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Membranes experimental systems

In whole tissue or cell monolayer experiments, transcellular membrane resistance (Rm = Pm1) lumps mucosal to serosal compartment elements in series with aqueous resistance (R = P ). The operational definition of Lm depends on the experimental procedure for solute transport measurement (see Section VII), but its magnitude can be considered relatively constant within any given experimental system. Since the Kp range dwarfs the range of Dm, solute differences in partition coefficient dominate solute differences in transcellular membrane transport. The lumped precellular resistance and lumped membrane resistance add in series to define an effective resistance to solute transport ... [Pg.173]

Precellular solute ionization dictates membrane permeability dependence on mucosal pH. Therefore, lumenal or cellular events that affect mucosal microclimate pH may alter the membrane transport of ionizable solutes. The mucosal microclimate pH is defined by a region in the neighborhood of the mucosal membrane in which pH is lower than in the lumenal fluid. This is the result of proton secretion by the enterocytes, for which outward diffusion is slowed by intestinal mucus. (In fact, mucosal secretion of any ion coupled with mucus-restricted diffusion will provide an ionic microclimate.) Important differences in solute transport between experimental systems may be due to differences in intestinal ions and mucus secretion. It might be anticipated that microclimate pH effects would be less pronounced in epithelial cell culture (devoid of goblet cells) transport studies than in whole intestinal tissue. [Pg.174]

Attempts to study the entry of ES products into cells using markers of fluid phase endocytosis yielded unexpected results. When larvae browse resistant IEC-6 cells in the presence of extracellular fluorescent dextran, dextran enters the cytoplasm of a significant proportion of the cells in the mono-layer (Butcher et al., 2000). The parameters of dextran entry are most compatible with the conclusion that larvae wound the plasma membranes of IEC-6 cells that is, they create transient breaches in the membrane that allow impermeant markers to enter the cell (McNeil and Ito, 1989). Wounding is considered to be a common occurrence in intestinal epithelia (McNeil and Ito, 1989). Injured cells are able to heal their wounds by recruiting vesicles to seal the breach (Steinhardt et al., 1994). In an experimental system, healing allows the injured cell to retain cytoplasmic dextran. In epithelial cell cultures inoculated with T. spiralis larvae, the relationship between glycoprotein delivery and injury of plasma membranes is not clear, i.e. dextran-laden cells do not always stain with Tyv-specific antibodies and... [Pg.121]

Both active and passive transport occur simultaneously, and their quantitative roles differ at different concentration gradients. At low substrate concentrations, active transport plays a major role, whilst above the concentration of saturation passive diffusion is the major transport process. This very simple rule can be studied in an experimental system using cell culture-based models, and the concentration dependency of the transport of a compound as well as asymmetric transport over the membrane are two factors used to evaluate the presence and influence of transporters. Previous data have indicated that the permeability of actively absorbed compounds may be underestimated in the Caco-2 model due to a lack of (or low) expression of some uptake transporters. However, many data which show a lack of influence of transporters are usually derived from experiments... [Pg.114]

With particular reference to reverse osmosis systems involving cellulose acetate membranes and aqueous solutions, the membrane material has both polar and nonpolar character, and the solvent, of course, is polar. When these two components of the reverse osmosis system are kept constant, preferential sorption at the membrane-solution interface, and, in turn, solute separation in reverse osmosis, may be expected to be controlled by the chemical nature of the solute. If the latter can be expressed by appropriate quantitative physicochemical parameters representing polar-, steric-, nonpolar-, and/or ionic-character of the solutes, then one can expect unique correlations to exist between such parameters and reverse osmosis data on solute separations for each membrane. Experimental results confirm that such is indeed the case (18). [Pg.30]

In in vitro permeability studies conducted in static systems, the UWL adjacent to the membrane can be up to 1500-4000 j,m thick, whereas in vivo the UWL is only 30-300 j,m in the GI tract and is negligible for the BBB [71]. The experimental system is often stirred or shaken to minimize the effects of the UWL. An orbital shaker is often not effective and can be modified by adding beads to enhance the agitation. Recently, it has been clearly demonstrated that the quantitative structure activity relationship was interfered if the UWL limited... [Pg.128]

Figure 2. Experimental system for the measurement of membrane potential by a PVC matrix liquid-membrane-type electrode (reprinted with permission from Yakugaku Zasshi 1995, 115, 432. Copyright 1995 The Pharmaceutical Society of Japan). Figure 2. Experimental system for the measurement of membrane potential by a PVC matrix liquid-membrane-type electrode (reprinted with permission from Yakugaku Zasshi 1995, 115, 432. Copyright 1995 The Pharmaceutical Society of Japan).
S and D (and hence DT) or P for any particular membrane-penetrant system can be determined experimentally by standard methods based on Eq. (1) and appropriate full or partial solutions of Eq. (3)2,3). [Pg.96]

The above discussion provides an illustration of the wealth of information that can be obtained from the transient transport behaviour of non-ideal penetrant-membrane systems. The methods discussed are capable of further development and refinement and are potentially applicable to a wide variety of experimental systems. [Pg.138]

On this basis, our research is based on the development of an experimental system that allows both high yields and good selectivity of the process, limiting the formation of undesirable by-products, and an efficient separation by the identification of a membrane with high phenol permeability and complete rejection to the catalyst. [Pg.357]

Adds, A. Lim, C. Grace, J. The Fluidized Bed Membrane Reactor System A Pilot-Scale Experimental Study Chemical Engineering Science 49, No. 24B (1994) 5833-5843. [Pg.109]

In parallel with the HEM experiments, studies using a model porous membrane (Nuclepore ) system, with urea and mannitol as the permeants, were conducted. These studies showed that for these permeants, under experimental conditions identical to those of the HEM studies, the measured temperature dependence of permeation was in line with measured activation energies of bulk diffusion (Longsworth, 1953). The measured temperature-dependent ratios P glP2T) were 1.34 0.03 and 1.38 0.02 N = 4, ave. s.d.) for urea and mannitol, respectively (Peck et al., 1995). These ratios were viewed as a reference point to which the permeation temperature-dependence ratios determined for HEM could be compared. [Pg.276]


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