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1)  anaerobic floating bed bilfilm reactor
厌氧浮动床生物膜反应器
2)  Anaerobic floating bed biofilm reacter(AFBBR)
厌氧浮动床生物反应器
3)  anaerobic moving bed biofilm reactor
厌氧移动床生物膜反应器
1.
The biogas-producing capability of anaerobic moving bed biofilm reactor and the factors,such as organic loading rate(OLR),the differences between influent pH and effluent pH(ΔpH),alkalinity and volatile fatty acids(VFA),to affect the biogas output and its composition are investigated by taking wine distillery wastewater as testing example.
以葡萄酒蒸馏废水为例,研究了厌氧移动床生物膜反应器的产气能力以及有机负荷、厌氧系统进水与出水pH差(ΔpH)、碱度、挥发性脂肪酸(VFA)等对沼气产量、沼气成分的影响。
4)  anaerobic/aerobic membrane bioreactor
厌氧-好氧膜生物反应器
5)  anaerobic-aerobic MBR
厌氧/好氧膜生物反应器
1.
In order to investigate the decoloration behavior in treatment of printing and dyeing wastewater by anaerobic-aerobic MBR process,UV-VIS spectrophotometer was employed to evaluate the degradation characteristics of the UV-VIS absorption spectra of dye at various pH of influent.
采用厌氧/好氧膜生物反应器(A/O MBR),以艳蓝KN-R活性染料为模拟染料,在不同进水pH条件下,系统考察了A/O MBR各反应段出水的紫外-可见光谱谱图特征,初步探索pH变化时厌氧与好氧污泥对染料的降解情况。
6)  anaerobic membrane bioreactor
厌氧膜生物反应器
1.
Studying on Treatment Beer Wastewater by the Combined System of Anaerobic Membrane Bioreactor and Ion Exchange;
厌氧膜生物反应器与离子交换工艺组合处理啤酒废水试验研究
2.
In the trials of high concentration food wastewater treatment conducted by an anaerobic membrane bioreactor,the flux decline rule of four polyethersulphone (PES) ultrafiltration (UF) membranes with different surface morphology was investigated with atomic force microscopy.
在厌氧膜生物反应器处理高浓度食品废水的试验中,借助原子力显微镜分析了四种表面形貌不同的聚醚砜超滤膜的通量衰减规律。
3.
This research investigated the effect of high ammonia-N on treatment of municipal landfill leachate by anaerobic membrane bioreactor.
结果表明,COD去除率、沼气产量、沼气产率、辅酶F420和最大比产甲烷活性均随氨氮浓度的增加而减小;当氨氮浓度<3600mg/L时,不会对厌氧膜生物反应器的运行产生明显的影响;氨氮对厌氧污泥产甲烷活性的50%抑制浓度为4350mg/L;高浓度氨氮会造成系统VFA浓度增加;当氨氮浓度由4800mg/L降低到2000mg/L后,受重度抑制的厌氧微生物的活性可以在20d里恢复到未受抑制时的活性水平。
补充资料:厌氧附着膜膨胀床法
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性质:利用反应器中膨胀床载体上的生物膜对废水进行厌氧生物处理的过程。载体常采用烟道灰或硅藻土。废水从密闭反应器底部进入后上升流动,控制床层膨胀率(10%~20%),搅动床层并使废水回流。有机物经厌氧发酵后转化为气体,集中在反应器上部后引出。

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