Caspian seawater desalination and whey concentration through forward osmosis (FO)-reverse osmosis (RO) and FO-FO-RO hybrid systems: Experimental and theoretical study

被引:14
|
作者
Arjmandi, Mehrzad [1 ,2 ]
Chenar, Mahdi Pourafshari [1 ]
Altaee, Ali [3 ]
Arjmandi, Abolfazl [4 ]
Peyravi, Majid [4 ]
Jahanshahi, Mohsen [4 ]
Binaeian, Ehsan [5 ]
机构
[1] Ferdowsi Univ Mashhad, Fac Engn, Chem Engn Dept, Mashhad, Razavi Khorasan, Iran
[2] Kalleh Dairy Co, Solico Grp, R&D Dept, POB 46161-63114, Amol, Iran
[3] Univ Technol Sydney, Sch Civil & Environm Engn, Ctr Technol Water & Wastewater, Sydney, NSW, Australia
[4] Babol Noshirvani Univ Technol, Nanotechnol Res Inst, Membrane Res Grp, Babol, Iran
[5] Chinese Acad Sci, Fujian Inst Res Struct Matter, State Key Lab Struct Chem, Fuzhou, Fujian, Peoples R China
关键词
Forward osmosis; Reverse osmosis; Hybrid; Caspian seawater; Cheese whey; TRACE ORGANIC-COMPOUNDS; REVERSE-OSMOSIS; MEMBRANE; PERFORMANCE; NANOFILTRATION; FUTURE; MICROFILTRATION; PRETREATMENT; TECHNOLOGY; FILTRATION;
D O I
10.1016/j.jwpe.2020.101492
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The current experimental and theoretical study proposes forward osmosis (FO)-reverse osmosis (RO) (FR*) and FO-FO-RO (FFR) hybrid systems to combine concentration of cheese whey and Caspian seawater desalination. The powerful TF-PMM was used as a FO membrane. The impact of sales of concentrated cheese whey on reducing Caspian seawater desalination costs was studied. The results showed that the TF-PMM has good potential for concentration of cheese whey with a water flux of about 12.62 L/m(2)h. In terms of permeate concentration (C-p) and at low recovery rates (RR), the choice of FR* and FFR hybrid systems with 0.3 M NaCl as the draw solution (DS) should be the priority. At high RR, although the sensitivity of the type of system is reduced, the FR* system should not be used. The total power consumption (E-st) for the FR*-30 % and FR*-50 % systems are lower than that of a single RO unit. In FR* hybrid system by increasing the RRFO1, the power consumption of the FO unit and also the Est decreased. Also, in the FFR system, by increasing the concentration of the DS, while increasing the E-st, the power consumption portion of the FO unit decreased. The existence of a valuable by-product in the proposed hybrid systems increases the allowable limit of the cost of required equipment and other operating costs to achieve profitability and reach the break-even point. In the meantime, the FR*-50 % system generates the most revenue, and also the quality of produced freshwater from the FFR-50 %-0.3 M system is the highest.
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页数:10
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