Phosphorus removal in wastewater treatment is crucial for preventing eutrophication in water bodies. Two main methods are used: biological and chemical removal. Biological removal uses special bacteria to store phosphorus, while chemical removal adds metal salts to form insoluble precipitates.
The biological method, called , relies on . These bacteria store phosphorus under specific conditions. Chemical removal involves adding metal salts like or aluminum sulfate to create phosphate precipitates that can be filtered out.
Biological and Chemical Phosphorus Removal
Mechanisms of phosphorus removal
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Top images from around the web for Mechanisms of phosphorus removal
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A comparative study of microbial dynamics and phosphorus removal for a two side-stream ... View original
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Biological phosphorus removal
Enhanced biological phosphorus removal (EBPR) process alternates between anaerobic and aerobic conditions to promote the growth of phosphorus accumulating organisms (PAOs)
During the anaerobic phase, PAOs uptake and store them as while releasing phosphorus
In the aerobic phase, PAOs use the stored PHAs as an energy source to uptake and store large amounts of phosphorus as granules
Phosphorus is ultimately removed from the system through the process, which discards excess bacterial biomass containing the stored polyphosphate
Chemical phosphorus removal
Involves the addition of metal salts, such as ferric chloride (FeCl3) or aluminum sulfate (, Al2(SO4)3), to the wastewater
Metal ions react with soluble phosphorus species to form (e.g., FePO4, AlPO4)
Precipitates are removed from the wastewater through in clarifiers and subsequent processes
Chemical phosphorus removal can be implemented as a standalone treatment or in conjunction with biological processes to enhance overall phosphorus
Microorganisms in EBPR
Phosphorus accumulating organisms (PAOs)
Key microorganisms responsible for the enhanced biological phosphorus removal process
Possess the unique ability to store large amounts of polyphosphate within their cells, typically in the form of intracellular granules
During the anaerobic phase, PAOs uptake volatile fatty acids (VFAs) and store them as poly-β-hydroxyalkanoates (PHAs) while simultaneously releasing phosphorus
In the subsequent aerobic phase, PAOs utilize the stored PHAs as an energy source to uptake and store phosphorus, replenishing their polyphosphate reserves
Compete with PAOs for volatile fatty acids (VFAs) during the anaerobic phase of the EBPR process
Unlike PAOs, GAOs do not contribute to phosphorus removal as they lack the ability to store polyphosphate
The presence of GAOs in significant numbers can reduce the overall efficiency of the EBPR process by consuming VFAs that would otherwise be available for PAOs
Factors affecting EBPR performance
Carbon source availability
Sufficient volatile fatty acids (VFAs) must be present during the anaerobic phase for PAOs to uptake and store them as poly-β-hydroxyalkanoates (PHAs)
A lack of readily biodegradable carbon sources (e.g., acetate, propionate) can limit the performance of the EBPR process by restricting PHA storage in PAOs
Anaerobic and aerobic conditions
Strict anaerobic conditions must be maintained during the anaerobic phase to promote VFA uptake and PHA storage by PAOs
The presence of nitrate or oxygen can disrupt the anaerobic environment and hinder the selective advantage of PAOs
Adequate aerobic conditions are necessary during the aerobic phase for PAOs to efficiently uptake phosphorus and replenish their polyphosphate reserves
Insufficient aerobic retention time can limit the amount of phosphorus removed by PAOs
Competing microbial populations
The presence of glycogen accumulating organisms (GAOs) can reduce the amount of VFAs available for PAOs, thereby limiting EBPR performance
Nitrate or oxygen intrusion during the anaerobic phase can favor the growth of denitrifying bacteria, which compete with PAOs for carbon sources and can diminish EBPR efficiency
Chemical vs biological phosphorus removal
Metal salt addition
Common metal salts used for chemical phosphorus removal include ferric chloride (FeCl3), aluminum sulfate (alum, Al2(SO4)3), and calcium hydroxide (lime, Ca(OH)2)
Metal salts can be added at various points in the wastewater treatment process, such as the primary , secondary clarifier, or as part of a tertiary treatment step
Factors affecting the performance of chemical phosphorus removal include pH, alkalinity, and the presence of competing ions (e.g., carbonate, sulfate)
Integration with biological processes
can be employed as a standalone treatment or in combination with biological phosphorus removal processes like EBPR
Chemical addition to the secondary clarifier can provide additional phosphorus removal capacity and serve as a "backup" for EBPR during periods of reduced biological performance
Simultaneous precipitation involves adding metal salts directly to the aeration basin, allowing for concurrent biological and chemical phosphorus removal within the same reactor