Fluidized bed biofilm reactor for wastewater treatment

2005 ◽  
pp. 131-169 ◽  
Author(s):  
Wen K. Shieh ◽  
John D. Keenan
Keyword(s):  
Wastewater Treatment ◽  
Fluidized Bed ◽  
Biofilm Reactor

A novel fast mass transfer anaerobic inner loop fluidized bed biofilm reactor for PTA wastewater treatment

2016 ◽  
Vol 74 (5) ◽  
pp. 1088-1095 ◽  
Author(s):  
Yingwen Chen ◽  
Jinlong Zhao ◽  
Kai Li ◽  
Shitao Xie
Keyword(s):  
Mass Transfer ◽  
Wastewater Treatment ◽  
Fluidized Bed ◽  
Terephthalic Acid ◽  
Oxygen Demand ◽  
Biofilm Reactor ◽  
Stable Chemical ◽  
Start Up ◽  
Operation Stability ◽  
Purified Terephthalic Acid

In this paper, a fast mass transfer anaerobic inner loop fluidized bed biofilm reactor (ILFBBR) was developed to improve purified terephthalic acid (PTA) wastewater treatment. The emphasis of this study was on the start-up mode of the anaerobic ILFBBR, the hydraulic loadings and the operation stability. The biological morphology of the anaerobic biofilm in the reactors was also analyzed. The anaerobic column could operate successfully for 46 days due to the pre-aerating process. The anaerobic column had the capacity to resist shock loadings and maintained a high stable chemical oxygen demand (COD) and terephthalic acid removal rates at a hydraulic retention time of 5–10 h, even under conditions of organic volumetric loadings as high as 28.8 kg COD·m−3.d−1. The scanning electron microscope analysis of the anaerobic carrier demonstrated that clusters of prokaryotes grew inside of pores and that the filaments generated by pre-aeration contributed to the anaerobic biofilm formation and stability.

Approximated solution of model for three-phase fluidized bed biofilm reactor in wastewater treatment

2000 ◽  
Vol 5 (1) ◽  
pp. 65-70 ◽  
Author(s):  
Jeong-Woo Choi ◽  
Junhong Min ◽  
Won-Hong Lee ◽  
Sang Baek Lee
Keyword(s):  
Wastewater Treatment ◽  
Fluidized Bed ◽  
Biofilm Reactor ◽  
Three Phase

Mathematical model for a three-phase fluidized bed biofilm reactor in wastewater treatment

1999 ◽  
Vol 4 (1) ◽  
pp. 51-58 ◽  
Author(s):  
Jeong-Woo Choi ◽  
Juhong Min ◽  
Won-Hong Lee ◽  
Sang Back Lee
Keyword(s):  
Mathematical Model ◽  
Wastewater Treatment ◽  
Fluidized Bed ◽  
Biofilm Reactor ◽  
Three Phase

scholarly journals Mathematical model for a three-phase fluidized bed biofilm reactor in wastewater treatment

1999 ◽  
Vol 4 (1) ◽  
pp. 58-58
Author(s):  
Jeong-Woo Choi ◽  
Juhong Min ◽  
Won-Hong Lee ◽  
Sang Back Lee
Keyword(s):  
Mathematical Model ◽  
Wastewater Treatment ◽  
Fluidized Bed ◽  
Biofilm Reactor ◽  
Three Phase

Treatability studies of textile wastewater on an aerobic fluidized bed biofilm reactor (FABR): a case study

2009 ◽  
Vol 59 (9) ◽  
pp. 1817-1821 ◽  
Author(s):  
Thalla Arun Kumar ◽  
S. Saravanan
Keyword(s):  
Wastewater Treatment ◽  
Fluidized Bed ◽  
Removal Efficiency ◽  
Textile Wastewater ◽  
Pilot Scale ◽  
Biofilm Reactor ◽  
Combined Process ◽  
Biofilm Process ◽  
Textile Wastewater Treatment

The performance of a pilot scale aerobic fluidized bed biofilm process and chemical coagulation for textile wastewater treatment was studied. In order to enhance biological treatment efficiency of textile wastewater, poly urethane cubes were incorporated as a supporting media for attached growth. Fenton's reagent was used as a coagulant in the present study. The fluidized bed biofilm process was operated at four HRTs (3, 4.5, 6 and 8 hour) and the results showed that the COD removal efficiency increased from 69% to 94% when the HRT increased from 3 to 4.5 and there of the removal efficiency remained constant around 94%, even though using relatively low MLSS concentration and short sludge retention time. COD and TDS removals of 94.2% and 93.3% were achieved by overall combined process (FABR + Coagulation aided Sedimentation). After the treatment there is remarkable decrease in colour in addition to COD and TDS. This combined process was highly competitive in comparison to the other similar combined systems. It was concluded that this combined process was successfully employed and much effectively decreased they COD, TDS and color of textile wastewater treatment at pilot scale.

Kinetic model for dynamic response of three-phase fluidized bed biofilm reactor for wastewater treatment

2002 ◽  
Vol 10 (1) ◽  
pp. 31-37 ◽  
Author(s):  
Satoshi Tsuneda ◽  
Joseph Auresenia ◽  
Yutaka Inoue ◽  
Yuji Hashimoto ◽  
Akira Hirata
Keyword(s):  
Wastewater Treatment ◽  
Kinetic Model ◽  
Dynamic Response ◽  
Fluidized Bed ◽  
Biofilm Reactor ◽  
Three Phase

Wastewater treatment in a pilot scale inverse fluidized-bed biofilm reactor

1995 ◽  
Vol 9 (1) ◽  
pp. 35-40 ◽  
Author(s):  
Yoon Chan Choi ◽  
Dong Seog Kim ◽  
Tae Joo Park ◽  
Kyung Kee Park ◽  
Seung Koo Song
Keyword(s):  
Wastewater Treatment ◽  
Fluidized Bed ◽  
Pilot Scale ◽  
Biofilm Reactor ◽  
Inverse Fluidized Bed

scholarly journals Moving bed biofilm reactor (MBBR) for dairy wastewater treatment

2020 ◽  
Vol 6 ◽  
pp. 340-344
Author(s):  
Andreia D. Santos ◽  
Rui C. Martins ◽  
Rosa M. Quinta-Ferreira ◽  
Luis M. Castro
Keyword(s):  
Wastewater Treatment ◽  
Biofilm Reactor ◽  
Dairy Wastewater ◽  
Moving Bed Biofilm Reactor ◽  
Moving Bed
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