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Membranes nano-filtration

Rather than use ion exchange, water can be deionized using membrane processes. Both nano-filtration and reverse... [Pg.467]

Reverse osmosis and nano-filtration are high-pressure membrane separation processes (typically 10 to 50 bar for reverse osmosis and 5 to 20 bar for nano-filtration), which can be used to reject dissolved inorganic salt or heavy metals. The processes were discussed in Chapter 10 and are particularly useful for removal of ionic species, such... [Pg.586]

To find a suitable membrane for a certain application, an important parameter is the molecular weight cut-off (MWCO). The MWCO is defined as the molecular weight at which 90% of the solutes are retained by the membrane. It should be taken into account that the pore size of many ultra- and nano filtration membranes is greatly influenced by the solvent and by the temperature used under experimental conditions. This particularly concerns polymeric membranes as will be discussed in the next paragraph. [Pg.78]

The most widely applied commercial nano filtration membrane is the MPF series of Koch Int.[19] (Figure 4.9). The series contains polymeric silicon-derived membranes in the MWCO range of 400-700 Da. [20] The membranes are supplied in a 50% ethanol / water mixture, and should under no circumstances be allowed to dry out. Before use, the membranes must be conditioned with the solvent of choice. [Pg.79]

Koschuh, W., V.H. Thang, S. Krasteva, S. Novalin and K.D. Kulbe, Flux and Retention Behaviour of Nano filtration and Fine Ultrafiltration Membranes in Filtrating Juice from a Green Biorefinery A Membrane Sreening, J. Membr. Sci., 261, 121-128 (2005). [Pg.19]

A holy grail for DON (and DOM in general) remains a rapid and portable method to quantitatively isolate and desalt a large dissolved sample (Bronk, 2002). Such a method would not only allow a wealth of diverse techniques to be brought to bear on the largest unknown fraction of DON, but would allow direct isotopic measurements and compound-specific mass balances. Examples of some approaches currently being explored to improve DON recovery on both small and large scales include homemade ion-retardation resins (Bronk, unpublished data), electrodialysis (Vetter et al, 2007), and use of nano-filtration membranes coupled to standard ultrafiltration approaches (McCarthy et al unpubhshed data). [Pg.1257]

Nano filtration According to the International Union of Pure and Applied Chemistry (lUPAC) recommendations [16] nanofiltration is a pressure-driven membrane-based separation process in which particles and dissolved molecules smaller than about 2 nm are retained. ... [Pg.1104]

C. Guizard, A. Julbe, A. Larbot, L. Cot, Nanostructures in Sol-Gel Derived Materials. Application to the Elaboration of Nano filtration Membranes, Key Engineering Materials Vols. 61 62 (1991) pp. 47-56, Trans Tech Publications, Switzerland. [Pg.178]

These cut-off values are nominal values (N.M.W C O ) and are therefore not always precise enough to be used as an exact parameter when fractioning continuously distributed polymers However ultra-filtration from nano filtration could have a scale of 100-lmil Dalton, Fig 3 illustrates a typical example of the membrane range... [Pg.81]

Van Gestel T, Kruidhof H, Blank DHA, and Bouwmeester HIM. Zr02 and Ti02 membranes for nanofiltration and per-vaporation. Part 1. Preparation and characterization of a corrosion-resistant Zr02 nano filtration membrane with a MWCO < 300. J. Membr. Set 2006 284 128-136. [Pg.254]

Ahmed S, Rasul MG, Hasib MA, Watanabe Y. Performance of nano filtration membrane in a vibrating module (VSEP-NF) for arsenic removal. Desalination 2010 252 127-134. [Pg.291]

Bhanushali, D., Kloos, S., and Bhattacharyya, D. (2002) Solute transport in solvent resistant nano filtration membranes for non-aqueous systems Experimental results and the role of solute-solvent coupling. Journal of Membrane Science 208, 343-359. [Pg.659]

