Permeability porous membranes

The ion pair extraction by flow injection analysis (FIA) has been used to analyze sodium dodecyl sulfate and sodium dodecyl ether (3 EO) sulfate among other anionic surfactants. The solvating agent was methanol and the phase-separating system was designed with a PTFE porous membrane permeable to chloroform but impermeable to the aqueous solution. The method is applicable to concentrations up to 1.25 mM with a detection limit of 15 pM [304]. 

Kcurentjes et al. (1996) have also reported the separation of racemic mixtures. Two liquids are made oppositely chiral by the addition of R- or S-enantiomers of a chiral selector, respectively. These liquids are miscible, but are kept separated by a non-miscible liquid contained in a porous membrane. These authors have used different types of hollow-fibre modules and optimization of shell-side flow distribution was carried out. The liquid membrane should be permeable to the enantiomers to be separated but non-permeable to the chiral selector molecules. Separation of racemic mixtures like norephedrine, ephedrine, phenyl glycine, salbutanol, etc. was attempted and both enantiomers of 99.3 to 99.8% purity were realized. 

TFF module types include plate-and-frame (or cassettes), hollow fibers, tubes, monoliths, spirals, and vortex flow. Figures 20-52 and 20-53 show several common module types and the flow paths within each. Hollow fiber or tubular modules are made by potting the cast membrane fibers or tubes into end caps and enclosing the assembly in a shell. Similar to fibers or tubes, monoliths have their retentive layer coated on the inside of tubular flow channels or lumens with a high-permeability porous structure on the shell side. 

Consider a system in which both solutions contain various ions for which the membrane is permeable (diffusible ions) and one type of ion that, for some reason (e.g. a macromolecular ion for a porous membrane), cannot pass through the membrane (non-diffusible ion). The membrane is permeable for the solvent. 

There are several cell monolayer models that are frequently used for the evaluation of drug permeability and absorption potential (Table 18.1). For a more detailed discussion, please refer to Chap. 8. Caco-2 cells (adenocarcinoma cells derived from colon) are the most extensively characterized and frequently used of the available cell lines [5-9], A unique feature of Caco-2 cells is that they undergo spontaneous enterocyte differentiation in cell culture. Unlike intestinal enterocytes, Caco-2 cells are immortalized and replicate rapidly into confluent monolayers. When the cells reach confluency during culture on a semi-porous membrane, they start to polarize and form tight junctions, creating an ideal system for permeability and transport studies. During the past decade, use of... 

The Caco-2 permeability assay is usually performed in a Transwell device (Figure 18.1). The Transwell contains two compartments a donor and a receiver compartment. The apical donor compartment contains a porous membrane that supports the growth of the Caco-2 monolayer. Caco-2 cells are seeded on the porous membrane. Upon confluency of the cell culture, the compound is added into the donor compartment at a concentration range from one to several hundred micromolar. Samples are collected from the receiver compartment for up to 2 h, then LC-UV or LC-MS methods are used to quantify compound in each sample. The permeability coefficient of the compound is calculated based on the following equation ... 

Cell monolayers grown on permeable culture inserts form confluent mono-layers with barrier properties and can be used for drug absorption experiments. The most well-known cell line for the in vitro determination of intestinal drug permeability is the human colon adenocarcinoma Caco-2 [20, 21], The utility of the Caco-2 cell line is due to its spontaneous differentiation to enterocytes under conventional cell culture conditions upon reaching confluency on a porous membrane to resemble the intestinal epithelium. This cell model displays small intestinal carriers, brush borders, villous cell model, tight junctions, and high resistance [22], Caco-2 cells express active transport systems, brush border enzymes, and phase I and II enzymes [22-24], Permeability models... 

In order to make a good gas separation membrane, two demands should be met. First a high permeability is necessary and second the membrane should be selective. Porous membranes have quite high permeabilities [several times 10000 Barrer (1 Barrer = 1 x 10" cmVcm -s-cm Hg) for nitrogen (Vuren et al. 1987)], but relatively low selectivity. Nonporous mem-... 

In dense membranes, no pore space is available for diffusion. Transport in these membranes is achieved by the solution diffusion mechanism. Gases are to a certain extent soluble in the membrane matrix and dissolve. Due to a concentration gradient the dissolved species diffuses through the matrix. Due to differences in solubility and diffusivity of gases in the membrane, separation occurs. The selectivities of these separations can be very high, but the permeability is typically quite low, in comparison to that in porous membranes, primarily due to the low values of diffusion coefficients in the solid membrane phase. 

