SOLUBLE PHOSPHATE REMOVAL IN THE ACTIVATED SLUDGE PROCESS

Author(s):  
DAVID A. LONG ◽  
JOHN B. NESBITT ◽  
R. RUPERT KOUNTZ
1973 ◽  
Vol 7 (1-2) ◽  
pp. 321-324 ◽  
Author(s):  
David A. Long ◽  
John B. Nesbitt ◽  
R.Rupert Kountz

1985 ◽  
Vol 17 (11-12) ◽  
pp. 301-302 ◽  
Author(s):  
D. A. Kerdachi ◽  
M. R. Roberts

The principal results of many years of study of the removal of nutrients from municipal wastewater by a full-scale mainstream activated sludge process (capable of 95% removal of C, N and P without chemical dosing) indicate that anaerobic zones have two important functions, the second of which has not been reported previously in wastewater research publications:(1)  Anaerobic zones provide ideal conditions for uptake of organic carbon and release of phosphate by Acinetobacter which accounted for about 50% of the heterotrophic organisms in the plant as determined by the API system.(2)  Anaerobic zones also provide ideal conditions for reduction of influent ferric iron to ferrous iron and subsequent precipitation and adsorption of mixed metallic phosphates; such as a colloidal modification of ferrous calcium phosphate (1;0,4:1 molar) which forms in the pH range 6 to 7,5. It was found that anaerobic retention times of short duration were sufficient to stimulate subsequent uptake of soluble phosphate by Acinetobacter in aerobic zones. However, much longer anaerobic retention times were necessary to lower the redox pote ntial sufficiently to reduce bound iron in the ferric state to ferrous ions which were identified in significant quantities in the sludge by using cold PCA fractionation procedures in conjunction with bathophenanthroline. The partial transfer in anaerobic zones of phosphate, from intracellular polyphosphate in vivo to extracellularly adsorbed metallic phosphates in vitro, was found to be essential for truly enhanced removal of phosphate by this mainstream process which always removed more than 95% of the nitrogen from the municipal wastewater. A further finding of significance was the limited phosphate storage capacity of Acinetobacter. Metabolic phosphate, excess biological uptake and extracellular precipitation/ adsorption each accounted for about one third of the total phosphate removed. About two thirds of the total influent nitrogen was removed by “simultaneous” nitrification and denitrification and most of the remainder was removed as organic nitrogen in the surplus sludge. The continuous recycling of activated sludge containing extracellularly adsorbed colloidal phosphate precipitates eliminates the need for nucleation and induction and provides additional surface area with active sites for adsorption of excess phosphate. This could explain the observation that phosphate removal efficiencies improved when solids retention times and sludge concentrations were increased. The plant and its performance have been described in detail in previous papers by the same Authors:1980 “The ability of the extended aeration activated sludge process to remove phosphorus consistently to less than 0,1 mg P/l in a simple surface-aerated rectangular reactor.” IWPC (South African Branch) Conference, Pretoria (2-6 June).1981 “Application of numerical models to design and operation of municipal wastewater treatment works incorporating multi-mini-step activated sludge reactors for enhanced P-removal.” Unpublished.1982 “Full scale phosphate removal experiences in the Umhlatuzana Works at different sludge ages.” IAWPR Post Conference Seminar on phosphate removal in biological treatment processes, Pretoria 5-6 ApriI 1982. Wat.Sci.Tech.Vol. 15, Cape Town, pp 261-281.1983 “Further developments in the understanding of phosphate removal at Umhlatuzana.” IWPC Conference, East London. Operating at sludge temperatures in the range 17°C to 26°C for many years without chemical dosing, the plant exhibited, from time to time, the ability to remove consistently for many consecutive months 95% of the carbon, phosphate, and nitrogen from unsettled municipal wastewater (in a soft water area), with a TKN/COD ratio of 0,07; a P/COD ratio of 0,014; and a low alkalinity/COD ratio of 0,25 (as CaCO3/COD).


1992 ◽  
Vol 25 (4-5) ◽  
pp. 203-209 ◽  
Author(s):  
R. Kayser ◽  
G. Stobbe ◽  
M. Werner

At Wolfsburg for a load of 100,000 p.e., the step-feed activated sludge process for nitrogen removal is successfully in operation. Due to the high denitrification potential (BOD:TKN = 5:1) the effluent total nitrogen content can be kept below 10 mg l−1 N; furthermore by some enhanced biological phosphate removal about 80% phosphorus may be removed without any chemicals.


1983 ◽  
Vol 15 (3-4) ◽  
pp. 15-41 ◽  
Author(s):  
G v R Marais ◽  
R E Loewenthal ◽  
I P Siebritz

The paper briefly reviews the development of the biological excess removal of phosphorus in the activated sludge process, from 1959 when it was first observed to the present. It concludes by proposing, tentatively, a biochemical mechanism whereby excess P uptake and release can be explained.


1993 ◽  
Vol 28 (11-12) ◽  
pp. 499-512 ◽  
Author(s):  
S. H. Isaacs ◽  
M. Henze ◽  
H. Søeberg ◽  
M. Kümmel

Pilot plant studies indicate that the addition of COD in the form of acetate to an alternating nutrient removal activated sludge process as a means to improve denitrification rates is not detrimental to biological phosphate removal. This is in spite of the fact that the added acetate can cause a significant release of phosphate during the anoxic phases in the aeration tanks. The added COD also appears to result in increased rates of aerobic phosphate uptake, thus improving the phosphate removal ability of the process. These observations are presented and discussed in the paper.


1985 ◽  
Vol 17 (11-12) ◽  
pp. 139-146 ◽  
Author(s):  
T. E. Cloete ◽  
P. L. Steyn ◽  
L. Buchan

Data are reported on the role of Acinetobacter in phosphate removal in activated sludge. The fluorescent antibody (FA) technique was applied in an autecological study of Acinetobacter in this habitat. Results indicated that Acinetobacter was present in numbers exceeding 106 organisms per cm3 throughout all zones of the activated sludge process, with higher numbers occurring in the aeration zone. It was also found that Acinetobacter numbers did not vary regardless of whether phosphate was removed or not. Combined electron microscopy and electron dispersive micro-analysis of X-rays (EDAX) furthermore indicated that bacteria from phosphate removing activated sludge plants contained phosphate granules, whereas those from non-removing plants or where removal had stopped, did not contain phosphate granules at all. Hence, it was concluded that no major population shifts of Acinetobacter occurred in activated sludge and that the process of phosphate accumulation is induced in Acinetobacter. However, Acinetobacter never occurred in numbers sufficiently large to account for phosphate removal to the extent sometimes observed in activated sludge.


2016 ◽  
Vol 9 (2) ◽  
Author(s):  
Dinda Rita K. Hartaja ◽  
Imam Setiadi

Generally, wastewater of nata de coco industry contains suspended solids and COD were high, ranging from 90,000 mg / l. The high level of of the wastewater pollutants, resulting in nata de coco industry can not be directly disposed of its wastewater into the environment agency. Appropriate technology required in order to process the waste water so that the treated water can meet the environmental quality standards that are allowed. Designing the waste water treatment plant that is suitable and efficient for treating industrial wastewater nata de coco is the activated sludge process. Wastewater treatment using activated sludge process of conventional (standard) generally consists of initial sedimentation, aeration and final sedimentation.Keywords : Activated Sludge, Design, IPAL


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