Abstract
Problem statement: The use of aerobic biological methods for the treatment of livestock wastes has resulted in a proliferation of mechanical aeration devices to accomplish the desired treatment. The oxidation ditch system with disc aerators is among the aerobic systems that have been used to treat livestock waste. The main objectives of this study were to investigate the effects of various disc design parameters and system operational parameters on the oxygen transfer coefficient and to study the physical phenomenon of oxygen transfer using high speed movie techniques. Approach: A bench-scale oxidation ditch with a disc aerator was used to conduct a series of experiments to determine the effects of immersion depth (2.5-7.5 cm), disc speed (50-250 rpm), disc thickness (0.32-2.55 cm), hole diameter (0.00-1.92 cm) and number of rotating discs (1-2) on the oxygen transfer coefficient. The unsteady state method with sodium sulfite oxidation was used to deoxygenate the water and the dissolved oxygen concentration was measured with time. Results: The disc speed had the most significant effect on KLa with the immersion depth and hole diameter both showing strong effects and the disc thickness showing less effect. The effect of adding a second disc was comparable to using a single disc of double the thickness at lower speeds while at speeds higher than 200 rpm doubling the thickness of a single disc had less effect than a second disc. Conclusion: The highest oxygen transfer (1.526 min-1) was achieved using two coaxial discs with a disc speed of 250 rpm, a disc thickness of 0.64 cm, a hole diameter of 1.92 cm and an immersion depth of 7.5 cm. Bubble aeration and eddy aeration were the most prevalent mechanisms of oxygen transfer in the oxidation ditch while surface aeration played a relatively small role in oxygen transfer.
Highlights
At the least cost per kilogram of waste treated
The ditch essentially consists of a closed loop, open channel in which liquid circulation and oxygen input are maintained by a mechanical device such as paddle, brush, or disc aerators
The immersion depth of 7.5 cm was maintained throughout these experiments
Summary
At the least cost per kilogram of waste treated. The oxidation ditch system has been successfully used for. Experimental design: Three independent disc design variables (disc thickness, hole diameter and number of holes) and two operational variables (disc immersion depth, disc rotational speed and number of coaxially mounted discs) were considered for optimization of the oxygenation capacity of the system. When the saturation concentration (Cs) was reached (the oxygen concentration curve became flat), the aerator motor was switched off and 13.8 ml of 0.10 M Na2SO3 solution (173.8 mg sodium sulfite) and 1.6 ml of 0.01 M CoCl2·6H2O solution (2.2 mg cobalt chloride) were added These solutions were distributed throughout the oxidation ditch by the impeller. This left KLa exclusively a function of the design parameters of the disc aerator in the oxidation ditch
Published Version (Free)
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have