The Biochemistry of Enhanced Phosphorus Removal by Activated Sludge

1985 ◽  
Vol 17 (11-12) ◽  
pp. 303-304 ◽  
Author(s):  
J. B. Heymann

The design and operation of an activated sludge plant which aims to achieve maximum phosphorus removal should be based on sound biochemical principles. This poster presents the biochemical reactions believed to be responsible for observed variations in the concentration of different phosphorus species in such plants. Excess phosphorus removed in the aerated stage of plant configurations such as the Phoredox process (i.e. more than is necessary for sludge metabolism) is accumulated in the sludge in the form of polyphosphate. The most likely major function of this compound is to supply energy for active membrane transport of specific carbon sources into the cells in the anaerobic stage, acetate being one such compound. The energy for this process is derived from the hydrolysis of polyphosphate to orthophosphate which is then released into the medium around the cells. Five possible mechanisms are proposed to describe this process. From the microbial viewpoint the main advantage of active membrane transport is the high rate at which compounds transported becomes available inside the cell. In the absence of a terminal electron acceptor such as oxygen or nitrate, carbon compounds absorbed cannot be oxidized. Accumulation as such would inhibit further absorption and may lead to disturbance of intracellular conditions. Absorbed material is therefore converted to a reserve to be stored for later use. Indications are that sewage feed composition favours the formation of one reserve compound: poly-β-hydroxybutyrate (PHB). In the presence of oxygen, the cell is able to oxidise PHB at a high rate relative to other reserves such as glycogen and triglycerides. The energy produced in this way is far in excess of what the cell needs for normal metabolism and results in an ‘over-production' of adenosine triphosphate (ATP) far in excess of that needed for biosynthesis. In its role as energy carrier, ATP formed due to the oxidation of PHB cannot be accumulated. Instead, to control the ATP:ADP ratio (ADP = adenosine diphosphate) in the cell, the energy is transferred from ATP to polyphosphate by polyphosphate kinase. When the sludge is recirculated to the anaerobic stage, some of this polyphosphate is used for active membrane transport. The success of excess phosphorus removal by activated sludge revolves firstly around the degree of PHB formation in the anaerobic stage. Any chemical or physical agent inhibiting this process would reduce the extent of phosphorus removal. The second important factor is the extent of ATP ‘over-production' which is mainly determined by biosynthetic activities. An increase in biosynthesis of structural cell components would lead to a higher rate of ATP utilization for energy and thus decrease polyphosphate formation. These are the central concepts on which enhanced phosphorus removal in activated sludge plants should be based. It seems that phosphorus removal in the Phoredox process represents an interplay between structural cell biosynthesis and reserve material synthesis. The organic compounds in the sewage feed play a decisive role in determining the set of processes which is going to occur. It is hypothesized that compounds needed in the biosynthesis of cell material would result in the so-called ‘normal' phosphorus removal, while substances with high energy content and lower biosynthetic value would favour ‘excess' phosphorus removal. The building blocks of cell material usually contain high amounts of nitrogen (such as proteins and nucleic acids) while the compounds usually associated with high energy content contain very little nitrogen (such as carbohydrates and lipids). This concept is reflected in the importance and value attached to the COD:TKN ratio, which roughly approximates the ratio of non-nitrogen containing compounds to nitrogen-rich compounds. In view of the above-mentioned ideas, this parameter can be refined to the following proposed ratio: In the formulation of these concepts, conventional biochemical principles were applied to old and new observations in a relatively new field. However, very little quantitative information regarding the validity of these hypotheses are available and care should be taken not to see these as the final answer.

1990 ◽  
Vol 22 (7-8) ◽  
pp. 21-33 ◽  
Author(s):  
Clifford W. Randall ◽  
David Waltrip ◽  
Milind V. Wable

A full-scale activated sludge plant was modified for high-rate BNR operation at minimal cost. Three different processes (A/0+, A2/0+ and UCT) were studied at BSRTs varying from 4 to 14 days and HRTs of 2 to 6 hours. Onset of BPR was almost immediate without addition of special seed. Good phosphorus removal was obtained with all three processes except for periods of extremely high influent flows or high nitrate recycle to the anaerobic zone. However, because of high process phosphorus loadings resulting from high influent concentrations and sludge processing recycles, effluent TP concentrations were typically in excess of 2 mg/L. Nitrogen removal was excellent when nitrification could be maintained and nitrate recycle was sufficiently high. All processes yielded excellent nitrogen removals during warm weather, but complete nitrification could not be maintained during winter conditions. Implementation of a statewide phosphate detergent ban resulted in a 40 per cent decrease in the influent wastewater concentrations. Following the ban, the UCT process was shown to be capable of consistently meeting the Virginia nutrient discharge standards of 10 mg/L TN and 2 mg/L TP during the growing season.


