Membrane distillation-crystallization of seawater reverse osmosis brines

被引:277
作者
Ji, Xiaosheng [1 ]
Curcio, Efrem [1 ,2 ]
Al Obaidani, Sulaiman [3 ]
Di Profio, Gianluca [1 ,2 ]
Fontananova, Enrica [1 ,2 ]
Drioli, Enrico [1 ,2 ]
机构
[1] Univ Calabria, Dept Chem Engn & Mat, I-87030 Arcavacata Di Rende, CS, Italy
[2] Univ Calabria, ITM, CNR, I-87030 Arcavacata Di Rende, CS, Italy
[3] Sultan Qaboos Univ, Dept Mech & Ind Engn, Al Khoud 123, PC, Oman
关键词
Membrane distillation; Membrane crystallization; Brine disposal; Zero liquid discharge; ENVIRONMENTAL-IMPACT; NACL SOLUTION; DESALINATION; NUCLEATION; DISPOSAL; KINETICS; GROWTH;
D O I
10.1016/j.seppur.2009.11.004
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This work aims at investigating the performance, in terms of water recovery and NaCl crystallization kinetics, of a membrane distillation-crystallization (MDC) bench-scale plant operated on brines discharged from a seawater reverse osmosis (RO) unit. Experimental tests carried out on artificial RO concentrates resulted in the production of 21 kg/m(3) of NaCl crystals, exhibiting substantially a ordinary cubic shape with size between 20 and 200 mu m; the final water recovery factor increased up to 90%. Analogous investigations carried out on RO brines from natural seawater were affected by the presence of dissolved organic matter, showing a 20% reduction of the amount of salt crystallized, and a 8% decrease of the transmembrane flux. Growth rate of sodium chloride crystals generated from natural RO brines varied between 0.8 x 10(-8) and 2.8 x 10(-8) m/s; these values were 15-23% lower than those measured for NaCl crystals grown form artificial concentrates. in general, the NaCl crystal size distribution was characterized by a narrow dispersion (coefficient of variation within 35-40%). MDC operations were stable over 100 h as a result of a careful control of supersaturation, polarization phenomena, nucleation process and hydrodynamics. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:76 / 82
页数:7
相关论文
共 33 条
[1]   Feasibility of salt production from inland RO desalination plant reject brine: a case study [J].
Ahmed, M ;
Arakel, A ;
Hoey, D ;
Thumarukudy, MR ;
Goosen, MFA ;
Al-Haddabi, M ;
Al-Belushi, A .
DESALINATION, 2003, 158 (1-3) :109-117
[2]   The growth and dissolution of sodium chloride in a fluidized bed crystallizer [J].
Al-Jibbouri, S ;
Ulrich, J .
JOURNAL OF CRYSTAL GROWTH, 2002, 234 (01) :237-246
[3]   Potential of membrane distillation in seawater desalination: Thermal efficiency, sensitivity study and cost estimation [J].
Al-Obaidani, Sulaiman ;
Curcio, Efrem ;
Macedonio, Francesca ;
Di Profio, Gianluca ;
Ai-Hinai, Hilal ;
Drioli, Enrico .
JOURNAL OF MEMBRANE SCIENCE, 2008, 323 (01) :85-98
[4]  
ASSELBERG AJ, 1978, THESIS DELFT TU
[5]  
Baruth E.E., 2005, WATER TREATMENT PLAN, V4th
[6]  
BENNETT RC, 1973, CHEM ENG PROG, V69, P86
[7]   Optimal model-based experimental design in batch crystallization [J].
Chung, SH ;
Ma, DL ;
Braatz, RD .
CHEMOMETRICS AND INTELLIGENT LABORATORY SYSTEMS, 2000, 50 (01) :83-90
[8]   Influence of the structural properties of poly(vinylidene fluoride) membranes on the heterogeneous nucleation rate of protein crystals [J].
Curcio, E ;
Fontananova, E ;
Di Profio, G ;
Drioli, E .
JOURNAL OF PHYSICAL CHEMISTRY B, 2006, 110 (25) :12438-12445
[9]   Membrane distillation and related operations - A review [J].
Curcio, E ;
Drioli, E .
SEPARATION AND PURIFICATION REVIEWS, 2005, 34 (01) :35-86
[10]   Membrane crystallizers [J].
Curcio, E ;
Criscuoli, A ;
Drioli, E .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2001, 40 (12) :2679-2684