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The aim of this work was to investigate the aerobic degradation of high-strength industrial (refinery) wastewaters in the inverse fluidized bed biological reactor, in which polypropylene particles of density 910 kg/m3 were fluidized by an upward flow of gas through a bed. Measurements of chemical oxygen demand (COD) versus residence time t were performed for various ratios of settled bed volume to reactor volume (Vb/VR) and air velocities u. The largest COD reduction, namely, from 54,840 to 2,190 mg/l, i.e. a 96% COD decrease, was achieved when the reactor was operated at the ratio (Vb/VR) = 0.55, air velocity u = 0.046 m/s and t = 65 h. Thus, these values of (Vb/VR), u and t can be considered as the optimal operating parameters for a reactor when used in treatment of high-strength refinery wastewaters. In the treatment operation conducted in a reactor optimally controlled at (Vb/VR) = 0.55, u = 0.046 m/s and t = 65 h, the conversions obtained for all phenolic constituents of the wastewater were larger than 95%. The conversions of about 90% were attained for other hydrocarbons.
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篇名 Evaluation of the Inverse Fluidized Bed Biological Reactor for Treating High-Strength Industrial Wastewaters
来源期刊 化学工程与科学期刊(英文) 学科 地球科学
关键词 BIOLOGICAL WASTEWATER TREATMENT Aerobic WASTEWATER TREATMENT HIGH-STRENGTH Industrial WASTEWATERS Inverse BIOLOGICAL Reactor Fluidized Bed Bioreactor LOW-DENSITY Biomass Support
年,卷(期) 2011,(4) 所属期刊栏目
研究方向 页码范围 239-244
页数 6页 分类号 X7
字数 语种
DOI
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节点文献
BIOLOGICAL
WASTEWATER
TREATMENT
Aerobic
WASTEWATER
TREATMENT
HIGH-STRENGTH
Industrial
WASTEWATERS
Inverse
BIOLOGICAL
Reactor
Fluidized
Bed
Bioreactor
LOW-DENSITY
Biomass
Support
研究起点
研究来源
研究分支
研究去脉
引文网络交叉学科
相关学者/机构
期刊影响力
化学工程与科学期刊(英文)
季刊
2160-0392
武汉市江夏区汤逊湖北路38号光谷总部空间
出版文献量(篇)
386
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