Phosphate release and uptake in enhanced biological phosphorus removal from wastewater

Phosphorus removal from municipal and industrial waste waters is required to protect receiving waters from eutrophication (nutrient enrichment). Many treatment plants have been de signed or upgraded to uptake phosphorus, most often by the addition of chemicals. As an alternative, an enhanced biological phosphorus (bio-P) removal process offers the advantage of not requiring chemical additions and of reducing the volumes of sludge produced. A simple bio-P removal process must include at least two stages: non-aerated and aerated. In the first stage, influent wastewater and return sludge are combined under non aerated conditions. Phosphate release from the biomass and sol uble chemical oxygen demand (COD) removal are observed un der these anaerobic conditions in the absence of both oxygen and nitrate. In the subsequent aerated stage, phosphate removal from solution, COD removal and nitrification take place. Phos phorus-rich sludge is usually wasted from this aerobic reactor. Many processes also include an intermediate denitrification stage (often referred to as "anoxic") in which nitrified mixed liquor is recycled from the aerated reactor.

[1]  James L. Barnard,et al.  Biological nutrient removal without the addition of chemicals , 1975 .

[2]  Erik Arvin,et al.  Exchange of Organics, Phosphate and Cations between Sludge and Water in Biological Phosphorus and Nitrogen Removal Processes , 1985 .

[3]  R. Thauer,et al.  Energy Conservation in Chemotrophic Anaerobic Bacteria , 1977, Bacteriological reviews.

[4]  F. A. Koch,et al.  Oxidation-Reduction Potential – A Tool for Monitoring, Control and Optimization of Biological Nutrient Removal Systems , 1985 .

[5]  Thomas D. Brock,et al.  Biology of microorganisms , 1970 .

[6]  F. Harold Membranes and Energy Transduction in Bacteria1 1Abbreviations: Δψ, membrane potential; ΔpH, pH gradient; Δp, proton-motive force. These are related by: Δp = Δψ - (23RT/F) ΔpH ≅ Δψ - 60 ΔpH. ANS, l-anilino-8-naphthalene sulfonate; DCCD, N, N'-dicyclohexylcarbodiimide; CCCP, carbonylcyanide-m-chloroph , 1977 .

[7]  B. Rosen,et al.  Cation/proton antiport systems in Escherichia coli. , 1978, Biochemical and biophysical research communications.

[8]  A. E. Greenberg,et al.  Standard methods for the examination of water and wastewater : supplement to the sixteenth edition , 1988 .

[9]  E. Padan,et al.  How Does Escherichia coli Regulate Internal pH , 1982 .

[10]  W. K. Oldham,et al.  Excess biological phosphorus removal in the activated sludge process using primary sludge fermentation , 1986 .

[11]  G. Marais,et al.  Observations Supporting Phosphate Removal by Biological Excess Uptake – A Review , 1983 .

[12]  W. Oldham Full Scale Optimization of Biological Phosphorus Removal at Kelowna, Canada , 1985 .

[13]  R. Hancock Alterations in outer membrane permeability. , 1984, Annual review of microbiology.

[14]  I. Kulaev,et al.  Polyphosphate metabolism in micro-organisms. , 1983, Advances in microbial physiology.

[15]  D. Jenkins,et al.  Biological removal of phosphorus from wastewater , 1985 .

[16]  F. Harold Inorganic polyphosphates in biology: structure, metabolism, and function , 1966, Bacteriological reviews.

[17]  G. Ames,et al.  Membranes and Transport , 1973 .

[18]  R. Hancock,et al.  Biochemical model for enhanced biological phosphorus removal , 1986 .