TY - JOUR
T1 - Treatment of sulphate wastewater by freeze desalination
AU - Zikalala, N.
AU - Maree, J. P.
AU - Zvinowanda, C.
AU - Akinwekomi, V.
AU - Mtombeni, T.
AU - Mpenyana-Monyatsi, L.
N1 - Publisher Copyright:
© 2017 Desalination Publications. All rights reserved.
PY - 2017/6
Y1 - 2017/6
N2 - Cooling and freezing can be used to produce fresh water from brackish water, industrial brines and leachates from industrial wastes. The aim of this study was to identify how cooling and/or freezing can be used for the recovery of drinking water from sulphate rich solutions associated with various cations. It was found that: (i) If the solution contains only Na2SO4, after pre-treatment with sodium alkalis, it can be removed from solution through cooling down to 0.33 mol/L (31.7 g/L SO4) through crystallization of Na2SO4·10H2O; (ii) the solubility of Na2SO4 upon cooling is influenced by the Cl-concentration; (iii) the Reverse Osmosis-Cooling (ROC) process is most suitable for treatment of saline solutions rich in Na2SO4, as it can be precipitated through cooling as Na2SO4·10H2O, followed by reverse osmosis to produce drinking water; (iv) The energy required to cool water, containing 100 g/L Na2SO4, from 25°C to 0°C, amounts to 10.66 kWh/t water. When the water is further cooled down to freeze 90% of the water, the energy consumption increased from 10.66 kW/h to 37.74 kWh/t.
AB - Cooling and freezing can be used to produce fresh water from brackish water, industrial brines and leachates from industrial wastes. The aim of this study was to identify how cooling and/or freezing can be used for the recovery of drinking water from sulphate rich solutions associated with various cations. It was found that: (i) If the solution contains only Na2SO4, after pre-treatment with sodium alkalis, it can be removed from solution through cooling down to 0.33 mol/L (31.7 g/L SO4) through crystallization of Na2SO4·10H2O; (ii) the solubility of Na2SO4 upon cooling is influenced by the Cl-concentration; (iii) the Reverse Osmosis-Cooling (ROC) process is most suitable for treatment of saline solutions rich in Na2SO4, as it can be precipitated through cooling as Na2SO4·10H2O, followed by reverse osmosis to produce drinking water; (iv) The energy required to cool water, containing 100 g/L Na2SO4, from 25°C to 0°C, amounts to 10.66 kWh/t water. When the water is further cooled down to freeze 90% of the water, the energy consumption increased from 10.66 kW/h to 37.74 kWh/t.
KW - Freeze desalination
KW - Reverse osmosis cooling
UR - http://www.scopus.com/inward/record.url?scp=85027128928&partnerID=8YFLogxK
U2 - 10.5004/dwt.2017.20927
DO - 10.5004/dwt.2017.20927
M3 - Article
AN - SCOPUS:85027128928
SN - 1944-3994
VL - 79
SP - 93
EP - 102
JO - Desalination and Water Treatment
JF - Desalination and Water Treatment
ER -