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Pore Membranes

Membrane thickness is a factor in microbial retention, Tortiioiis-pore membranes rated at 0,22 jlrn tvpicallv have surface openings as large as 1 jlrn (Fig, 22-71), Narrovv er restrictions are found beneath the surface. In challenge tests, P. diminnta organisms are found vv ell beneath the surface of an 0,2 jlrn membrane, but not in the permeate. [Pg.2045]

Fouling Fouling affec ts MF as it affects all membrane processes. One difference is that the fouling effect caused by deposition of a foulant in the pores or on the surface of the membrane can be confounded by a rearrangement or compression of the sohds cake which may form on the membrane surface. Also, the high, open space found in tortuous-pore membranes makes them slower to foiil and harder to clean. [Pg.2046]

In reverse osmosis water is forced by pressure through a very fine-pore membrane, which has the property of rejecting dissolved salts. The process thus removes both particulate and dissolved matter. Generally, the flux of water is extremely slow, so that large membrane areas have to be installed to achieve the desired output. Different grades of membrane show different rejections and fluxes. [Pg.482]

Filtration of the catalytic mixture using pore membrane filters or filter aids allows the distinction between soluble and insoluble catalysts. Further catalytic activity analysis from the solution and insoluble residue can give information about the state of the real catalyst. In turn, centrifugation can be appropriated to separate metal NPs from the catalytic solutions, due to their high molecular weight and density, and thus to be separated from molecular species. [Pg.430]

This interpretation is consistent with that of Sladek et.ai. who found both that the primary determinant of fecal coliform growth on a membrane filter was the size of the pores adjacent to the feed and that their optimum size was approximately 2.4 pM (8). Sladek s study resulted in the development of a commercial moderately anisotropic membrane with optimum feed surface pores, but with fine surface pores of 0.7 uM The ability of such a large pored membrane to retain all bacteria... [Pg.208]

Coat overnight with Matrigel the required number of 6-well Transwell inserts containing a polycarbonate 8.0 pm pore membrane. [Pg.275]

The electrical potential across a LB film of dioleoyl-lecithin deposited onto a fine-pore membrane, imposed between equimolar aqueous solutions of NaCl and KC1, was reported to exhibit rhythmic and sustained pulsing or oscillations of electrical potential between the two solutions. These oscillations were attributed to the change of permeability of Na+ and K+ ions across the membrane, which originated from the phase transition of lecithin. [Pg.100]

The Vel data as a function of flow rate, Q, are shown for a 10 g/mol molecular weight polystyrene in Figure A. Both the Ubbelohde viscometric data and the membrane viscometer data are platted on the same graph for a 0.6 urn pore membrane at a low concentration of 100 ppm. The flow is Newtonian. The actual agreement of the capillary and membrane viscosities at low flow rates is always excellent when << Dj., and the concentration is extremely low. At small pore size, high concentrations, and high shear rates the flow can become non-Newtonian. The latter effects are only briefly discussed in this paper, but it is this effect that offers an oportunity to characterize the shape rather than the overall size. Even for a relatively large pore (0.6, Hi , membrane the shear rates vary from 100 s at E mi/Hr to 10 s at 200... [Pg.159]

Reynolds numbers are an order of magnitude below turbulence. The D/1 ratios are less than 1/10 except for the 10 hi" pore membrane in which Foiseuille flow formulas need to be corrected for end effects to determine true viscosities or shear rates. [Pg.162]

The particle sampler chosen for this study was the Stacked Filter Unit (SFU) described by Cahill e al (, ) Particle collection in two size fractions was achieved by placing two Nude-pore membrane filters in series. The first filter, with 8pm... [Pg.328]

Sample preparation for color analysis will depend on the type of food sample. Liquid samples such as beverages can be filtered through a 0.45 /rm pore membrane filter and injected directly in the HPLC. Carbonated beverages are degassed. Beverages containing suspended solids are filtered or centrifuged to eliminate suspended solids (143,156,160). [Pg.554]

The analysis of transfer mechanisms of drugs across the intestinal epithelial layer has passed a long way since the theory of lipid pore membrane [118] in which the total pore area of the intestinal membranes was calculated (and found to be low compared with the total surface of the mucosal aspect of the gut), through the Fickian diffusion calculations of the transport of unionized moieties of drug molecules (the Henderson-Hasselbach equation), which led to the conclusion that acidic drugs are absorbed in the stomach [119,120]. [Pg.16]

