Fouling analysis and control in a DCMD process for SWRO brine

Desalination 367 (2015) 21-27

Authors

Abstract

Fouling remains a significant challenge in the application of membrane distillation process to the desalination industry. This study was focused on the characterizations of fouling layer on the membrane of a membrane distillation process fed with real seawater reverse osmosis concentrate. The deposit morphology and compositions of foulants were determined using different analytical methods, including scanning electron microscopy coupled with energy dispersive X-ray (SEM-EDS), X-ray diffraction (XRD), Fourier transform infrared spectrometry (FTIR), atomic force microscopy (AFM) and contact angle measurement. Organic and inorganic foulants were identified in the fouling layer. The organic deposits characterized by FTIR were polysaccharides, proteins, and humic like substances. Inorganic foulants mainly consist of calcium carbonate, calcium sulfate and halite. The fouling and wetting was effectively controlled by the chemical conditioning of the feed using sodium hypochlorite (NaOCl). The combination of NaOCl-added conditioning and membrane cleaning with 3% HCl restored the permeate flux up to 70–85% and stabilized the electrical conductivity of the distillate for extended time. © 2015 Elsevier B.V. All rights reserved.

Conclusion

1. Membrane fouling and wetting were more significant at the higher feed temperature as the SWRO brine was directly introduced to the DCMD process as a feed. 2. The fouling comprises of significant amount of inorganic foulants such as CaCO3, CaSO4, NaCl and organic foulants including polysaccharide, protein and humic like substances. Fig. 11. ATR-FTIR Spectra of virgin membrane (A), fouled membrane at 60 °C without NaOCl addition (B), fouled membrane at 60 °C with NaOCl addition (C), cleaned membrane (D). [1] K.W. Lawson, D.R. Lloyd, Membrane distillation, J. Membr. Sci. 124 (1997) 1–25. [2] A. Alkhudhiri, N. Darwish, N. Hilal, Membrane distillation: a comprehensive review, [3] M.S. El-Bourawi, Z. Ding, R. Ma, M. Khayet, A framework for better understanding membrane distillation separation process, J. Membr. Sci. 285 (2006) 4–29. [4] J.W. Chew, W.B. Krantz, A.G. Fane, Effect of a macromolecular- or bio-fouling layer on membrane distillation, J. Membr. Sci. 456 (2014) 66–76. [5] S.T. Hsu, K.T. Cheng, J.S. Chiou, Seawater desalination by direct contact membrane [6] S. Srisurichan, R. Jiraratananon, A.G. Fane, Humic acid fouling in the membrane [7] F. He, K.K. Sirkar, J. Gilron, Studies on scaling of membranes in desalination by direct contact membrane distillation: CaCO3 and mixed CaCO3/CaSO4 systems, Chem. Eng. Sci. 64 (2009) 1844–1859. [8] M. Gryta, Alkaline scaling in the membrane distillation process, Desalination 228 (2008) 128–134. [9] F. He, K.K. Sirkar, J. Gilron, Effects of antiscalants to mitigate membrane scaling by direct contact membrane distillation, J. Membr. Sci. 345 (2009) 53–58. [10] M. Gryta, Fouling in direct contact membrane distillation process, J. Membr. Sci. 325 (2008) 383–394. [11] L.D. Nghiem, T. Cath, A scaling mitigation approach during direct contact membrane distillation, Sep. Purif. Technol. 80 (2011) 315–322. [12] J. Ge, Y. Peng, Z. Li, P. Chen, S. Wang, Membrane fouling and wetting in a DCMD [13] E. Alayemieka, S. Lee, D. Kim, Effect of membrane surface characteristics on hydraulic flux balance and feed stream translation in concentrate multi-stage system, [14] S. Nataraj, R. Schomäcker, M. Kraume, I.M. Mishra, A. Drews, Analyses of polysaccharide fouling mechanisms during crossflow membrane filtration, J. Membr. Sci. 308 (2008) 152–161. [15] S. Goh, J. Zhang, Y. Liu, A.G. Fane, Fouling and wetting in membrane distillation (MD) and MD-bioreactor (MDBR) for wastewater reclamation, Desalination 323 (2013) 39–47. [16] H.A.N. Abdulla, E.C. Minor, R.F. Dias, P.G. Hatcher, Changes in the compound classes of dissolved organic matter along an estuarine transect: a study using FTIR and 13C NMR, Geochim. Cosmochim. Acta 74 (2010) 3815–3838. [17] A. Zarebska, D.R. Nieto, K.V. Christensen, B. Norddahl, Ammonia recovery from agricultural wastes by membrane distillation: Fouling characterization and mechanism, Water Res. 56 (2014) 1–10. [18] S. Jeong, S.-J. Kim, L. Hee Kim, M. Seop Shin, S. Vigneswaran, T. Vinh Nguyen, I.S. Kim, Foulant analysis of a reverse osmosis membrane used pretreated seawater, J. Membr. Sci. 428 (2013) 434–444. [19] M. Gryta, M. Tomaszewska, J. Grzechulska, A.W. Morawski, Membrane distillation of NaCl solution containing natural organic matter, J. Membr. Sci. 181 (2001) 279–287. [20] C.-F. Lin, S.-H. Liu, O.J. Hao, Effect of functional groups of humic substances on uf performance, Water Res. 35 (2001) 2395–2402. [21] D. Qu, J. Wang, B. Fan, Z. Luan, D. Hou, Study on concentrating primary reverse osmosis retentate by direct contact membrane distillation, Desalination 247 (2009) 540–550. [22] M. Gryta, Calcium sulphate scaling in membrane distillation process, Chem. Pap. 63 (2009) 146–151. [23] M. Gryta, Desalination of thermally softened water by membrane distillation [24] P. Wang, Z. Wang, Z. Wu, Q. Zhou, D. Yang, Effect of hypochlorite cleaning on the physiochemical characteristics of polyvinylidene fluoride membranes, Chem. Eng. J. 162 (2010) 1050–1056. [25] Z. Wang, F. Meng, X. He, Z. Zhou, L.-N. Huang, S. Liang, Optimisation and performance of NaClO-assisted maintenance cleaning for fouling control in membrane bioreactors, Water Res. 53 (2014) 1–11. [26] Q. Li, M. Elimelech, Organic fouling and chemical cleaning of nanofiltration membranes: measurements and mechanisms, Environ. Sci. Technol. 38 (2004) 4683–4693.

Tags

Chemical pretreatment, Inorganic foulants, Membrane cleaning, Membrane distillation (MD), Organic foulants, Seawater reverse osmosis (SWRO) brine


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