Author(s):  
James Barber

AbstractThe biological energy cycle of our planet is driven by photosynthesis whereby sunlight is absorbed by chlorophyll and other accessory pigments. The excitation energy is then efficiently transferred to a reaction centre where charge separation occurs in a few picoseconds. In the case of photosystem II (PSII), the energy of the charge transfer state is used to split water into oxygen and reducing equivalents. This is accomplished by the relatively low energy content of four photons of visible light. PSII is a large multi-subunit membrane protein complex embedded in the lipid environment of the thylakoid membranes of plants, algae and cyanobacteria. Four high energy electrons, together with four protons (4H+), are used to reduce plastoquinone (PQ), the terminal electron acceptor of PSII, to plastoquinol (PQH2). PQH2 passes its reducing equivalents to an electron transfer chain which feeds into photosystem I (PSI) where they gain additional reducing potential from a second light reaction which is necessary to drive CO2 reduction. The catalytic centre of PSII consists of a cluster of four Mn ions and a Ca2+ linked by oxo bonds. In addition, there are seven amino acid ligands. In this Article, I discuss the structure of this metal cluster, its stability and the probability that an acid-base (nucleophilic-electrophilic) mechanism catalyses the water splitting reaction on the surface of the metal-cluster. Evidence for this mechanism is presented from studies on water splitting catalysts consisting of organo-complexes of ruthenium and manganese and also by comparison with the enzymology of carbon monoxide dehydrogenase (CODH). Finally the relevance of our understanding of PSII is discussed in terms of artificial photosynthesis with emphasis on inorganic water splitting catalysts as oxygen generating photoelectrodes.


1990 ◽  
Vol 22 (7-8) ◽  
pp. 131-138
Author(s):  
Ahmed Fadel

Many of Egypt's cities have existing treatment plants under operation that have been constructed before 1970. Almost all of these treatment plants now need rehabilitation and upgrading to extend their services for a longer period. One of these plants is the Beni Suef City Wastewater Treatment Plant. The Beni Suef WWTP was constructed in 1956. It has primary treatment followed by secondary treatment employing intermediate rate trickling filters. The BOD, COD, and SS concentration levels are relatively high. They are approximately 800, 1100, and 600 mg/litre, respectively. The Beni Suef city required the determination of the level of work needed for the rehabilitation and upgrading of the existing 200 l/s plant and to extend its capacity to 440 l/s at year 2000 A description of the existing units, their deficiencies and operation problems, and the required rehabilitation are presented and discussed in this paper. Major problems facing the upgrading were the lack of space for expansion and the shortage of funds. It was, therefore, necessary to study several alternative solutions and methods of treatment. The choice of alternatives was from one of the following schemes: a) changing the filter medium, its mode of operation and increasing the number of units, b) changing the trickling filter to high rate and combining it with the activated sludge process, for operation by one of several possible combinations such as: trickling filter-solids contact, roughing filter-activated sludge, and trickling filter-activated sludge process, c) dividing the flow into two parts, the first part to be treated using the existing system and the second part to be treated by activated sludge process, and d) expanding the existing system by increasing the numbers of the different process units. The selection of the alternative was based on technical, operational and economic evaluations. The different alternatives were compared on the basis of system costs, shock load handling, treatment plant operation and predicted effluent quality. The flow schemes for the alternatives are presented. The methodology of selecting the best alternative is discussed. From the study it was concluded that the first alternative is the most reliable from the point of view of costs, handling shock load, and operation.


1990 ◽  
Vol 22 (7-8) ◽  
pp. 35-43
Author(s):  
K. D. Tracy ◽  
S. N. Hong

The anaerobic selector of the A/0™ process offers many advantages over conventional activated sludge processes with respect to process performance and operational stability. This high-rate, single-sludge process has been successfully demonstrated in full-scale operations for biological phosphorus removal and total nitrogen control in addition to BOD and TSS removal. This process can be easily utilized in upgrading existing treatment plants to meet stringent discharge limitations and to provide capacity expansion. Upgrades of two full-scale installations are described and performance data from the two facilities are presented.


1994 ◽  
Vol 30 (6) ◽  
pp. 31-40 ◽  
Author(s):  
Hiroyshi Emori ◽  
Hiroki Nakamura ◽  
Tatsuo Sumino ◽  
Tadashi Takeshima ◽  
Katsuzo Motegi ◽  
...  

For the sewage treatment plants near rivers and closed water bodies in urbanized areas in Japan and European countries, there is a growing demand for introduction of advanced treatment processes for nitrogen and phosphorus from the viewpoints of water quality conservation and environmental protection. In order to remove nitrogen by the conventional biological treatment techniques, it is necessary to make a substantial expansion of the facility as compared with the conventional activated sludge process. In such urbanized districts, it is difficult to secure a site and much capital is required to expand the existing treatment plant. To solve these problems, a compact single sludge pre-denitrification process using immobilized nitrifiers was developed. Dosing the pellets, which are suitable for nitrifiers growth and physically durable, into the nitrification tank of single sludge pre-denitrification process made it possible to perform simultaneous removal of BOD and nitrogen in a retention time equal to that in the conventional activated sludge process even at the low water temperature of about 10 °C. The 3,000 m3/d full-scale conventional activated sludge plant was retrofitted and has been successfully operated.


2017 ◽  
Vol 14 (2) ◽  
pp. 99-106 ◽  
Author(s):  
Zhengan Zhang ◽  
Shulin Pan ◽  
Fei Huang ◽  
Xiang Li ◽  
Juanfang Shang ◽  
...  

2017 ◽  
Vol 2017 (3) ◽  
pp. 47-52
Author(s):  
Xiaocen Liu ◽  
Tim Van Winckel ◽  
Birthe V Kjellerup ◽  
Imre Tacaks ◽  
Belinda Sturm ◽  
...  

2000 ◽  
Vol 41 (9) ◽  
pp. 139-145
Author(s):  
R. Kayser

The German design guideline A 131 “Design of single stage activated sludge plants” was amended in 1999. The main changes of the guideline from 1991 are outlined. The design procedure for plants with nitrogen and phosphorus removal is presented.


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