Determine the Optimal ZLD Process for Reuse of Reverse Osmosis Effluent

Authors

1 Faculty of Water Engineering, Bandar Abbas Azad University

2 Faculty of Water Engineering, Shiraz University

Abstract

Need for urban water supply in many parts of the world has become a crisis. The need for affordable inland desalination has become critical in many regions of the world where communities strive to meet rapidly growing water demands with limited freshwater supplies [1].
Among various desalination technologies, reverse osmosis (RO) membranes currently have wide acceptance [2].
In ZLD, concentrated water is treated to produce desalinated water and essentially dry salts. Consequently, there is no discharge of liquid waste from the process [3]. There are a variety of process options that can be considered for the intermediate concentrate step including adsorption processes, chemical precipitation, and ion exchange, or even combinations of these processes [4]. Water that passes through the membrane is recovered as product water. As recovery of product water in RO is pushed to its sustainable limit, water on the feed side of the membrane becomes increasingly concentrated and supersaturated, with respect to sparingly soluble salts such as calcium carbonate (CaCO3), calcium sulfate (CaSO4), barium sulfate (BaSO4), and silica (SiO2) [5, 6, 7]. If the feed solution becomes sufficiently supersaturated, these salts precipitate and form deposits on the membrane surface. Deposition of these inorganic precipitates on the membrane surface, referred to as scaling, reduces the permeability of the membrane [8, 9]. Therefore, recovery in RO systems is limited by the precipitation potential of sparingly soluble salts [10].

Keywords


[1]     Gardner-Outlaw, T., Engelman, R., "Sustaining Water, Easing Scarcity: A Second Update", Population International, Washington DC, 1997.
[2]     Ning, R., "Reverse Osmosis Process Chemistry Relevant to the Gulf", Desalination, 1999, 123 (2-3), 157-164.
[3]     Mohsen, M. S., Al-Jayyousi, O. R., "Brackish Water Desalination: An Alternative for Water Supply Enhancementin Jordan", Desalination, 1999, 124, 163-174.
[4]     Vergili, I., Kaya, Y., Sen, U., Gönder, Z. B., Aydiner, C., "Techno-Economic Analysis of Textile Dye Bath Wastewater Treatment by Integrated Membrane Processes under the Zero Liquid Discharge Approach", Resources, Conservation and Recycling, 2012, 58, 25-35.
[5]     Li, M., "Reducing Specific Energy Consumption in Reverse Osmosis (RO) Water Desalination: An analysis from First Principles”, Desalination, 2011, 276 (1–3), 128-135.
[6]     Bond, R., Veerapaneni, S., "Zero Liquid Discharge for Inland Desalination", Awwa Research Foundation, US, 2007.
[7]     Ning, Y. R., Troyer, T. L., "Tandom Reverse Osmosis Pprocess for Zero-Liquid Discharge", Desalination, 2009, 237 (1-3), 238-242.
[8]     Oren, Y., Korngold, E., Daltrophe, N., Messalem, R., Volkman, Y., Aronov, L., Weismann, M., "Pilot Studies on High Recovery BWRO-EDR for Near Zero Liquid Discharge Approach", Desalination, 2010, 261 (3), 321-330.
[9]     Nadeem, A. M., Khan, S. H., Mushtaq, S. H., "Management of Treated Pulp and Paper Mill Effluent to Achieve Zero Discharge", Journal of Environmental Management, 2008, 88 (4), 1285-1299.
[10]   Ning, R. Y., Tarquin, A., Trzcinski, M. C., Patwardhan, G., "Recovery Optimization of RO Concentrates from Desert Wells", Desalination, 2006, 20, 315-322.
[11]   Sheikholeslami, R., Tan, S., "Effects of Water Quality on Silica Fouling of Desalination Plants", Desalination, 1999, 126, 267-280.
[12]   Sheikholeslami, R., "Nucleation and Kinetics of Mixed Salts in Scaling", AIChE Journal, 2003, 49, 194-202.