2641712 πππ 3.78 πΏ Γ πΏ 13 πΏππ Γ 1 π3 1 1 πΏππ 1 πππ = Γ Γ π 60 π πΊ 1000 πΏ 1.2π2 10 π Γ 1 πππ = 1.803 Γ 10β5
100 90
Collection Efficiency, %
80 70 60
50 40 30 20 10 0 0
0.000005
0.00001
0.000015
Liquid to Gas Ratio
Figure 1 Effect of L/G Ratio to Efficiency of Venturi Scrubber
0.00002
Reference 1. K. S. Agrawal, 2007. Performancce of Venturi Scrubber, 3. 2. Education, E., n.d. Model: AP 02