CLC number: X703
On-line Access: 2024-08-27
Received: 2023-10-17
Revision Accepted: 2024-05-08
Crosschecked: 2010-01-14
Cited: 6
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Xiao-guang CHEN, Ping ZHENG, Jing CAI, Mahmood QAISAR. Bed expansion behavior and sensitivity analysis for super-high-rate anaerobic bioreactor[J]. Journal of Zhejiang University Science B, 2010, 11(2): 79-86.
@article{title="Bed expansion behavior and sensitivity analysis for super-high-rate anaerobic bioreactor",
author="Xiao-guang CHEN, Ping ZHENG, Jing CAI, Mahmood QAISAR",
journal="Journal of Zhejiang University Science B",
volume="11",
number="2",
pages="79-86",
year="2010",
publisher="Zhejiang University Press & Springer",
doi="10.1631/jzus.B0900256"
}
%0 Journal Article
%T Bed expansion behavior and sensitivity analysis for super-high-rate anaerobic bioreactor
%A Xiao-guang CHEN
%A Ping ZHENG
%A Jing CAI
%A Mahmood QAISAR
%J Journal of Zhejiang University SCIENCE B
%V 11
%N 2
%P 79-86
%@ 1673-1581
%D 2010
%I Zhejiang University Press & Springer
%DOI 10.1631/jzus.B0900256
TY - JOUR
T1 - Bed expansion behavior and sensitivity analysis for super-high-rate anaerobic bioreactor
A1 - Xiao-guang CHEN
A1 - Ping ZHENG
A1 - Jing CAI
A1 - Mahmood QAISAR
J0 - Journal of Zhejiang University Science B
VL - 11
IS - 2
SP - 79
EP - 86
%@ 1673-1581
Y1 - 2010
PB - Zhejiang University Press & Springer
ER -
DOI - 10.1631/jzus.B0900256
Abstract: Bed expansion behavior and sensitivity analysis for super-high-rate anaerobic bioreactor (SAB) were performed based on bed expansion ratio (E), maximum bed sludge content (Vpmax), and maximum bed contact time between sludge and liquid (τmax). Bed expansion behavior models were established under bed unfluidization, fluidization, and transportation states. Under unfluidization state, E was 0, Vpmax was 4 867 ml, and τmax was 844–3 800 s. Under fluidization state, E, Vpmax, and τmax were 5.28%–255.69%, 1 368–4 559 ml, and 104–732 s, respectively. Under transportation state, washout of granular sludge occurred and destabilized the SAB. During stable running of SAB under fluidization state, E correlated positively with superficial gas and liquid velocities (ug and ul), while Vpmax and τmax correlated negatively. For E and Vpmax, the sensitivities of ug and ul were close to each other, while for τmax, the sensitivity of ul was greater than that of ug. The prediction from these models was a close match to the experimental data.
[1] Chen, C., Wang, A.J., Ren, N.Q., Lee, D.J., Lai, J.Y., 2009. High-rate denitrifying sulfide removal process in expanded granular sludge bed reactor. Bioresource Technology, 100(7):2316-2319.
[2] Chen, J.W., Tang, C.J., Zheng, P., Zhang, L., 2008. Performance of lab-scale SPAC anaerobic bioreactor with high loading rate. Chinese Journal Biotechnology, 24(8):1413-1419 (in Chinese).
[3] Chern, H.H., Fan, L.S., Muroyama, K.L., 1984. Hydrodynamics of concurrent gas-liquid-solid semifluidization with a liquid as the continuous phase. American Institute of Chemical Engineers Journal, 30(2):288-294.
[4] Diez Blanco, V., Garacia Encina, P.A., Fdz-polanco, F., 1995. Effects of biofilm growth, gas and liquid velocities on the expansion of an anaerobic fluidized bed reactor (AFBR). Water Research, 29(7):1649-1654.
[5] Heijnen, J.J., Mulder, A., Enger, W., Hoeks, F., 1989. Review on the application of anaerobic fluidized bed reactors in wastewater treatment. Chemical Engineering Journal, 41(3):37-50.
[6] Huang, J.S., Wu, C.S., 1996. Specific energy dissipation rate for fluidized-bed bioreactors. Biotechnology and Bioengineering, 50(6):643-654.
[7] Jin, R.C., Zheng, P., Hu, A.H., Mahmood, Q., 2008. Performance comparison of two anammox reactors: SBR and UBF. Chemical Engineering Journal, 138(1-3):224-230.
[8] Khan, A.R., Richardson, J.F., 1987. The resistance to motion of a solid sphere in a fluid. Chemical Engineering Communications, 62(1):135-150.
[9] Khan, A.R., Richardson, J.F., 1989. Fluid-particle interactions and flow characteristics of fluidized beds and settling suspensions of spherical particles. Chemical Engineering Communications, 78(1):111-130.
[10] Lens, P.N.L., van den Bosch, M.C., Poll, W.H., Lettinga, G., 1998. Effect of staging on volatile fatty acid degradation in a sulfidogenic granular sludge reactor. Water Research, 32(4):1178-1192.
[11] Lettinga, G., Field, J.A., Sierra-Alvarez, R., 1991. Future perspectives for the anaerobic treatment of forest Industrial wastewaters. Water Science and Technology, 24(3/4):91-102.
[12] Pereboom, J.H.F., Vereijken, T.L.F.M., 1994. Methanogenic granule development in full scale internal circulation reactors. Water Science and Technology, 30(8):9-21.
[13] Sowmeyan, R., Swaminathan, G., 2008a. Evaluation of inverse anaerobic fluidized bed reactor for treating high strength organic wastewater. Bioresource Technology, 99(9):3877-3880.
[14] Sowmeyan, R., Swaminathan, G., 2008b. Performance of inverse anaerobic fluidized bed reactor for treating high strength organic wastewater during start-up phase. Bioresource Technology, 99(14):6280-6284.
[15] Summerfelt, S.T., 2006. Design and management of conventional fluidized-sand biofilters. Aquacultural Engineering, 34(3):275-302.
[16] Wu, C.S., Huang, J.S., Chou, H., 2006. Influence of internal biogas production on hydrodynamic behavior of anaerobic fluidized-bed reactors. Water Research, 40(1):126-136.
[17] Yu, H.B., Rittmann, B.E., 1997. Predicting bed expansion and phase hold-ups for there-phase fluidized-bed reactors with and without biofilm. Water Research, 31(10):2604-2616.
[18] Zheng, P., Feng, X.S., 2006. Biotechnology for Wastes Treatment. Higher Education Press, Beijing, China (in Chinese).
[19] Zheng, P., Chen, J.W., Tang, C.J., Hu, B.L., 2008. A New Type of Spiral Automatic Circulation (SPAC) Anaerobic Reactor. China Patent ZL200720106182.6 (in Chinese).
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