Abstract

When designing wastewater aeration systems, fine-pore diffusers are typically selected for their potential energy efficiency. Because aeration is one of the most energy-intensive unit operations during treatment, the accurate quantification of aeration performance parameters is crucial to minimize the process energy footprint. Oxygen transfer efficiency in process water is the key design parameter; however, performance indicators that account for fouling and increased pressure drop with time must be considered. Both fouling and pressure drop increase cause an increase in blower power requirements. This paper presents a new approach to improve this design procedure, without altering the technical structure of the classical approach. Although the administrative and bidding milestones are underway (i.e., in the first few months of the project), an independent aeration team can test candidate diffusers suitable for design in an in situ aeration column. Subsequently, an extended fouling test in the plant’s wastewater can be carried out within the design timing, providing the designers with site-specific aeration performance data. This methodology improves the accuracy of the design process and increases overall energy savings.

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Acknowledgments

The authors gratefully thank the diffuser manufacturers and the treatment plants that participated in this study. Also, the authors thank Derek Nguyen, Keith Gellerman, and Maani Firouzian for the help during the experiments. The authors deeply thank the team lead by Rudy Limburg, late manager of the Biological Sciences Machine Shop at the University of California, Irvine, for the invaluable help constructing the testing tank. Finally, the authors thank Elias Bordcosh, late facilities manager of the UCI Henri Samueli School of Engineering, for his precious help during testing setup.

References

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Information

Published In

Go to Journal of Environmental Engineering
Journal of Environmental Engineering
Volume 139Issue 4April 2013
Pages: 530 - 537

History

Received: Mar 14, 2011
Accepted: Jul 26, 2012
Published online: Aug 3, 2012
Published in print: Apr 1, 2013

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Authors

Affiliations

Diego Rosso [email protected]
Assistant Professor, Dept. of Civil and Environmental Engineering, Univ. of California, Irvine, CA 92697-2175 (corresponding author). E-mail: [email protected]
Lu-Man Jiang [email protected]
Ph.D. Candidate, Dept. of Civil and Environmental Engineering, Univ. of California, Irvine, CA 92697-2175. E-mail: [email protected]
P.E.
Vice President, Hazen and Sawyer, P.C., 498 7th Ave., New York, NY 10018. E-mail: [email protected]
Charles S. Hocking [email protected]
P.E.
Vice President, Hazen and Sawyer, P.C., 498 7th Ave., New York, NY 10018. E-mail: [email protected]
Michael K. Stenstrom [email protected]
P.E.
F.ASCE
Distinguished Professor, Dept. of Civil and Environmental Engineering, Univ. of California, Los Angeles, CA 90095-1593. E-mail: [email protected]
Sudhir Murthy [email protected]
P.E.
Manager, Process Development and Optimization, Dept. of Wastewater Treatment, DC WATER, 5000 Overlook Ave. SW, Washington, DC 20032. E-mail: [email protected]
David M. Hayden [email protected]
Plant Operations Supervisor, Irvine Ranch Water District, 3512 Michelson Dr., Irvine, CA 92612-1799. E-mail: [email protected]
Joseph Zhong [email protected]
M.S. Student, Dept. of Chemical Engineering and Materials Science, Univ. of California, Irvine, CA 92617-2575. E-mail: [email protected]
Daniel H. Coller [email protected]
M.S. Student, Dept. of Chemical Engineering, Univ. of California, Santa Barbara, CA, 93106-5080. E-mail: [email protected]
Andrew Y. Kim [email protected]
M.S. Student, Dept. of Chemical Engineering and Materials Science, Univ. of California, Irvine, CA 92617-2575. E-mail: [email protected]
M.S. Student, Dept. of Petroleum and Geosystems Engineering, Univ. of Texas, Austin, TX 78712. E-mail: [email protected]

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