Lindtner S, Kroiss H, Nowak O
Institute for Water Quality and Waste Management, Vienna University of Technology, Karlsplatz 13, 1040 Wien, Austria.
Water Sci Technol. 2004;50(7):265-71.
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 ([see symbol in text] 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.
奥地利的一个研究项目专注于为具有不同工艺和运行模式的污水处理厂开发过程指标。整个处理方案被细分为四个过程,即机械预处理(过程1)、机械 - 生物废水处理(过程2)、污泥浓缩与稳定化(过程3)以及进一步的污泥处理与处置(过程4)。为了获得可比较的过程指标,有必要根据奥地利各地76个污水处理厂进水的平均有机负荷(化学需氧量)将其样本分为五组。四个过程的特定年度总成本、年度运营成本和年度资本成本已与以化学需氧量表示的实测有机负荷的年度平均值(110克化学需氧量/人/天)相关联。整个污水处理厂和过程2的特定投资成本已与以化学需氧量表示的污水处理厂机械 - 生物部分的计算标准设计能力相关联。过程1、3和4的资本成本已与污水处理厂的设计能力相关联。对于每个组(与工厂规模相关),已为年度总成本、年度总运营成本和年度总资本成本定义了一个基准范围。对于过程1至4的运营成本,已为每个组定义了一个基准(每人每年[见文中符号])。此外,还计算了理论成本降低潜力。分析了在水保护方面以及一些特殊子过程(如曝气和污泥脱水)方面的成本效率。