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Membrane fouling is a process whereby a solution or a particle is deposited on a membrane surface or in membrane pores in a processes such as in a membrane bioreactor,[1] reverse osmosis,[2] forward osmosis,[3] membrane distillation,[4] ultrafiltration, microfiltration, or nanofiltration[5] so that the membrane's performance is degraded. It is a major obstacle to the widespread use of this technology. Membrane fouling can cause severe flux decline and affect the quality of the water produced. Severe fouling may require intense chemical cleaning or membrane replacement. This increases the operating costs of a treatment plant. There are various types of foulants: colloidal (clays, flocs), biological (bacteria, fungi), organic (oils, polyelectrolytes, humics) and scaling (mineral precipitates).[6]

Fouling can be divided into reversible and irreversible fouling based on the attachment strength of particles to the membrane surface. Reversible fouling can be removed by a strong shear force or backwashing. Formation of a strong matrix of fouling layer with the solute during a continuous filtration process will result in reversible fouling being transformed into an irreversible fouling layer. Irreversible fouling is the strong attachment of particles which cannot be removed by physical cleaning.[7]

Contents

Influential factorsEdit

Factors that affect membrane fouling:

Recent fundamental studies indicate that membrane fouling is influenced by numerous factors such as system hydrodynamics, operating conditions,[8] membrane properties, and material properties (solute). At low pressure, low feed concentration, and high feed velocity, concentration polarisation effects are minimal and flux is almost proportional to trans-membrane pressure difference. However, in the high pressure range, flux becomes almost independent of applied pressure.[9] Deviation from linear flux-pressure relation is due to concentration polarization. At low feed flow rate or with high feed concentration, the limiting flux situation is observed even at relatively low pressures.

MeasurementEdit

Flux,[3] transmembrane pressure (TMP), Permeability, and Resistance are the best indicators of membrane fouling. Under constant flux operation, TMP increases to compensate for the fouling. On the other hand, under constant pressure operation, flux declines due to membrane fouling. In some technologies such as membrane distillation, fouling reduces membrane rejection, and thus permeate quality (e.g. as measured by electrical conductivity) is a primary measurement for fouling.[8]

Fouling controlEdit

Even though membrane fouling is an inevitable phenomenon during membrane filtration, it can be minimised by strategies such as cleaning, appropriate membrane selection and choice of operating conditions.

Membranes can be cleaned physically, biologically or chemically. Physical cleaning includes gas scour, sponges, water jets or backflushing using permeate[10] or pressurized air[11]. Biological cleaning uses biocides to remove all viable microorganisms, whereas chemical cleaning involves the use of acids and bases to remove foulants and impurities.

Another strategy to minimise membrane fouling is the use of the appropriate membrane for a specific operation. The nature of the feed water must first be known; then a membrane that is less prone to fouling with that solution is chosen. For aqueous filtration, a hydrophilic membrane is preferred.[12] For membrane distillation, a hydrophobic membrane is preferred.[13]

Operating conditions during membrane filtration are also vital, as they may affect fouling conditions during filtration. For instance, crossflow filtration is often preferred to dead end filtration, because turbulence generated during the filtration entails a thinner deposit layer and therefore minimises fouling (e.g. tubular pinch effect). In some applications such as in many MBR applications, air scour is used to promote turbulence at the membrane surface.

