Lo C H, McAdam E, Judd S
Cranfield University, UK E-mail:
Water Sci Technol. 2015;72(10):1739-46. doi: 10.2166/wst.2015.394.
The individual cost contributions to the mechanical components of a small membrane bioreactor (MBR) (100-2,500 m3/d flow capacity) are itemised and collated to generate overall capital and operating costs (CAPEX and OPEX) as a function of size. The outcomes are compared to those from previously published detailed cost studies provided for both very small containerised plants (<40 m3/day capacity) and larger municipal plants (2,200-19,000 m3/d). Cost curves, as a function of flow capacity, determined for OPEX, CAPEX and net present value (NPV) based on the heuristic data used indicate a logarithmic function for OPEX and a power-based one for the CAPEX. OPEX correlations were in good quantitative agreement with those reported in the literature. Disparities in the calculated CAPEX trend compared with reported data were attributed to differences in assumptions concerning cost contributions. More reasonable agreement was obtained with the reported membrane separation component CAPEX data from published studies. The heuristic approach taken appears appropriate for small-scale MBRs with minimal costs associated with installation. An overall relationship of net present value=(a tb)Q(-c lnt+d) was determined for the net present value where a=1.265, b=0.44, c=0.00385 and d=0.868 according to the dataset employed for the analysis.
对小型膜生物反应器(MBR)(流量为100 - 2500立方米/天)机械部件的各项成本贡献进行了分项整理,以生成作为规模函数的总体资本成本和运营成本(资本支出和运营支出)。将结果与之前发表的针对超小型集装箱式工厂(日处理量<40立方米/天)和大型市政工厂(2200 - 19000立方米/天)的详细成本研究结果进行了比较。根据所使用的启发式数据确定的作为流量函数的运营成本、资本支出和净现值(NPV)的成本曲线表明,运营成本呈对数函数,资本支出呈幂函数。运营成本相关性与文献报道的结果在数量上吻合良好。计算出的资本支出趋势与报道数据的差异归因于成本贡献假设的不同。与已发表研究中报道的膜分离组件资本支出数据取得了更合理的一致性。所采用的启发式方法似乎适用于安装成本最低的小型膜生物反应器。根据分析所用数据集,确定了净现值的总体关系为净现值 =(a tb)Q(-c lnt + d),其中a = 1.265,b = 0.44,c = 0.00385,d = 0.868。