Geng, A., Lin, H. T., and Tan, Y. (2002) Solvent recovery from edible oil extract using nano-filtration ceramic membranes. In World Conference and Exhibition on Oilseed and Edible, Industrial, and Specialty Oils (p. 17) abstracts. Istanbul, Turkey. [Pg.659]

Fig. 7. a Locations for the large losses of exergy in crystallization of amino acids using a water-miscible cosolvent (shaded boxes), b Locations for the small losses of exergy in crystallization of amino acids using a selective (e.g., nano-filtration) membrane... [Pg.12]

Petersen, R.J. 1993. Composite reverse osmosis and nano filtration membranes. d Memh S 83 81-150. [Pg.155]

Biocatalysts are not always immobilized on membranes in bioreactors, though. As enzymes are macromolecules and often differ greatly in size from reactants they can be separated by size exclusion membrane filtration with ultra- or nano-filtration. This is used on an industrial scale in one type of enzyme membrane reactor for the production of enantiopure amino acids by kinetic racemic resolution of chemically derived racemic amino acids. The most prominent example is the production of L-methionine on a scale of 400 t/y (Liese et al, 2006). The advantage of this method over immobilization of the catalyst is that the enzymes are not altered in activity or selectivity as they remain solubilized. This principle can be applied to all macromolecular catalysts which can be separated from the other reactants by means of filtration. So far, only enzymes have been used to a significant extent. [Pg.4]

Separation/desalination/purification using membranes is essentially a mechanical process and usually no heating is needed but sometime operates using pressure, thus consiunes less energy. The main division of this method are (i) Electro-Dialysis Reversal (EDR), (ii) Reverse Osmosis (RO), (iii) Nano-Filtration (NF) and (iv) Membrane Distillation. [Pg.182]

AN, 0-Carboxy methyl chitosan/cellulose acetate blend nano filtration membrane was prepared in acetone solvent. It had been tested to separate chromium and copper fiom effluent treatment. The highest rejection was observed to be 83.40% and 72.60%, respectively (Alka et al., 2010). A chitosan/cellulose acetate/polyethylene glycol ultra filtration membrane was prepared with DMF as solvent. It was focused to be efficient in removing chromium from artificial and tannery effluent wastewater. The highest rejection rate was responding (Sudha et al., 2008).Cross-linked chitosan/polyvinyl alcohol blend beads were prepared and studied for the adsorption capacity of Cd from wastewater. The maximum adsorption of Cd(II) ions was foimd to be 73.75% at pH 6 (Kumar et al., 2009). [Pg.36]

Basu, S. Maes, M. Cano-Odena, A. Alaerts, L. De Vos, D. E. Vankelecom, 1. F. J. solvent resistant nano filtration (SRNF) membranes based on metal-organic frameworks. J. Membrane Science, 2009, 344, 190-198. [Pg.255]

UF membranes operate within the parameters of the micro- and nano-filtration membranes. Therefore, UF membranes have smaller pores as compared to MF membranes. They involve retaining macromolecules and colloids from solution which range between 2-100 nm and operating pressures between 1 and 10 bar., for example, laige organic molecules and proteins. UF is used to separate colloids such as proteins from small molecules such as sugars and salts [16]. [Pg.174]

Here (v) is the observable transmembrane solvent velocity, and P is the membrane solute diffusional permeability. The permeability in turn is defined as the ratio of the molar flux of solute transport, moles/area-time, to the solute concentration difference causing this transport The most familiar examples of low-Pe devices are blood oxygenators and hemodialyzers. High-Pe systems include micro-, ultra-, and nano-filtration and reverse osmosis. The design and operation of membrane separators is discussed in some detail in standard references [Ho and Sirkar, 1992 Noble and Stern, 1995], and a summary of useful predictions is provided in Section 5.4. [Pg.91]

Victor Starov (influence of surface forces on membrane separation nano-filtration, ultra- and microfiltration (fouling and/or gel layers formation)). Department of Chemical Engineering, Loughborough University, Loughborough... [Pg.33]


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