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Benchmarking of municipal waste water treatment plants (an Austrian project)

机译:市政废水处理厂的基准(奥地利项目)

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An Austrian research project focused on the development of process indicators for treatment plants with different process and operation modes. The whole treatment scheme was subdivided into four processes, i.e. mechanical pretreatment (Process 1), mechanical-biological waste water treatment (Process 2), sludge thickening and stabilisation (Process 3) and further sludge treatment and disposal (Process 4). In order to get comparable process indicators it was necessary to subdivide the sample of 76 individual treatment plants all over Austria into five groups according to their mean organic load (COD) in the influent. The specific total yearly costs, the yearly operating costs and the yearly capital costs of the four processes have been related to the yearly average of the measured organic load expressed in COD (110 g COD/pe/d). The specific investment costs for the whole treatment plant and for Process 2 have been related to a calculated standard design capacity of the mechanical-biological part of the treatment plant expressed in COD. The capital costs of processes 1, 3 and 4 have been related to the design capacity of the treatment plant. For each group (related to the size of the plant) a benchmark band has been defined for the total yearly costs, the total yearly operational costs and the total yearly capital costs. For the operational costs of the Processes 1 to 4 one benchmark (? per pe/year) has been defined for each group. In addition a theoretical cost reduction potential has been calculated. The cost efficiency in regard to water protection and some special sub-processes such as aeration and sludge dewatering has been analysed.
机译:奥地利研究项目专注于使用不同工艺和操作模式的治疗厂的过程指标的开发。将整个处理方案细分为四个方法,即机械预处理(方法1),机械生物废水处理(方法2),污泥增稠和稳定(方法3)以及进一步的污泥处理和处置(过程4)。为了获得可比的过程指示剂,必须将76个个体治疗植物的样品遍布奥地利的76个个体治疗植物的样品根据流入的平均有机载荷(COD)。每年的年度成本,每年的每年的每年的年度成本和每年的年度资本成本与COD(110克COD / PE / D)表达的测量有机载量的年平均值有关。整个治疗厂和过程2的具体投资成本与COD表达的治疗植物的机械生物部分的计算标准设计能力有关。过程1,3和4的资本成本与治疗厂的设计能力有关。对于每组(与工厂大小相关),已为年度成本,年度成本总成本和全年资本成本进行了基准频段。对于流程的运营成本为每组定义了1到4个一个基准(?每个PE /年)。此外,已经计算了理论成本降低电位。分析了水保护的成本效率和曝气和污泥脱水等一些特殊子程序。

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