CLC number: X703
On-line Access: 2024-08-27
Received: 2023-10-17
Revision Accepted: 2024-05-08
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Cited: 11
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ZHAO Li-jun, MA Fang, GUO Jing-bo, ZHAO Qing-liang. Petrochemical wastewater treatment with a pilot-scale bioaugmented biological treatment system[J]. Journal of Zhejiang University Science A, 2007, 8(11): 1831-1838.
@article{title="Petrochemical wastewater treatment with a pilot-scale bioaugmented biological treatment system",
author="ZHAO Li-jun, MA Fang, GUO Jing-bo, ZHAO Qing-liang",
journal="Journal of Zhejiang University Science A",
volume="8",
number="11",
pages="1831-1838",
year="2007",
publisher="Zhejiang University Press & Springer",
doi="10.1631/jzus.2007.A1831"
}
%0 Journal Article
%T Petrochemical wastewater treatment with a pilot-scale bioaugmented biological treatment system
%A ZHAO Li-jun
%A MA Fang
%A GUO Jing-bo
%A ZHAO Qing-liang
%J Journal of Zhejiang University SCIENCE A
%V 8
%N 11
%P 1831-1838
%@ 1673-565X
%D 2007
%I Zhejiang University Press & Springer
%DOI 10.1631/jzus.2007.A1831
TY - JOUR
T1 - Petrochemical wastewater treatment with a pilot-scale bioaugmented biological treatment system
A1 - ZHAO Li-jun
A1 - MA Fang
A1 - GUO Jing-bo
A1 - ZHAO Qing-liang
J0 - Journal of Zhejiang University Science A
VL - 8
IS - 11
SP - 1831
EP - 1838
%@ 1673-565X
Y1 - 2007
PB - Zhejiang University Press & Springer
ER -
DOI - 10.1631/jzus.2007.A1831
Abstract: In solving the deterioration of biological treatment system treating petrochemical wastewater under low temperatures, bioaugmentation technology was adopted by delivering engineering bacteria into a pilot-scale two-stage anoxic-oxic (A/O) process based on previous lab-scale study. Experimental results showed that when the concentrations of COD and NH4+-N of the influent were 370~910 mg/L and 10~70 mg/L, the corresponding average concentrations of those of effluent were about 80 mg/L and 8 mg/L respectively, which was better than the Level I criteria of the Integrated Wastewater Discharge Standard (GB8978-1996). According to GC-MS analysis of the effluents from both the wastewater treatment plant (WWTP) and the pilot system, there were 68 kinds of persistent organic pollutants in the WWTP effluent, while there were only 32 in that of the pilot system. In addition, the amount of the organics in the effluent of the pilot system reduced by almost 50% compared to that of the WWTP. As a whole, after bioaugmentation, the organic removal efficiency of the wastewater treatment system obviously increased.
[1] Boon, N., Goris, J., de Vos, P., Verstraete, W., Top, E.M., 2000. Bioaugmentation of activated sludge by an indigenous 3-chloroaniline-degrading Comamonas testosterone strain, I2gfp. Appl. Environ. Microbiol., 66(7):2906-2913.
[2] Boon, N., Top, E.M., Verstraete, W., Siciliano, S.D., 2003. Bioaugmentation as a tool to protect the structure and function of an activated sludge microbial community against a 3-chloroaniline shock load. Appl. Environ. Microbiol., 69(3):1511-1520.
[3] Dhouib, A., Hamad, N., Hassaïri, I., Sayadi, S., 2003. Degradation of anionic surfactants by Citrobacter braakii. Process Biochemistry, 38(8):1245-1250.
[4] Elmitwalli, T.A., Oanh, K.L.T., Zeeman, G., Lettinga, G., 2002. Treatment of domestic sewage in a two-step anaerobic filter/anaerobic hybrid system at low temperature. Wat. Res., 36(9):2225-223.
[5] Head, M.A., Oleszkiewicz, J.A., 2004. Bioaugmentation for nitrification at cold temperatures. Wat. Res., 38(3):523-530.
[6] Kennes, C., Mendez, R., Lema, J.M., 1997. Methanogenic degradation of p-cresol in batch and in continuous UASB reactors. Wat. Res., 31(7):1549-1554.
[7] Quan, X.C., Shi, H.C., Liu, H., 2004. Removal of 2,4-dichlorophenol in a conventional activated sludge system through bioaugementation. Process Biochemistry, 39(11):1701-1707.
[8] Ro, K.S., Babcock, R.W., Stenstrom, M.K., 1997. Demonstration of bioaugmentation in a fluidized-bed process treating 1-naphthylamine. Wat. Res., 31(7):1687-1693.
[9] SEPAC (State Environmental Protection Administration of China), 1992. Petrifaction Industry Wastewater Treatment. China Environmental Press, Beijing, p.152-160 (in Chinese).
[10] SSB (State Standard Bureau), 1997. Integrated Wastewater Discharge Standard GB8978-1996.
[11] Venkata Mohan, S., Chandrasekhara Rao, N., Krishna Prasad, K., Sarma, P.N., 2005. Bioaugmentation of an anaerobic sequencing batch biofilm reactor (AnSBBR) with immobilized sulphate reducing bacteria (SRB) for the treatment of sulphate bearing chemical wastewater. Process Biochemistry, 40(8):2849-2857.
[12] Yu, Z.T., Mohn, W.W., 2002. Bioaugmentation with the resin acid-degrading bacterium Zoogloea resiniphila DhA-35 to counteract pH stress in an aerated lagoon treating pulp and paper mill effluent. Wat. Res., 36(11):2793-2801.
[13] Zakkour, P.D., Gaterell, M.R., Griffin, P., Gochin, R.J., Lester, J.N., 2001. Anaerobic treatment of domestic wastewater in temperate climates: treatment plant modeling with economic considerations. Wat. Res., 35(17):4137-4149.
[14] SEPAC (State Environmental Protection Administration of China), 2002. Water and Wastewater Analytical Methods (4 Ed.). China Environmental Press, Beijing (in Chinese).
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