Fouling of dairy components on hydrophobic polytetrafluoroethylene (PTFE) membranes for membrane distillation

Abstract This study investigates fouling of membranes during membrane distillation (MD) of two model dairy feeds — skim milk and whey, as well as their major single components. Every MD experiment was conducted for 20 h at 54 °C feed inlet temperature and 5 °C permeate inlet temperature using PTFE membranes. Performance was assessed in terms of throughput (flux) and retention efficiency. Skim milk flux was found to be lower but stable over time compared to whey. The study using single components as well as combinations thereof revealed that fouling was primarily driven by proteins and calcium, but only in combination. Lactose also played a role to a lesser extent in the protein/membrane interactions, possibly due to preferential hydration, but did not interact with the membrane polymer directly. However lactose was found to deposit once an anchor point to the membrane was established by other components. Skim milk showed strong adhesion from its principle proteins, caseins; however salts were needed to form a thick and dense cake layer. Caseins seem to form a layer on the membrane surface that prevents other components from interacting with the membrane polymer. Whey proteins, on the other hand, deposited to a lesser extent. In general, membrane distillation was found to be a process that generates high quality water with retention of all tested components >99% while simultaneously concentrating whey or skim milk.

[1]  Marek Gryta,et al.  Fouling in direct contact membrane distillation process , 2008 .

[2]  Michael J. Lewis,et al.  Hydrodynamic factors affecting flux and fouling during ultrafiltration of skimmed milk , 2000 .

[3]  Munir Cheryan,et al.  Ultrafiltration and Microfiltration Handbook , 1998 .

[4]  F. García-Ochoa,et al.  Kinetic Modeling of Lactose Hydrolysis by a β-Galactosidase from Kluyveromices Fragilis , 1998 .

[5]  Z. Derriche,et al.  Impact of zeta potential and size of caseins as precursors of fouling deposit on limiting and critical fluxes in spiral ultrafiltration of modified skim milks , 2008 .

[6]  R. Boom,et al.  In situ quantification of membrane foulant accumulation by reflectometry , 2010 .

[7]  M. Duke,et al.  Improving cell yield and lactic acid production of Lactococcus lactis ssp. cremoris by a novel submerged membrane fermentation process , 2012 .

[8]  H. G. R. Rao Mechanisms of flux decline during ultrafiltration of dairy products and influence of pH on flux rates of whey and buttermilk , 2002 .

[9]  K. Christensen,et al.  Using direct contact membrane distillation for whey protein concentration , 2006 .

[10]  F. García-Ochoa,et al.  Kinetic modeling of lactose hydrolysis with an immobilized beta-galactosidase from Kluyveromyces fragilis. , 2000, Enzyme and microbial technology.

[11]  O. Monticelli,et al.  Poly(vinylidene fluoride) with improved functionalization for membrane production , 2000 .

[12]  L. Martinez-diez,et al.  Temperature and concentration polarization in membrane distillation of aqueous salt solutions , 1999 .

[13]  M. Turek,et al.  Scaling analysis of nanofiltration systems fed with saturated calcium sulfate solutions in the presence of carbonate ions , 2003 .

[14]  Sangho Lee,et al.  EFFECT OF OPERATING CONDITIONS ON CaSO4 SCALE FORMATION MECHANISM IN NANOFILTRATION FOR WATER SOFTENING , 2000 .

[15]  C. Holt,et al.  Casein Micelle Structure, Functions and Interactions , 2003 .

[16]  G. Daufin,et al.  Physico-chemical aspects of membrane fouling by dairy fluids , 1995 .

[17]  Stephen R Gray,et al.  Direct contact membrane distillation (DCMD): Experimental study on the commercial PTFE membrane and , 2011 .

[18]  C. V. Morr,et al.  Foaming Properties of Lipid‐Reduced and Calcium‐Reduced Whey Protein Concentrates , 1995 .

[19]  J. G. Zadow Whey and Lactose Processing , 1992 .

[20]  H. Singh,et al.  Thermal Denaturation, Aggregation and Gelation of Whey Proteins , 2003 .

