Permeation definition

Salt Effects. The definition of a capacity factor k in hydrophobic interaction chromatography is analogous to the distribution coefficient, in gel permeation chromatography ... 

Basic Equations In Background and Definitions, the basic equation for gas permeation was derived with the major assumptions noted. Equation (22-62) may be restated as ... 

For gas and vapor systems, by combining the laws of sorption and diffusion in the sequence (l)-(3), general permeation equations are obtained. For sheet membrane samples of polymers above Tg, if the definition is made that permeation coefficient Q = Ds,... 

Modules and Housings Modern gas membranes are packaged either as hollow-fiber bundles or as spiral-wound modules. The former uses extruded hollow fibers. Tube-side feed is preferable, but it is limited to about 1.5 MPa. Higher-pressure applications are usually fed on the shell side. A large industrial permeator contains fibers 400 pm by 200 pm i.d. in a 6-inch shell 10 feet long. Flat-sheet membrane is wound into spirals, with an 8- by 36-inch permeator containing 25 of membrane. Both types of module are similar to those illustrated in Background and Definitions. Spiral modules are useful when feed... 

In view of Freeman s studies on the use of normal alkanes and polystyrenes to probe the macroporosity of porous materials (24), the results presented here would suggest that low molecular weight species ranging from twenty (deuterium oxide) to several thousand daltons may be used to define microporosity of a SBC support. The ease with which this is achieved may allow routine examination of microporosity in new support materials and a more exact definition of total permeation volume in SBC. 

The ion-selective membrane is the key component of all potentiometric ion sensors. It establishes the preference with which the sensor responds to the ion of interest in the presence of various other ionic components of the sample. By definition, the ion-selective membrane forms a nonpolarized interface with the solution. If the interface is permeable to only one ion, the potential difference at that interface is expressed by the Nernst equation (6.6). If more than one ion can permeate, the interface can be anything between the liquid junction and the mixed potential. The key distinguishing feature is the absolute magnitude of the total exchange current density. 

Many controlled release devices are not membranes by the conventional definition, since only transient release of an active agent, without permeation occurring between an upstream and a downstream, is typical. Nevertheless, some controlled release units do operate with a concentration driving force to achieve effectively steady state release from the internal reservoir of the device to the external surrounding. Such processes are included here for completeness. 

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