TY - JOUR
T1 - An improved protocol for electrodialytic desalination yielding mineral-balanced potable water
AU - Thakur, Amit K.
AU - Srivastava, Niharika
AU - Chakrabarty, Tina
AU - Rebary, Babulal
AU - Patidar, Rajesh
AU - Sanghavi, Rahul J.
AU - Shahi, Vinod K.
AU - Ghosh, Pushpito K.
N1 - Funding Information:
This work was an outcome of a laboratory project on study of electro-membrane processes. Instrumental support received from Analytical Science Division, CSIR-CSMCRI is gratefully acknowledged. One of the authors (NS) is thankful to the Department of Science and Technology for providing DST-Woman Scientist fellowship. Dr. S. Maiti is acknowledged for information on thermal desalination in solar still.
PY - 2014/2/17
Y1 - 2014/2/17
N2 - Brackish water desalination through distillation produces essentially distilled water devoid of all minerals. In reverse osmosis (RO) all dissolved minerals get depleted but depletion of useful minerals (Mg2+, Ca2+, SO42- and CO32-/HCO3-) is even greater than of Na+ and Cl-. Conventional electrodialysis (EDconv) too fails to meet the desired objective, all constituents being depleted in similar proportions with respect to feed. Consequently, re-mineralisation is necessary but in many cases not implemented. We report selective electrodialysis (EDsel), for production of desalinated water containing relatively higher proportions of desirable minerals. Commercial cation- and anion exchange membranes (CEMCNS and AEMCNS) were coated with polyaniline (PANI), and the resultant membranes (PANI-CEMCNS, PANI-AEMCNS) were characterised by physico-chemical and electrochemical techniques. Due to sieving and hydrophobic effects, the PANI coating was demonstrated to improve the retention of Mg2+, Ca2+ and SO42- during desalination. Retention of mineral constituents was further enhanced with PANI modified styrene-co-divinylbenzene-polyethylene-based interpolymer cation- and anion-exchange membranes (CEMIP and AEMIP). The total alkalinity of the treated stream increased during EDsel, presumably due to concentration polarisation accompanied by preferential transport of H+ over OH-. The process efficiency was only marginally lower (5%) for EDsel, suggesting that this approach to desalination may be of practical importance.
AB - Brackish water desalination through distillation produces essentially distilled water devoid of all minerals. In reverse osmosis (RO) all dissolved minerals get depleted but depletion of useful minerals (Mg2+, Ca2+, SO42- and CO32-/HCO3-) is even greater than of Na+ and Cl-. Conventional electrodialysis (EDconv) too fails to meet the desired objective, all constituents being depleted in similar proportions with respect to feed. Consequently, re-mineralisation is necessary but in many cases not implemented. We report selective electrodialysis (EDsel), for production of desalinated water containing relatively higher proportions of desirable minerals. Commercial cation- and anion exchange membranes (CEMCNS and AEMCNS) were coated with polyaniline (PANI), and the resultant membranes (PANI-CEMCNS, PANI-AEMCNS) were characterised by physico-chemical and electrochemical techniques. Due to sieving and hydrophobic effects, the PANI coating was demonstrated to improve the retention of Mg2+, Ca2+ and SO42- during desalination. Retention of mineral constituents was further enhanced with PANI modified styrene-co-divinylbenzene-polyethylene-based interpolymer cation- and anion-exchange membranes (CEMIP and AEMIP). The total alkalinity of the treated stream increased during EDsel, presumably due to concentration polarisation accompanied by preferential transport of H+ over OH-. The process efficiency was only marginally lower (5%) for EDsel, suggesting that this approach to desalination may be of practical importance.
KW - Desalination
KW - Drinking water
KW - Selective electrodialysis
KW - Useful mineral retention
UR - http://www.scopus.com/inward/record.url?scp=84892463915&partnerID=8YFLogxK
U2 - 10.1016/j.desal.2013.12.007
DO - 10.1016/j.desal.2013.12.007
M3 - Article
AN - SCOPUS:84892463915
SN - 0011-9164
VL - 335
SP - 96
EP - 101
JO - Desalination
JF - Desalination
IS - 1
ER -