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Medium with double capacity

Rocks are nommiform in terms of their permeability. In this connection in them are identified areas with relatively high permeability, i.e., channels, and with low permeability, i.e., blocks, which could be considered impermeable. In loose porous deposits the size of impermeable particles or their blocks is small and comparable with permeable channels in volume, so their effect is disregarded. Contrary to this, in fractured massive rocks impermeable blocks take most of the volume and actually control the nature of the mass transfer. In most fractured-porous rocks the mechanism of mass transfer depends on the ratio of blocks and permeable channel volumes - fractures separating them. Because of this in recent times the structure of enclosing rocks is ever more often interpreted as mosaic heterogeneous bloc structure or as a medium with double capacity. The idea of such a structure is illustrated in Figure 2.8, b. [Pg.145]

Another approach in the application of affinity protocols is the addition of ethidium bromide to the size-separation medium for double-stranded DNA. This improves the separation capacity of the method at a high field strength to such an extent that even mutations can be detected (43). Theoretical plates up to 107 have been obtained, which is vastly superior to what can be achieved in general with DNA oligomers. [Pg.263]

The fundamental case for pressure filters may be made using equation 10 for dry cake production capacity Y (kg/m s) derived from Darcy s law when the filter medium resistance is neglected. Eor the same cycle time (same speed), if the pressure drop is increased by a factor of four, production capacity is doubled. In other words, filtration area can be halved for the same capacity but only if is constant. If increases with pressure drop, and depending how fast it increases, the increased pressure drop may not give much more capacity and may actually cause capacity reductions. [Pg.393]

While the lipid bilayer has a very low water content, and therefore behaves quite hydrophobically, especially in its core (see Chapter 2 of this volume), the cell wall is rather hydrophilic, with some 90% of water. Physicochemically, the cell wall is particularly relevant because of its high ion binding capacity and the ensuing impact on the biointerphasial electric double layer. Due to the presence of such an electric double layer, the cell wall possesses Donnan-like features, leaving only a limited part of the interphasial potential decay in the diffuse double layer in the adjacent medium. For a detailed outline, the reader is referred to recent overviews of the subject matter [1,2]. [Pg.115]

Alkyl monoesters of poly(vinyl methyl ether-maleic anhydride) (PVM-MA) are bioerodible acidic polymers that are used to control drug release. In biological fluids with poor buffering capacity, drug release from the polymers and their dissolution are slowed owing to the lower pH on the polymer surface. We studied whether the release of timolol from matrices of monoisopropyl ester of PVM-MA in vitro and in vivo in rabbits eyes could be affected by disodium phosphate in the matrices. Addition of disodium phosphate to the matrices doubled the release rate of timolol in vitro, but it did not affect the bulk pH of the dissolution medium. On the basis of the timolol concentrations in the tear fluid and in systemic circulation, disodium phosphate seems to accelerate drug release in vivo also. Disodium phosphate probably affects the rate of dmg release by increasing the microenvironmental pH on the polymer surface. [Pg.155]

If we measure electrocapillary curves of mercury in an aqueous medium which contains KF, NaF, or CsF, then we observe that the typical parabolas become narrower with increasing concentration. Explanation With increasing salt concentration the Debye-length becomes shorter, the capacity of the double layer increases. The maximum of the electrocapillarity curve, and thus the point of zero charge (pzc), remains constant, i.e., neither the cations nor fluoride adsorb strongly to mercury. [Pg.62]

The double-layer capacity depends strongly on the nature of the electrode material, even in cases where there is no specific adsorption of ions and solvent. It was therefore suggested, first by O.K. Rice, that the metal makes a direct contribution to the double-layer capacity. This idea was quantitatively pursued within the -> jel-lium model, in which the distribution of the electrons at the surface is affected by the double-layer field. In essence, the surface electrons form a highly polarizable medium, which enhances the capacity. In combination with the hard sphere electrolyte model, it gives the correct order of magnitude for the capacity at the -> point of zero charge also, it predicts correctly that the capacity of simple sp-metals should increase with the electronic density. An extension of the jellium-hard sphere elec-... [Pg.169]

In some cases of pilot scale filtration, entire units have been enclosed as a secondary containment precaution (see Chapter 8). A recent commercial development is the MBR-Sultzer dynamic filter which is available in three sizes. Dynamic filtration is the same as cross flow filtration with little or no recirculation. The cross flow effect is derived from the spinning of the inner surface filter. This type of filter is more efficient, has a lower pump rate and a much higher linear velocity across the filter surface, than conventional cross flow filtration units. There is also little or no damaging effect on sensitive cells. The medium size has the same capacity as the Westfalia SA-7 separator. Van Hemert and Tiesjema concluded that the dynamic filter is suitable for work requiring strict aseptic and primary containment conditions. The use of a double mechanical seal on the rotating shaft could offer a higher degree of containment if required. [Pg.154]

In Figure 3.5, a double-sided pressurised machine is described. It possesses two inter casings with suction and pressure ports, so that an exchange of the medium to be compressed can take place via both front faces of the compressor stage. This type of arrangement is necessary if large suction capacities are to be realised with comparatively long impellers. [Pg.37]


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See also in sourсe #XX -- [ Pg.146 ]




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