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Absorption of Oxygen in Water in a Packed Colum

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1 Absorption of Oxygen in Water in a Packed Colum
Kelly Yates Quintin Picard 4/30/15

2 Experimental Setup Packing increases area in column
Testing effects of: Water flow rate (100, 150, 200 L/h) Pressure (1, 1.25, 1.5 bar) Gas flow rate (25, 37, 50 L/min) Set up a 33 factorial design

3 Equations General Mass Transfer lnโก( ๐‘ ๐‘Ž โˆ’ ๐‘ 0 ๐‘ ๐‘Ž โˆ’ ๐‘ ๐‘™ ) ๐พ ๐‘™ = ๐‘ ๐‘Ž
Sherwood-Holloway Correlation ๐พ ๐‘™ ๐‘Ž ๐ท ๐ด๐ต =๐›ผ ( ๐ฟ ๐œ‡ ) .8 ( ๐œ‡ ๐‘ ๐ท ๐ด๐ต ) 1/2 Wilke Chang Correlation ๐ท ๐ด๐ต = 1.173โˆ— 10 โˆ’16 (๐œ‘๐‘€) 1/2 ๐‘‡ ๐œ‡ ๐‘‰ .6 ฯ•= association parameter Rate Rate=๐น๐‘™๐‘ข๐‘ฅโˆ—๐ด๐‘Ÿ๐‘’๐‘Ž Henryโ€™s Law ๐‘ƒ ๐‘ ๐‘Ž๐‘ก =๐ป๐‘ฅ Resistance 1 ๐พ ๐‘™ = 1 ๐ป ๐‘˜ ๐‘” ๐‘˜ ๐‘™

4 Flux Theory Henryโ€™s constant for oxygen: 44253 bar
Pressure Gas Flow Rate Water Flow Rate Henryโ€™s constant for oxygen: bar Liquid side controls mass transfer

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8 ANOVA and Propagation of Error
At a 95% confidence limit Only water flow is significant At 80% confidence limit Pressure is significant Milwaukee MW 600: ยฑ1% accuracy Pressure gauge: ยฑ3% accuracy Rotameter: ยฑ5% accuracy ln ๐‘ ๐‘Ž โˆ’ ๐‘ 0 ๐‘ ๐‘Ž โˆ’ ๐‘ ๐‘™ ๐พ ๐‘™ = ๐‘ ๐‘Ž 9% Uncertainty ๐พ ๐‘™ ๐‘Ž ๐ท ๐ด๐ต =๐›ผ ๐ฟ ๐œ‡ .8 ( ๐œ‡ ๐‘ ๐ท ๐ด๐ต ) 1 2 5 % Uncertainty ๐‘ƒ ๐‘ ๐‘Ž๐‘ก =๐ป๐‘ฅ 3% Uncertainty

9 Scale Up Design 1 million gallon tank House 50 40kg sharks
Sharks requires 800 g/hour of O2 minimum Scale up by 25% to ensure adequate levels 1 million gallons = 3785 m3 keyword: aquarium sharks 20 m 12 m Pressure at bottom of tank is 1.18 bar

10 Final Column Design From ANOVA: use high pressure and high water flow rate P = 1.5 bar and Water Flow Rate = ? Area = ? Went with actual values over predicted ๐พ ๐‘™ =.0036 ๐‘š ๐‘  ๐‘™๐‘› ๐‘ ๐‘Ž โˆ’ ๐‘ ๐‘™๐‘œ ๐‘ ๐‘Ž โˆ’ ๐‘ ๐‘™๐‘“ =.473 ๐‘š๐‘œ๐‘™ ๐‘š 3 Area of 5.58 m2 - diameter of 2.67 m (ยฑ .11 m) Volumetric flow rate of 62 L/s N= ๐พ ๐‘™ lnโก( ๐‘ ๐‘Ž โˆ’ ๐‘ ๐‘™๐‘œ ๐‘ ๐‘Ž โˆ’ ๐‘ ๐‘™๐‘“ ) ๐‘…๐‘Ž๐‘ก๐‘’ ๐ด๐‘Ÿ๐‘’๐‘Ž = ๐พ ๐‘™ ๐‘™๐‘›( ๐‘ ๐‘Ž โˆ’ ๐‘ ๐‘™๐‘œ ๐‘ ๐‘Ž โˆ’ ๐‘ ๐‘™๐‘“ )

11 What About Temperature?
Wilke-Chang Method to account for change in diffusivity with temperature ๐ท ๐ด๐ต = 1.173โˆ— 10 โˆ’16 (๐œ‘๐‘€) 1/2 ๐‘‡ ๐œ‡ ๐‘‰ ฯ•= 2.6 for water ๐ท ๐ด๐ต =1.11โˆ— 10 โˆ’9 ๐‘š 2 ๐‘  Account for evaporation with rise in temperature so increase rate to g/h Calculate required flow rate with diameter of column and same concentration gradient Need 80.2 L/s Using Wilke-Chang Kl value becomes .004 m/s and the flow rate is L/s

12 Appendix: ANOVA

13 Appendix: Raw Data Water Pressure O2 Conc. Start O2 Conc. Final (mg/L)
Flux (mol)/(m^2*s) Rate (g/s) 5.56E-05 1.5 1.2 5.7


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