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首页> 外文期刊>Water Science and Technology >Start-up and maturation phases of a full-scale, high-rate anaerobic pond bioreactor (R) plus improved facultative ponds to treat municipal wastewater
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Start-up and maturation phases of a full-scale, high-rate anaerobic pond bioreactor (R) plus improved facultative ponds to treat municipal wastewater

机译:大规模,高速率厌氧池生物反应器(R)的启动和成熟阶段,以及用于处理城市废水的改进的兼性池塘

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摘要

Results of the start-up and maturation phases of a full-scale, high-rate anaerobic pond bioreactor (HRAPB)(R) plus improved facultative ponds (IFPs) to treat municipal wastewater are presented (CODt: 759 mg L-1, CODf: 219 mg L-1, S-SO42-: 102 mg L-1, and Cr+: 1,500 mu gL(-1)). The start-up of the HRAPB (R) comprised, first, the application of a selective pressure increasing up-flow velocity rates. Second, batch stages between successive rates were allowed until 70% of the initial CODf was removed. The IFPs were left in batch and ended when in-pond Chlorophyll-a concentration reached 800 mu gL(-1). Subsequently, the system underwent gradual maturation and reached effluent concentrations of CODt: 223 mg L-1, CODf : 50mg L-1, and Cr+: 60 mu gL(-1). The actual efficiency of the system compared with the expected design efficiency was lower given the characteristics of the influent wastewater biochemical oxygen demand/chemical oxygen demand ratios < 0.4, presence of Cr+ > 1,000 mu gL(-1), and variations in both conductivity (500-4,500 mu Scm(-1)) and pH (6.5-10.5 units). Nonetheless, the system exhibited an adaptation state in less than 1.5 months and yielded an ST/SV ratio of 0.46, and specific methanogenic activity of 0.43 g-CH4-CODg(-1)SV(-1)d(-1) for HRAPB (R); the in-pond Chlorophyll-a was on average 1,200 mu gL(-1) in the IFPs, which demonstrated the robustness of these ecotechnologies in tropical conditions.
机译:提出了一个全规模,高速率厌氧池生物反应器(HRAPB)(R)加上改良的兼性池(IFP)来处理市政废水的启动和成熟阶段的结果(CODt:759 mg L-1,CODf :219 mg L-1,S-SO42-:102 mg L-1和Cr +:1,500μgL(-1))。首先,HRAPB(R)的启动包括施加选择性压力来增加上流速度。第二,允许在连续速率之间进行分批操作,直到去除了初始CODf的70%。 IFP分批保留,当叶绿素a浓度达到800μgL(-1)时终止。随后,该系统逐渐成熟,出水浓度达到CODt:223 mg L-1,CODf:50 mg L-1和Cr +:60μgL(-1)。鉴于进水废水生化需氧量/化学需氧量比率<0.4,存在的Cr +> 1,000μgL(-1)以及两种电导率均存在差异,该系统的实际效率低于预期的设计效率。 500-4,500 mu Scm(-​​1))和pH(6.5-10.5单位)。尽管如此,该系统在不到1.5个月的时间内显示了适应状态,ST / SV比为0.46,对HRAPB的比产甲烷活性为0.43 g-CH4-CODg(-1)SV(-1)d(-1) (R);在IFP中,叶绿素a的平均含量为1200μgL(-1),这证明了这些生态技术在热带条件下的鲁棒性。

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