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Membranes Ultrafiltration, UF

Driving force for the rate of separation hydrostatic pressure. [Pg.133]

Membrane Most UF membranes are polysulfone asymmetric microporous with thin skin 0.1 to 1 [rm supported on a porous layer 50 to 250 jrm. Pore size 0.001-0.2 [rm. This is too porous for RO. Pore size prevents concentration polarization (limiting RO) but performance is limited by gel polarization with 0.2-0.4. Xgei = 0.25-0.35 for macromolecules = 0.75 for colloids. Need to have membrane life 1 year. [Pg.133]

Select diameter or channel spacing so that diameter of the target species is 0.1 of the diameter or channel spacing except for spiral wound where, for 0.75 mm spacing the particles must be 5-25 [im or 0.006-0.034 diameter of spacing for 1 mm spacing particles should be 25-50 p,m or 0.025-0.05 of the diameter or channel spacing. [Pg.133]

Permeate flux depends on the membrane and configuration hollow fibers/ polysulfone 0.005-0.016 L/s nf spiral wound/polysulfone 0.08-0.14 L/s m  [Pg.133]

Liquid permeability increases 25 % for every 10 °C increase in temperature. [Pg.133]


Figure 17. Relationship between volume concentration (formation of virus-rich retentate) and actual virus titer during 100,000 MWC0 membrane ultrafiltration (UF). Supernatant was concentrated 5.6 times by this method. Virus was concentrated 3.8 times. Figure 17. Relationship between volume concentration (formation of virus-rich retentate) and actual virus titer during 100,000 MWC0 membrane ultrafiltration (UF). Supernatant was concentrated 5.6 times by this method. Virus was concentrated 3.8 times.
Membranes such as nylon, polycarbonate, glass wool, Zirfon (a low cost membrane), ultrafiltration (UF), J-cloth, etc., have been widely used for macroscale MFCs. Results show that... [Pg.2199]

The separator is an important component in a MFC, which physically separates the anode and cathode. A variety of separators have been explored for MFCs, including a salt bridge, cation exchange membrane (CEM), anion exchange membrane (AEM), bipolar membrane (BPM), microfiltration (MF) membrane, ultrafiltration (UF) membrane, and porous fabrics and porous materials. [Pg.180]

PVDF-based microporous filters are in use at wineries, dairies, and electrocoating plants, as well as in water purification, biochemistry, and medical devices. Recently developed nanoselective filtration using PVDF membranes is 10 times more effective than conventional ultrafiltration (UF) for removing vimses from protein products of human or animal cell fermentations (218). PVDF protein-sequencing membranes are suitable for electroblotting procedures in protein research, or for analyzing the phosphoamino content in proteins under acidic and basic conditions or in solvents (219). [Pg.389]

Use of ultrafiltration (UF) membranes is becoming increasingly popular for clarification of apple juice. AH particulate matter and cloud is removed, but enzymes pass through the membrane as part of the clarified juice. Thus pasteurization before UF treatment to inactivate enzymes prevents haze formation from enzymatic activity. Retention of flavor volatiles is lower than that using a rack-and-frame press, but higher than that using rotary vacuum precoat-filtration (21). [Pg.573]

Membrane Sep r tion. The separation of components ofhquid milk products can be accompHshed with semipermeable membranes by either ultrafiltration (qv) or hyperfiltration, also called reverse osmosis (qv) (30). With ultrafiltration (UF) the membrane selectively prevents the passage of large molecules such as protein. In reverse osmosis (RO) different small, low molecular weight molecules are separated. Both procedures require that pressure be maintained and that the energy needed is a cost item. The materials from which the membranes are made are similar for both processes and include cellulose acetate, poly(vinyl chloride), poly(vinyHdene diduoride), nylon, and polyamide (see AFembrane technology). Membranes are commonly used for the concentration of whey and milk for cheesemaking (31). For example, membranes with 100 and 200 p.m are used to obtain a 4 1 reduction of skimmed milk. [Pg.368]

Common membrane processes include ultrafiltration (UF), reverse osmosis (RO), electro dialysis (ED), and electro dialysis reversal (EDR). These processes (with the exception of UF) remove most ions RO and UF systems also provide efficient removal of nonionized organics and particulates. Because UF membrane porosity is too large for ion rejection, the UF process is used to remove contaminants, such as oil and grease, and suspended soHds. [Pg.261]

Like normal filtration, with ultrafiltration (UF), a feed emulsion is introduced into and pumped through a membrane unit water and some dissolved low molecular weight materials pass through the membrane under an applied hydrostatic pressure. In contrast to ordinary filtration however, there is no build-up of retained materials on the membrane filter. [Pg.345]

Membranes used for the pressure driven separation processes, microfiltration (MF), ultrafiltration (UF) and reverse osmosis (RO), as well as those used for dialysis, are most commonly made of polymeric materials. Initially most such membranes were cellulosic in nature. These ate now being replaced by polyamide, polysulphone, polycarbonate and several other advanced polymers. These synthetic polymers have improved chemical stability and better resistance to microbial degradation. Membranes have most commonly been produced by a form of phase inversion known as immersion precipitation.11 This process has four main steps ... [Pg.357]

