ABSTRACT
The concept of recirculation of diluate/concentrate stream is implemented in multi-stage ion concentration polarization (ICP) desalination to deal with the issue of uncontrolled concentrate streams and deteriorated overall recovery rate to treat highly concentrated oil produce water from refineries. An improved empirical optimization model was established to calculate total energy consumption for operating cost and required membrane area for capital cost for a given set of operating parameters, feed salinity, salt removal ratio, and flow velocity. Using the empirical optimization model, a techno-economic analysis is performed to evaluate the feasibility of two-stage ICP system with recirculation loops. Brine of 160 g/kg is set as the system feed stream, whereas other operating conditions such as dilaute and concentrate streams are being controlled/fixed with 20 g/kg and ~250 g/kg respectively. Also, the system can be flexibly controlled to produce a specific concentration of product water and a recovery ratio with a corresponding water cost. With careful choices of recirculation rates, one can significantly increase the recovery ratio of two-stage ICP brine treatment process (from 25% to 39%) with only minor increase in overall cost (from $16.4-25.9/m3 to $20.6-22.54/m3), which is favourable for brine waste treatment application.
Subject(s)
Water Purification , Salinity , Sodium Chloride , WaterABSTRACT
A techno-economic analysis is used to evaluate the economic feasibility of ion concentration polarization (ICP) desalination for seawater desalination and brine management. An empirical optimization model based on a limited set of experimental data, which was obtained from a lab-scale ICP desalination prototype, was established to calculate the required energy and membrane area for a given set of operating parameters. By calculating operating and capital expenses in various feed and product cases, the optimal levelized cost of water is determined over a range of feed salinities, mostly above seawater salinity (35â¯g/kg). Through these analyses, we study the economic feasibility of three applications: 1) partial desalination of brine discharge by ICP (feed varied from 35 to 75â¯g/kg) to common seawater RO feed level (35â¯g/kg) in a hybrid ICP-RO system; 2) the concentration of seawater desalination brine for salt production, and 3) partial desalination of oilfield wastewater. The economic feasibility of ICP desalination processes has been evaluated and the rough cost of treatment has been generated for several relevant applications. The approach taken in this work could be employed for other new and existing desalination processes, where a priori process modeling and optimization is scientifically and/or numerically challenging.
