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This paper presents the results of an optimization study, based on minimum water cost, to explore the feasibility of the hybridization of RO and MSF processes.
It is of interest to note that the minimum water cost occurs at a recovery of about 50% whereas the minimum energy, and thus minimum GHG impact, occurs at a recovery of about 40%.
Nine different scenarios for the production of the same capacity of desalted water are presented and compared from the standpoint of minimum water cost, specific capital cost and water recovery.
The present work is a trial to participate in these efforts to throw more light on the feasibility of the hybridization idea through an optimization study for the prediction and comparison of the minimum water cost of seven different designs of hybrid plants.
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Our objective is to study the system in order to calculate the minimum water production cost as a function of the main parameters of the MSF section.
The minimum water application cost is obtained in all case studies in this paper for center pivot systems irrigating 75 ha, with lateral pipes of 254 mm (10 in.).
Considering three different FO membrane, the minimum specific water cost is 0.5727 $/m3 when mLbL-10 membrane as FO process and disodium phosphate as draw solute.
Third is the SHARPS cost-screening technique to customize process changes and ultimately generate a minimum water utilization network that is cost-effective and affordable.
This paper describes a new holistic framework for designing a cost-effective minimum water network (CEMWN) for industry and urban systems.
The objective of the model is to allocate water resources to each water sector and make the lowest cost under the minimum water demand.
At a minimum, water twice a day.
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