Fig. 16. a Schematic diagram of the pressure chamber for characterisation of flat membranes by means of a pneumatic SFM. b Height image of a nuclear pore membrane of polycarbonate recorded by the pneumatic SFM at a pressure difference of 0.4 bar. The elevations are resulted from the nitrogen streams through the pores. Reproduced from [167]... [Pg.92]

One step closer to up-scaling to industrial environments is the multiple-bead reactor shown in Fig. 4.9. Here pellet-type catalyst carriers, so-called beads, are positioned in square containers. The beads are made of alumina and are 1 mm in diameter. Gases are passed over these beads through microstructured pore membranes in the cover and the base plate of the containers. [Pg.96]

Nuclear tracks produced by ion beams have been applied to many fields such as track detectors for cosmic rays, nuclear track filters, membranes for separation processes, and single-pore membranes [24], However, the mechanisms of formation of nuclear tracks have not been elucidated so far. [Pg.102]

The NE is an elaborate structure that can be divided into several distinct sub-domains the nuclear pore complexes (NPCs), the lamin polymer, and a double membrane system consisting of the outer nuclear membrane (ONM), inner nuclear membrane (INM), lumen, and pore membrane (PoM) together with their integral proteins (Figure 1 see colour insert). The ONM is not only continuous with the ER, but is also studded with ribosomes indicating that in addition to being the outermost layer of the nucleus it is also a subcompartment of the ER. How much of its complement of integral membrane proteins is unique from more distal ER... [Pg.52]

Hallbeig, E., Wozniak, R.W. and Blobel, G. (1993) An integral membrane protein of the pore membrane domain of the nuclear envelope contains a nucleoporin-like region. J. Cell Biol. 122, 513-521. [Pg.73]

Figure 34.22 Schematic cross-sectional view of plasma polymerization coated large pore membrane. Figure 34.22 Schematic cross-sectional view of plasma polymerization coated large pore membrane.

See other pages where Pore Membranes is mentioned: [Pg.2044]    [Pg.335]    [Pg.23]    [Pg.430]    [Pg.54]    [Pg.427]    [Pg.430]    [Pg.386]    [Pg.862]    [Pg.2]    [Pg.216]    [Pg.443]    [Pg.528]    [Pg.528]    [Pg.552]    [Pg.91]    [Pg.72]    [Pg.57]    [Pg.303]    [Pg.381]    [Pg.46]    [Pg.453]    [Pg.268]    [Pg.174]    [Pg.1802]    [Pg.53]    [Pg.54]   
See also in sourсe #XX -- [ Pg.23 , Pg.24 ]




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Amorphous materials membranes pore structure

Biological membranes pores

Capillary-pore membranes

Carbon molecular sieve membranes pores size

Conical membrane pores

Constricted membrane pores

Filter membranes pore size

Mean pore size, membrane emulsification

Membrane Large pore zeolite

Membrane Medium pore zeolite

Membrane contactors pores entrance

Membrane narrow pore size distribution

Membrane pore densities

Membrane pore formation, microbial

Membrane pore radius

Membrane pore size

Membrane pore size effect

Membrane pore size experiments

Membrane pore-forming peptides

Membrane pore-size distribution

Membrane pores isolated

Membrane pores straight cylindrical

Membrane pores tortuous pore network

Membrane pores, mass transfer

Membrane pores, mass transfer processes

Membrane transition pore

Membrane-spanning pore

Membranes gated pores

Membranes restricted pore size distribution

Membranes with SP-grafted pores

Membranous pore

Microfiltration membrane pore size

Microporous membranes pore sizes

NEARLY STRAIGHT-PORE MEMBRANES

Nanofiltration membranes pore size

Nucleus Membrane, pores

Polymer electrolyte membrane fuel cell pore network modelling

Pore Characteristics and Membrane Architecture

Pore Model for Membrane Gas Transport

Pore filling membrane

Pore flow membranes

Pore size MF membrane

Pore size distribution inorganic membranes

Pore size distributions of membranes

Pore size limitations, ceramic membranes

Pore structure carbon membranes

Pore tortuosity, porous membrane diffusion

Pore-filled composite membranes

Pore-filling electrolyte membranes

Pores in membranes

Porous membranes pore dimensions

Porous membranes, imaging pore opening

Reverse osmosis membranes pore size

Self-assembly membrane pores

Silica membranes pore structure

Some Membranes Have Relatively Large Pores

Straight-pore membrane

The Pore Radius and Tortuosity of a Porous Membrane for Gas Permeation

Tortuous pore, liquid membrane

Tortuous-pore membrane

Track-etched capillary pore membranes

Transmembrane transport membrane pores

Ultrafiltration membranes pore size

Ultrafiltration membranes pore volume distribution

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