CLC number: X172
On-line Access: 2024-08-27
Received: 2023-10-17
Revision Accepted: 2024-05-08
Crosschecked: 0000-00-00
Cited: 6
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CHEN Hong. ATP content and biomass activity in sequential anaerobic/aerobic reactors[J]. Journal of Zhejiang University Science A, 2004, 5(6): 727-732.
@article{title="ATP content and biomass activity in sequential anaerobic/aerobic reactors",
author="CHEN Hong",
journal="Journal of Zhejiang University Science A",
volume="5",
number="6",
pages="727-732",
year="2004",
publisher="Zhejiang University Press & Springer",
doi="10.1631/jzus.2004.0727"
}
%0 Journal Article
%T ATP content and biomass activity in sequential anaerobic/aerobic reactors
%A CHEN Hong
%J Journal of Zhejiang University SCIENCE A
%V 5
%N 6
%P 727-732
%@ 1869-1951
%D 2004
%I Zhejiang University Press & Springer
%DOI 10.1631/jzus.2004.0727
TY - JOUR
T1 - ATP content and biomass activity in sequential anaerobic/aerobic reactors
A1 - CHEN Hong
J0 - Journal of Zhejiang University Science A
VL - 5
IS - 6
SP - 727
EP - 732
%@ 1869-1951
Y1 - 2004
PB - Zhejiang University Press & Springer
ER -
DOI - 10.1631/jzus.2004.0727
Abstract: Specific ATP content of volatile solids was measured to characterize the sludge activity in a sequential anaerobic/aerobic wastewater treatment system, with an upflow anaerobic sludge blanket (UASB) reactor and a three-phase aerobic fluidized bed (AFB) reactor. The wastewater COD level was 2000-3000 mg/L in simulation of real textile wastewater. The ATP content and the specific ATP contents of volatile solids at different heights of the UASB reactor and those of the suspended and immobilized biomass in the AFB reactor were measured. In the UASB reactor, the maximum value of specific ATP (0.85 mg ATP/g VS) was obtained at a hydraulic retention time (HRT) 7.14 h in the blanket solution. In the AFB reactor, the specific ATP content of suspended biomass was higher than that of immobilized biomass and increased with hydraulic retention time reaching a maximum value of 1.6 mg ATP/g VS at hydraulic retention time 4.35 h. The ATP content of anaerobes in the UASB effluent declined rapidly under aerobic conditions following a 2nd-order kinetic model.
[1] Ali, I., Khararjian, H., Ahmed, M., 1985. Viability microbial mass in compartmentalized single activated sludge process.Wat. Res.,19:927-932.
[2] Agar, D.W., 1985. Microbial growth rate measurement techniques.Comprehensive Biotechnology,4:305-327.
[3] APHA, 1992. Standard Methods for the Examination of Water and Wastewater, 17th ed. American Public Health Association, Washington D.C.
[4] Bhattacharya, S.K., Yuan, Q., Jian, P., 1996. Removal of pentachlorophenol from wastewater by combined anaerobic-aerobic treatment.J. Hazard Materials,49(2-3):143-154.
[5] Chung, Y.C., Neethling, J.B., 1988. ATP as a measurement of anaerobic sludge digester activity.J. Water Pollut. Control Fed.,61(3):343-349.
[6] Chung, Y.C, Neethling, J.B., 1990. Viability of anaerobic digest sludge.Journal of Environmental Engineering,116(2):330-342.
[7] Gaikas, P., Livington, A.G., 1993. Use of ATP to characterize biomass viability in freely suspended and immobilized cell bioreactors.Biotechnology and Bio-engineering,42:1337-1351.
[8] Gerritse, J., Schut, F., Gottschal, J.C., 1990. Mixed chemostat cultures of obligately aerobic and fermentative or methanogenic bacteria grown under oxygen-limiting conditions.FEMS Microbiol. Lett.,66:87-93.
[9] Gerritse, J., Schut, F., Gottschal, J.C., 1992. Modeling of mixed chemostat culture of aerobic bacterium,comamonas testosteroni, and anaerobic bacterium veillonella alcalescens: comparison with experimental data.Appl. Environ. Microbiol.,58(5):1466-1476.
[10] Holm-Hansen, O., Booth, C.R., 1966. The measurement of adenosine triphosphate in the ocean and its ecological significance.Limnol. Oceanogar.,11:510-519.
[11] Jorgensen, P.E., Eriksen, T., Jensen, B.K., 1992. Estimation of viable biomass in wastewater and activated sludge by determination of ATP, oxygen utilization rate and FDA hydrolysis.Wat. Res.,26:1495-1501.
[12] Kucnerowicz, F., Verstraete, W., 1979. Direct measurement of microbial ATP in activated sludge samples.J. Chem. Technol. Biotechnol.,29:707-712.
[13] Leach, F., 1981. ATP determination with firefly luciferase.J. Appl. Biochem.,3:473-517.
[14] Lundin, A., Thore, A., 1975. Comparison of methods for extraction of bacterial adenine nucleotides determined by firefly assay.Appl. Microbiol.,30:713-721.
[15] Malaspina, F., Stante, L., Cellnamare, C.M., Tilche, A., 1995. Cheese whey and cheese factory wastewater treatment with a biological anaerobic-aerobic process.Wat. Sci. Technol.,32(12):59-72.
[16] Nelson, P.O., Lawrence, A.W., 1980. Microbial viability measurements and activated sludge kinetics.Wat. Res.,14:217-225.
[17] Randall, A.A., Benefield, L.D., Hill, W.E., Nicol, J.P., Boman, G.K., Jing, S.R., 1997. The effect of volatile fatty acids on enhanced biological phosphorus removal and population structure in anaerobic-aerobic sequencing batch reactors.Wat. Sci. technol.,35(1):153-160.
[18] Roe, P.C., Surinder, J., Bhagat, S.K., 1982. Adenosine triphosphate as a control parameter for activated sludge processes.J. Water Poll. Control Fed.,54(3):244-254.
[19] Speece, R.E., 1983. Anaerobic biotechnology for industrial wastewater treatment.Environ. Sci. Tech.,17(9):416A-427A.
[20] Weddle, C.L., Jenkins, D., 1971. The viability and activity of activated sludge.Wat. Res.,5:621-624.
[21] Zitomer, D.H., Speece, R.E., 1993. Sequential environments for enhanced biotransformation of aqueous contaminants.Environ. Sci. Technol.27(2):226-224.
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