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Cost Modeling and Estimation of Crossflow Membrane Filtration Processes

机译:错流膜过滤过程的成本建模和估算

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ABSTRACTA model is presented for estimating costs of crossflow ultrafiltration and microfiltration processes. The model incorporates separate correlations for several major components of capital costs, thus accounting for different economies of scale associated with different equipment and facilities. In contrast to previous cost-modeling exercises that have inherently assumed an economy of scale for capital costs based on current design estimates, this work considers an economy of scale for the entire membrane system that changes with the design mix as the capacity of the facility increases. The calibrated model is used to explore the impacts of raw water quality, plant capacity, and operating variables on treatment costs. Capital costs amortized per unit of production decrease with plant capacity due to economies of scale. The overall economies of scale associated with a membrane system are considered as a function of the raw water quality and the resultant permeate flux. When permeate flux is limited due to concentration polarization and cake growth, treatment costs are predicted to demonstrate relatively lower economies of scale. Selection of a combination of design and operating parameters such as membrane radius, transmembrane pressure, and system recovery, which results in higher permeate fluxes for a given raw water quality, is predicted to lower total treatment costs.Key words:Cost model; economics; membrane filtration; membrane process; microfiltration; ultrafiltration; water treatment
机译:摘要提出了用于估算错流超滤和微滤工艺成本的模型。该模型包含资本成本的几个主要组成部分的单独相关性,从而考虑了与不同设备和设施相关的不同规模经济。与以前的成本建模工作相比,这些工作本质上假设基于当前设计估计的资本成本的规模经济,这项工作考虑了整个膜系统的规模经济,随着设施容量的增加,该经济会随着设计组合而变化。该校准模型用于探索原水水质、工厂容量和运行变量对处理成本的影响。由于规模经济,每单位产量摊销的资本成本随着工厂产能的增加而降低。与膜系统相关的总体规模经济被认为是原水水质和由此产生的渗透通量的函数。当渗透通量由于浓度极化和滤饼生长而受到限制时,预计处理成本将表现出相对较低的规模经济。选择设计和操作参数的组合,如膜半径、跨膜压力和系统回收率,在给定的原水质量下产生更高的渗透通量,预计将降低总处理成本。关键词:成本模型;经济学;膜过滤;膜工艺;微滤;超滤;水处理

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