TECHNICAL PAPERS
Apr 1, 2007

Combined Anaerobic/Aerobic Secondary Municipal Wastewater Treatment: Pilot-Plant Demonstration of the UASB/Aerobic Solids Contact System

Publication: Journal of Environmental Engineering
Volume 133, Issue 4

Abstract

Anaerobic pretreatment followed by aerobic posttreatment of municipal wastewater is being used more frequently. Recent investigations in this field using an anaerobic fluidized bed reactor/aerobic solids contact combination demonstrated the technical feasibility of this process. The investigation presented herein describes the use of a combined upflow anaerobic sludge bed (UASB)/aerobic solids contact system for the treatment of municipal wastewater and attempts to demonstrate the technical feasibility of using the UASB process as both a pretreatment unit and a waste activated sludge digestion system. The results indicate that the UASB reactor has a total chemical oxygen demand removal efficiency of 34%, and a total suspended solids removal efficiency of about 36%. Of the solids removed by the unit, 33% were degraded by the action of microorganisms, and 4.6% accumulated in the reactor. This low solids accumulation rate allowed operating the UASB reactor for three months without sludge wasting. The long solids retention time in this unit is comparable to the one normally used in conventional sludge digestion units, thus allowing the stabilization of the waste activated sludge returned to the UASB reactor. Particle flocculation was very poor in the UASB reactor, and therefore, it required postaeration periods of at least 100min to proceed successfully in the aerobic unit. Polymer generation, which is necessary for efficient biological flocculation, was practically nonexistent in the anaerobic unit; therefore, it was necessary to maintain dissolved oxygen levels greater than 1.5mgL in the aerobic solids contact chamber for polymer generation to proceed at optimum levels. Once these conditions were attained, the quality of the settled solids contact chamber effluent always met the 30mg BOD/L, 30mg SS/L secondary effluent guidelines.

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Acknowledgments

Financial support for the research reported herein was provided by the University of New Orleans Schlieder Urban Environmental Systems Center through a grant from the U.S. Environmental Protection Agency, and by the Jefferson Parish Department of Sewerage.

References

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Information

Published In

Go to Journal of Environmental Engineering
Journal of Environmental Engineering
Volume 133Issue 4April 2007
Pages: 397 - 403

History

Received: Jun 24, 2005
Accepted: Aug 28, 2006
Published online: Apr 1, 2007
Published in print: Apr 2007

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Authors

Affiliations

Enrique J. La Motta
Professor, Dept. of Civil and Environmental Engineering, Univ. of New Orleans, New Orleans, LA 70148.
Eudomar Silva
Associate Engineer, MWH Americas Inc., Metairie, LA 70002.
Adriana Bustillos
Engineer III, Camp, Dresser and McKee, Inc., Miami, FL 33131.
Harold Padrón
Engineer II, Brown and Caldwell, New Orleans, LA 70113.
Jackeline Luque
Engineer II, Brown and Caldwell, New Orleans, LA 70113.

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