References
- Cama, J., C. Ayora, and A.C. Lasaga. 1999. The deviation-from-equilibrium effect on dissolution rate and on apparent variations in activation energy. Geochim. Cosmochim. Acta 63:2481–6. doi:10.1016/s0016-7037(99)00144-1
- Danckwerts, P.V. 1970. Gas–Liquid Reactions. New York, NY: McGraw-Hill.
- Garg, M., and A. Pundir. 2014. Utilization of brine sludge in nonstructural building components. A sustainable approach. J. Waste Manage. 1:1–7. doi:10.1155/2014/389316
- Guo, R., W. Pan, WX. Zhang and H. Xu. 2011. Dissolution rate of magnesium hydrate for wet flue gas desulfurization. Fuel 90:7–10. doi:10.1016/j.fuel.2010.08.016
- Kaminski, J. 2003. Technologies and costs of SO2-emissions reduction for energy sector. Appl. Energy 75:165–72. doi:10.1016/s0306-2619(03)00029-1
- Kircher, M.S. 1962. Electrolysis of brines in diaphragm cells. In Chlorine: Its Manufacture, Properties and Use, ed. J.S. Sconce, 81–9. New York, NY: Reinhold.
- Klein, C., and C.S. Hurlbut. 1985. Manual of Mineralogy. New York, NY: John Wiley and Sons.
- Levenspiel, O. 1972. Chemical Reaction Engineering. New York, NY: John Wiley and Sons.
- Nassar, M.K.K., R.M. El-Damak, and A.H.M. Ghanem. 2008. Impact of desalination plants brine injection wells on coastal aquifers. Environ. Geol. 54:445–54. doi:10.1007/s00254-007-0849-9
- Randall, S.F., and D.K. Matibe. 2003. Electricity and externalities in South Africa. Energy Policy 31:721–31. doi:10.1016/s0301-4215(02)00123-4
- Rutto, H.L. 2011. Effect of addition of ammonium compounds on the dissolution rate of a South African magnesium-based material. J. Chem. Eng. Jpn. 44:44–7. doi:10.1252/jcej.10we017
- Rutto, H.L., and C. Enweremadu. 2012. Dissolution of a South African calcium based material using urea: An optimized process. Korean J. Chem. Eng. 29:1–8. doi:10.1007/s11814-011-0136-z
- Shin-Min, S., L. Jyh-Ping, and S. Gwo-Yuan. 2001. Dissolution rates of limestones of different sources. J. Hazard. Mater. 79:159–71. doi:10.1016/s0304-3894(00)00253-3
- Souilah, O., D.E. Akretche, and M. Amara. 2004. Water reuse of an industrial effluent by means of electrodeionisation. Desalination 167:49–54. doi:10.1016/j.desal.2004.06.112
- Vedavyasan, C.V. 2001. Combating brine disposal under various scenarios. Desalination 139: 419–21. doi:10.1016/s0011-9164(01)00343-5
- Xiang, G., G. Rui-tang, D. Hong-lei, L. Zhong-yang, and C. Ke-fa. 2009. Dissolution rate of limestone for wet flue gas desulfurization in the presence of sulfite. J. Hazard. Mater. 168:1059–14. doi:10.1016/j.jhazmat.2009.02.156
- Zafar, Z.I. 2008. Determination of semi empirical kinetic model for dissolution of bauxite ore with sulfuric acid: Parametric cumulative effect on the Arrhenius parameters. Chem. Eng. J. 141:233–41. doi:10.1016/j.cej.2007.12.025
- Zhao, J., Y. Li, K. Han, S. Niu, and C. Lu. 2013. Dissolution characteristics of calcium-based alkaline industrial wastes. Can. J. Chem. Eng. 46:827–32. doi:10.1002/cjce.22138