Characteristic of Granular Sludge Bed and Granular Sludge in Interior Diversion Expanded Granular Sludge Bed

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The interior diversion expanded granular sludge bed was concurrently operated for 140d to study the characteristic of the granular sludge bed. The influent COD concentration varied from 2000mg/L to 22300 mg/L, hydraulic retention time was maintained constant at 24 h and the organic loading rate was changed through a change in substrate concentration. The results showed that the reactor had great COD removal efficiency. When the MLSS was 23.1g/L, the influent COD was 18890mg/L, the COD removal efficiency was 80.4%; The interior diversion EGSB could greatly improve the role of gas-dynamic, when the liquid upflow velocity was 3.55m/h, the gas production was 5.96 L/d shows higher sludge bed expansion rate than 2.77 L/d about 9.5%. During the experimental, the anaerobic sludge has the following properties: the average sludge diameter was increased from 0.41mm to 1.66mm. Observed under the scanning electronic microscopy, we found that the sludge appeared obviously granulation, the bacteria amount and species are more than seed sludge after operation of 50d. It was found that rough surface of anaerobic sludge has clear figure with being covered by mucous lamina, with visible hole or cavity on surface.

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Advanced Materials Research (Volumes 726-731)

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2813-2817

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August 2013

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© 2013 Trans Tech Publications Ltd. All Rights Reserved

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[1] Collins, G., Foy, C., McHugh, S., O'Flaherty, V. Anaerobic treatment of 2,4,6-trichlorophenol in an expanded granular sludge bed-anaerobic filter (EGSB-AF) reactor at 15˚C FEMS Microbiol. Ecol. 53(2005), 167–178.

DOI: 10.1016/j.femsec.2004.10.008

Google Scholar

[2] Collins, G., Foy, C., McHugh, S., Mahony, T., O'Flaherty, V., Anaerobic biological treatment of phenolic wastewater at 15–18℃. Water Res. 39 (2005) 1620–1640.

DOI: 10.1016/j.watres.2005.01.017

Google Scholar

[3] Connaughton, S., Collins, G., O'Flaherty, V., Development of microbial community structure and activity in a high-rateanaerobic bioreactor at 18℃. Water Res. 40(2006), 1009–1017.

DOI: 10.1016/j.watres.2005.12.026

Google Scholar

[4] Sean Connaughton, Gavin Collins, Vincent O'Flaherty. Psychrophilic and mesophilic anaerobic digestion of brewery effluent:A comparative study. Water Research. 40(2006) 2503 – 2510.

DOI: 10.1016/j.watres.2006.04.044

Google Scholar

[5] LI Guang, Han Xiangkui, LI Jing. Research on Wastewater Treatment efficiency in The Interior Diversion EGSB Reactor. Technology of water treatment. 2009,35(10) pp.97-100.( In Chinese)

Google Scholar

[6] Ricardo F.F. Pontes, Jos´e M. Pinto. Analysis of integrated kinetic and flow models for anaerobic digesters. Chemical Engineering Journal. 122 (2006) p.65–80.

DOI: 10.1016/j.cej.2006.02.018

Google Scholar

[7] YAN Zhiyong, HU Yongyou, XIAO Jibo,XIE Lei, ZHONG Haitao. Simulation of flow patterns in EGSB reactor .Industrial water & wastewater. 2004,35(2) pp.5-9. (In Chinese)

Google Scholar

[8] Abdullah Yasar, Nasir Ahmad, Muhammad Nawaz Chaudhry, Aamir Amanat Ali Khan. Sludge granulation and efficiency of phase separator in UASB reactor treating combined industrial effluent. Journal of Environmental Sciences.19(2007). p.553–558.

DOI: 10.1016/s1001-0742(07)60092-8

Google Scholar