Tannery Wastewater Treatment Using an Upflow Anaerobic Fixed Biofilm Reactor (UAFBR)

2003 ◽  
Vol 20 (6) ◽  
pp. 587-599 ◽  
Author(s):  
Z. Song ◽  
C.J. Williams ◽  
R.G.J. Edyvean
2004 ◽  
Vol 50 (10) ◽  
pp. 107-114 ◽  
Author(s):  
C. Di Iaconi ◽  
F. Bonemazzi ◽  
A. Lopez ◽  
R. Ramadori

This paper reports the results of an investigation aimed at evaluating the laboratory-scale performance of an innovative process for treating tannery wastewater. In this process, biological degradation, carried out in a sequencing batch biofilm reactor (SBBR), is combined with chemical oxidation by ozone. Tannery wastewater treatment was carried out, at laboratory scale, on a real primary effluent coming from a centralised plant treating wastewater produced by a large tannery district in Northern Italy. SBBR performance both without and with ozonation, was assessed with very satisfactory results. In particular, in the latter instance the recorded COD, TKN and TSS average removals, (96%), (92%) and (98%) respectively, allowed the maximum allowable concentration values fixed by the Italian regulation in force to be achieved without any additional polishing step. During the investigation biofilm properties (biofilm concentration and biofilm density) and flow dynamics aspects (head loss, shear stress, bed porosity) were also studied. A major feature of the process is that, with or without ozonation, it was characterised by very low specific sludge production (0.05 kgVSS/kgCODremoved) and high biofilm density (i.e. 87-122 gVSS/Lsludge) both contributing to a rather high biofilm concentration (i.e. 31-44 gTSS/Lfilter).


2018 ◽  
Vol 93 (11) ◽  
pp. 3264-3275 ◽  
Author(s):  
Iffat Naz ◽  
Douglas Hodgson ◽  
Ann Smith ◽  
Julian Marchesi ◽  
Shama Sehar ◽  
...  

2003 ◽  
Vol 37 (14) ◽  
pp. 3199-3205 ◽  
Author(s):  
C. Di Iaconi ◽  
A. Lopez ◽  
R. Ramadori ◽  
R. Passino

2010 ◽  
Vol 16 (2) ◽  
pp. 285-288 ◽  
Author(s):  
Weibin TANG ◽  
Houzhen ZHOU ◽  
Zhouliang TAN ◽  
Xudong LI

1998 ◽  
Vol 38 (8-9) ◽  
pp. 155-162 ◽  
Author(s):  
G. Jin ◽  
A. J. Englande

Kinetics of Carbon Tetrachloride biodegradation are evaluated in a continuous-flow fixed-biofilm reactor with controlled initial redox potential. The column was seeded with a mixed culture of indigenous microorganisms Pseudomonas cepacia and Providencia stuartii. The fixed biofilm reactor exhibited 98%–99.9% biodegradation of CT introduced into the reactor at an initial concentration of about 200 μg/l for retention times of 1 to 4 days respectively. Four models were employed to evaluate the kinetics of CT biodegradation. These included: Eckenfelder (1989), Arvin (1991), Bouwer and McCarty (1985) and a biphasic model. Comparison of calculated results with observed results between these models agreed very closely to each other (0.968 < R2 < 0.999). Predicted performance was best described by the model of Bouwer and McCarty (1985). However, the biphasic and Eckenfelder models provided excellent correlations and were much simpler to apply. The biphasic model yielded very good correlations of the data for all detention times evaluated; whereas, the Eckenfelder model effected comparable results only at the longer retention times studied.


2020 ◽  
Vol 6 ◽  
pp. 340-344
Author(s):  
Andreia D. Santos ◽  
Rui C. Martins ◽  
Rosa M. Quinta-Ferreira ◽  
Luis M. Castro

2021 ◽  
pp. 125748
Author(s):  
Vijay Sodhi ◽  
Charanjit Singh ◽  
Puneet Pal Singh Cheema ◽  
Reena Sharma ◽  
Ajay Bansal ◽  
...  

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