Mg2+//Cl--H2O solution system was treated via membrane distillation and crystallization to recycle the pure water and high NaCl crystal products with high property
simultaneously. The performance of membrane distillation and the properties NaCl product were explored under the different operation temperature and the various concentration of salts. The results indicate that
the permeate flux obviously increased with the increasing of the operation temperature
due to the increasing of the different vapour pressure with the temperature. Moreover
the permeate flux slightly decreased with the adding content of MgCl2 to the solution
it was mainly due to the decrease of the mass fraction of water and the increase of solution viscosity. The surface crystal particle deposition was also evaluated via lunching the comparison experiments. In addition
the hollow fiber membrane used in the experiments presents favorable reusability with 20 cycles during the membrane distillation. The NaCl crystal products obtained under the operation temperature of 65℃ exhibited the narrow size distribution
the smooth crystal surface
the perfect cube structure and without agglomeration
and the average size was 91.04
91.38 and 122.56 μm
and the coefficient of variation (C.V.) was 28.78
30.63 and 36.77
respectively. Meanwhile
the conductivity recycled water was 5 μS?m-1
and the purity of crystal products were higher than 98.15% after washing with the selective solution (ethanol). Therefore
by regulate the membrane permeate flux and interface function
the membrane distillation crystallization is a feasible technology to process the high concentration saline wastewater (Na+
Mg2+//Cl--H2O) to recycle the pure water and NaCl product with high purity
smooth surface and uniform size under the appropriate operation temperature and the lower Mg2+ concentration. This research can explore the potential approach for the ‘near zero discharge’ treatment of multiple ions high saline wastewater and the reuse of the inorganic salt resource.
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Related Author
Guoxin SUN
Mengxuan GOU
Cheng ZHOU
Pei CHANG
Gaohong HE
Xiaobin JIANG
Chuang LI
Yang ZHANG
Related Institution
State Key Laboratory of Fine Chemicals, Engineering Laboratory for Petrochemical Energy-efficient Separation Technology of Liaoning Province, School of Chemical Engineering, Dalian University of Technology
Xi’an Modern Chemistry Research Institute
School of Chemistry and Chemical Engineering, South China University of Technology
Pharmaceutical and Crystallization Process System Engineering Group, Beijing City Key Laboratory of Enze Biomass Fine Chemicals, College of New Materials and Chemical Engineering, Beijing Institute of Petrochemical Technology
State Key Laboratory of Fine Chemicals, Engineering Laboratory for Petrochemical Energy-efficient Separation Technology of Liaoning Province,School of Chemical Engineering, Dalian University of Technology