Ultrafiltration (UF) is used for the separation and concentration of macromolecules and colloidal particles. Ultrafiltration membranes usually have larger pore sizes than RO membranes, typically 1 to 100 nanometer (nm). Operating pressures are generally low (30-100 psig). Applications include electropaints, gray water, emulsions, oily wastes, and milk, cheese, and protein processing. [Pg.359]

The effect of pH and cation concentration on pectinesterase (PE) activation and permeation on 30 kD MWCO ultrafiltration (UF) membrane was evaluated. In order of increasing effectiveness, PE activity was stimulated by monovalent and divalent cations, poly amines and trivalent cations. A similar trend was observed for permeation on UF membranes. Cation addition and higher pH releases PE from an inactive complex, increases activity, and increases permeation. Higher cation concentration decreases activity and permeation. These results suggest a common mechanism is involved in PE activation and permeation. [Pg.475]

An survey of recent developments in membrane processes, involving reverse osmosis (RO), ultrafiltration (UF), microfiltration (MF), electrodialysis (ED), dialysis (D), pervaporation (Pr), gas permeation (GP), and emulsion liquid membrane (ELM), has been provided by Sirkar (1997). [Pg.431]

Recently, membrane filtration has become popular for treating industrial effluent. Membrane filtration includes microfiltration (MF), ultrafiltration (UF), nanofiltration (NF), and reverse... [Pg.329]

Ultrafiltration (UF) is an important component in wastewater treatment and in food industry [109,110]. With increasing concerns and regulations in environment as well as in food safety, the process of ultrafiltration has become more critical, whereby new technology development to provide faster and more efficient water treatment is not only necessary but also urgent. Currently, conventional polymeric UF membranes are prepared mainly by the phase immersion process, typically generating an asymmetric porous structure with two major limitations (1) relatively low porosity and (2) fairly broad pore-size distribution [111,112],... [Pg.147]

The development of industrial inorganic ultrafiltration (UF) and microfiltration (MF) membranes resulted from the combination of three factors ... [Pg.4]

Microfiltration (MF) and ultrafiltration (UF) membranes can be used as forms of pretreatment for nanofiltration (ISIF) or reverse osmosis (RO) desalination processes. Membrane pretreatment reduces the amount of chemicals that are required and hence reduces the environmental impact of the final discharge. MF membranes can be used to filter particles with diameters of 0.1-10 pmm and typically remove bacteria, viruses, precipitates, coagulates and large colloidal particles. UF can remove particles with diameters as small as 0.002 pm, and... [Pg.21]

Generally, a distinction can be made between membrane bioreactors based on cells performing a desired conversion and processes based on enzymes. In ceU-based processes, bacteria, plant and mammalian cells are used for the production of (fine) chemicals, pharmaceuticals and food additives or for the treatment of waste streams. Enzyme-based membrane bioreactors are typically used for the degradation of natural polymeric materials Hke starch, cellulose or proteins or for the resolution of optically active components in the pharmaceutical, agrochemical, food and chemical industry [50, 51]. In general, only ultrafiltration (UF) or microfiltration (MF)-based processes have been reported and little is known on the application of reverse osmosis (RO) or nanofiltration (NF) in membrane bioreactors. Additionally, membrane contactor systems have been developed, based on micro-porous polyolefin or teflon membranes [52-55]. [Pg.536]

A biological step is always necessary to remove the carbonaceous fraction from the influent wastewater suspended biomass treatments are the most common. These entail long SRTs (>25-30 d), and compartmentalization of the biological reactor is necessary for the removal of recalcitrant compounds. Furthermore, as many micro-pollutants tend to adsorb/absorb to the biomass flocks, efficient solid/ liquid separation can greatly improve their removal from wastewater and, at the same time, guarantee consistently good effluent quality. MBRs have been suggested for this purpose by many authors [9, 58, 80, 93], some of whom found that ultrafiltration (UF) membranes are more efficient than MF membranes [9, 93]. [Pg.163]

Raw material recovery can be achieved through solvent extraction, steam-stripping, and distillation operations. Dilute streams can be concentrated in evaporators and then recovered. Recently, with the advent of membrane technology, reverse osmosis (RO) and ultrafiltration (UF) can be used to recover and concentrate active ingredients [14]. [Pg.524]

The casein micelles are retained by fine-pore filters. Filtration through large-pore ceramic membranes is used to purify and concentrate casein on a laboratory scale. Ultrafiltration (UF) membranes retain both the caseins... [Pg.123]

In bioprocesses, a variety of apparatus that incorporate artificial (usually polymeric) membranes are often used for both separations and bioreactions. In this chapter, we shall briefly review the general principles of several membrane processes, namely, dialysis, ultrafiltration (UF), microfiltration (MF), and reverse osmosis (RO). [Pg.133]


See other pages where Membranes Ultrafiltration, UF is mentioned: [Pg.1385]    [Pg.132]    [Pg.133]    [Pg.401]    [Pg.489]    [Pg.1385]    [Pg.132]    [Pg.133]    [Pg.401]    [Pg.489]    [Pg.75]    [Pg.2038]    [Pg.356]    [Pg.126]    [Pg.127]    [Pg.354]    [Pg.294]    [Pg.113]    [Pg.440]    [Pg.476]    [Pg.985]    [Pg.284]    [Pg.1246]    [Pg.139]    [Pg.41]    [Pg.146]    [Pg.309]    [Pg.54]    [Pg.470]    [Pg.222]    [Pg.423]   


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