[21]  J. Hoek,et al.  BaSO4 solubility prediction in reverse osmosis membrane systems , 1999 .

[22]  G. J. Fleer,et al.  Reflectometry as a tool for adsorption studies , 1994 .

[23]  M. S. Yorgun,et al.  Performance comparison of ultrafiltration, nanofiltration and reverse osmosis on whey treatment , 2008 .

[24]  Mohamed Khayet,et al.  A framework for better understanding membrane distillation separation process , 2006 .

[25]  E. Windhab,et al.  EFFECT OF LACTOSE ON RHEOLOGY OF MILK PROTEIN DISPERSIONS , 2003 .

[26]  F. Temelli,et al.  Probing the hydrophobicity of commercial reverse osmosis membranes produced by interfacial polymerization using contact angle, XPS, FTIR, FE-SEM and AFM , 2011 .

[27]  R. Boom,et al.  Enzyme-catalyzed modification of PES surfaces: reduction in adsorption of BSA, dextrin and tannin. , 2012, Journal of colloid and interface science.

[28]  T. Benezech,et al.  Methodology of analysis of a spiral-wound module. Application to PES membrane for ultrafiltration of skimmed milk , 2006 .

[29]  F. Gaucheron,et al.  Buffering capacity of dairy products , 2005 .

[30]  E. Dickinson,et al.  Effect of sugars on the rheological properties of acid caseinate-stabilized emulsion gels , 2002 .

[31]  M. Corredig,et al.  Characterization of soluble aggregates from whey protein isolate , 2003 .

[32]  G. J. Fleer,et al.  Kinetics of polymer adsorption in stagnation point flow , 1990 .

[33]  M. Mänttäri,et al.  Comparison of analysis methods for protein concentration and its use in UF fractionation of whey , 2011 .

[34]  P. F. Fox,et al.  Dairy Chemistry and Biochemistry , 1998 .

[35]  Siegfried Ripperger,et al.  Length dependency of flux and protein permeation in crossflow microfiltration of skimmed milk , 2008 .

[36]  P. Schurtenberger,et al.  Structure, dynamics, and optical properties of concentrated milk suspensions: an analogy to hard-sphere liquids. , 2002, Journal of colloid and interface science.

[37]  C. Gatti,et al.  Hydrophobicity of whey protein concentrates measured by fluorescence quenching and its relation with surface functional properties. , 2001, Journal of agricultural and food chemistry.

[38]  T. Nickerson,et al.  RECOVERY OF LACTOSE FROM AQUEOUS SOLUTIONS: PRECIPITATION WITH CALCIUM HYDROXIDE AND SODIUM HYDROXIDE , 1977 .

[39]  P. Walstra,et al.  Competitive adsorption between beta-casein or beta-lactoglobulin and model milk membrane lipids at oil-water interfaces. , 2005, Journal of agricultural and food chemistry.

[40]  P. Jelen,et al.  Calcium Association With Isolated Whey Proteins , 1991 .

[41]  A. Karabelas,et al.  Whey protein fouling of microfiltration ceramic membranes—Pressure effects , 2006 .

[42]  Jae-Hong Kim,et al.  Analysis of CaSO4 scale formation mechanism in various nanofiltration modules , 1999 .

[43]  Yan Jing,et al.  Membrane fouling during filtration of milk––a microstructural study , 2003 .

[44]  P. Fox Developments in dairy chemistry. 4. Functional milk proteins. , 1989 .

[45]  Jun-de Li,et al.  Effect of applied pressure on performance of PTFE membrane in DCMD , 2011 .

[46]  Pieter Walstra,et al.  Dairy Technology: Principles of Milk Properties and Processes , 1999 .

[47]  C. S. Kira,et al.  Determination of major and minor elements in dairy products through inductively coupled plasma optical emission spectrometry after wet partial digestion and neutron activation analysis , 2007 .

[48]  F. Rousseau,et al.  Ionic strength dependence of skimmed milk microfiltration: Relations between filtration performance, deposit layer characteristics and colloidal properties of casein micelles , 2011 .

[49]  M. Duke,et al.  Direct Contact Membrane Distillation of Dairy Process Streams , 2011, Membranes.