See alsoEdit

ReferencesEdit

  1. ^ Meng, Fangang; Yang, Fenglin; Shi, Baoqiang; Zhang, Hanmin (February 2008). "A comprehensive study on membrane fouling in submerged membrane bioreactors operated under different aeration intensities". Separation and Purification Technology. 59 (1): 91–100. doi:10.1016/j.seppur.2007.05.040. Retrieved 15 April 2015. 
  2. ^ Warsinger, David M.; Tow, Emily W.; Maswadeh, Laith A.; Connors, Grace B.; Swaminathan, Jaichander; Lienhard V, John H. (2018). "Inorganic fouling mitigation by salinity cycling in batch reverse osmosis". Water Research. Elsevier BV. 137: 384–394. doi:10.1016/j.watres.2018.01.060. ISSN 0043-1354. 
  3. ^ a b Tow, Emily W.; Warsinger, David M.; Trueworthy, Ali M.; Swaminathan, Jaichander; Thiel, Gregory P.; Zubair, Syed M.; Myerson, Allan S.; Lienhard V, John H. (2018). "Comparison of fouling propensity between reverse osmosis, forward osmosis, and membrane distillation". Journal of Membrane Science. Elsevier BV. 556: 352–364. doi:10.1016/j.memsci.2018.03.065. ISSN 0376-7388. 
  4. ^ Warsinger, David M.; Swaminathan, Jaichander; Guillen-Burrieza, Elena; Arafat, Hassan A.; Lienhard V, John H. (2015). "Scaling and fouling in membrane distillation for desalination applications: A review". Desalination. Elsevier BV. 356: 294–313. doi:10.1016/j.desal.2014.06.031. ISSN 0011-9164. 
  5. ^ Hong, Seungkwan; Elimelech, Menachem (1997). "Chemical and physical aspects of natural organic matter (NOM) fouling of nanofiltration membranes". Journal of Membrane Science. Elsevier BV. 132 (2): 159–181. doi:10.1016/s0376-7388(97)00060-4. ISSN 0376-7388. 
  6. ^ Baker, R.W. (2004). Membrane Technology and Applications, England: John Wiley & Sons Ltd
  7. ^ Choi, H., Zhang, K., Dionysiou, D.D.,Oerther, D.B.& Sorial, G.A. (2005) Effect of permeate flux and tangential flow on membrane fouling for wastewater treatment. J. Separation and Purification Technology 45: 68-78.
  8. ^ a b Warsinger, David M.; Tow, Emily W.; Swaminathan, Jaichander; Lienhard V, John H. (2017). "Theoretical framework for predicting inorganic fouling in membrane distillation and experimental validation with calcium sulfate". Journal of Membrane Science. Elsevier BV. 528: 381–390. doi:10.1016/j.memsci.2017.01.031. ISSN 0376-7388. 
  9. ^ Ghosh, R., 2006, Principles of Bioseparation Engineering, World Scientific Publishing Pvt Ltd.
  10. ^ Liberman, Boris (2018). "Three methods of forward osmosis cleaning for RO membranes". Desalination. Elsevier BV. 431: 22–26. doi:10.1016/j.desal.2017.11.023. ISSN 0011-9164. 
  11. ^ Warsinger, David M.; Servi, Amelia; Connors, Grace B.; Mavukkandy, Musthafa O.; Arafat, Hassan A.; Gleason, Karen K.; Lienhard V, John H. (2017). "Reversing membrane wetting in membrane distillation: comparing dryout to backwashing with pressurized air". Environmental Science: Water Research & Technology. Royal Society of Chemistry (RSC). 3 (5): 930–939. doi:10.1039/c7ew00085e. ISSN 2053-1400. 
  12. ^ Goosen, M. F. A.; Sablani, S. S.; Al‐Hinai, H.; Al‐Obeidani, S.; Al‐Belushi, R.; Jackson, D. (2005-01-02). "Fouling of Reverse Osmosis and Ultrafiltration Membranes: A Critical Review". Separation Science and Technology. Informa UK Limited. 39 (10): 2261–2297. doi:10.1081/ss-120039343. ISSN 0149-6395. 
  13. ^ Warsinger, David M.; Servi, Amelia; Van Belleghem, Sarah; Gonzalez, Jocelyn; Swaminathan, Jaichander; Kharraz, Jehad; Chung, Hyung Won; Arafat, Hassan A.; Gleason, Karen K.; Lienhard V, John H. (2016). "Combining air recharging and membrane superhydrophobicity for fouling prevention in membrane distillation". Journal of Membrane Science. Elsevier BV. 505: 241–252. doi:10.1016/j.memsci.2016.01.018. ISSN 0376-7388.