In this last section some recent developments are mentioned in relation to gas separations with inorganic membranes. In porous membranes, the trend is towards smaller pores in order to obtain better selectivities. Lee and Khang (1987) made microporous, hollow silicon-based fibers. The selectivity for Hj over Nj was 5 at room temperature and low pressures, with permeability being 2.6 x 10 Barrer. Hammel et al. 1987 also produced silica-rich fibers with mean pore diameter 0.5-3.0nm (see Chapter 2). The selectivity for helium over methane was excellent (500-1000), but permeabilities were low (of the order of 1-10 Barrer). 

Dense metallic membranes have the advantage of very high selectivities since only certain species can be dissolved in their structural lattice. However, the permeabilities are lower by a factor of 100 than those of porous membranes (Ilias and Govind 1989, van Vuren et al. 1987, Itoh 1987, Suzuki, Onozato and Kurokawa 1987). For example, the permeability of... 

It is obvious from the above discussion that porous and dense membranes form two different cases, each with its own advantages and disadvantages. Dense membranes, (permeable only to one component) operating at optimum conditions, can be used to obtain complete conversions. However, because the permeation rate is low, the reaction rate has also to be kept low. Porous membranes (permeable to all components but at different permselectivities) are limited under optimum conditions to a maximum conversion (which is not 100%) due to the permeation of all the components. The permeation rates through porous membranes are, however, much higher than those through dense membranes and consequently higher reaction rates or smaller reactor volumes are possible. 

A separator is a porous membrane placed between electrodes of opposite polarity, permeable to ionic flow but preventing electric contact of the electrodes. A variety of separators have been used in batteries over the years. Starting with cedar shingles and sausage casing, separators have been manufactured from cellulosic papers and cellophane to nonwoven fabrics, foams, ion exchange membranes, and microporous flat sheet membranes made from polymeric materials. As batteries have become more sophisticated, separator function has also become more demanding and complex. 

L. C. Clark first suggested in 1956 that the test solution be separated from an amperometric oxygen sensor by a hydrophobic porous membrane, permeable only for gases (for a review of the Clark electrode see [88]). The first potentiometric sensor of this type was the Severinghaus CO2 electrode [150], with a glass electrode placed in a dilute solution of sodium hydrogenocarbonate as the internal sensor (see fig. 4.10). As an equilibrium pressure of CO2, corresponding to the CO2 concentration in the test solution, is established in the... 

The mere preparation of porous membranes is accompanied with a noticeable decrease of permselectivity 11, which is undesirable for reverse osmosis and ultrafiltration, A thin dense layer should be adopted to attain a high permeability with — out the decrease of permselectivity, but this necessarily decreases the mechanical strength. This conflict is largely resolved by the construction of asymmetric or composite membranes as described also in the present review. 

In the membrane tlisiilluliim process, combined use of distillation and membranes is made. Salt water is warmed to produce vapor. This vapor passes through porous membranes, which are permeable to vapor but not to the liquid phase. The vapor is condensed on a cooled surface to produce fresh water. The main advantage of this process is jts simplicity and the need for only small temperature differentials to operate. 

The porous membrane retaining the inicroorganisms was fixed on the surface of the Teflon membrane on the electrode. Furthermore, a gas permeable membrane was placed on the surface of the electrode and covered with a nylon net. 

Many classification schemes for hemodialysis membranes exist. Water permeability through the porous membranes is frequently used.14 Water permeability for a dialyzer is defined by the ultrafiltration coefficient for the particular device (KUF, mL/ h/mmHg). The KUF of any individual fiber will be related to the pore size and has an... 

Various analytical techniques make use of both porous and nonporous (semipermeable) membranes. For porous membranes, components are separated as a result of a sieving effect (size exclusion), that is, the membrane is permeable to molecules with diameters smaller than the membrane pore diameter. The selectivity of such a membrane is thus dependent on its pore diameter. The operation of nonporous membranes is based on differences in solubility and the diffusion coefficients of individual analytes in the membrane material. A porous membrane impregnated with a liquid or a membrane made of a monolithic material, such as silicone rubber, can be used as nonporous membranes. 

Selective barrier structure. Transport through porous membranes is possible by viscous flow or diffusion, and the selectivity is based on size exclusion (sieving mechanism). This means that permeability and selectivity are mainly influenced by membrane pore size and the (effective) size of the components ofthe feed Molecules... 

Highly porous membranes are prepared by a process based on the fibrillation of high-molecular-weight PTFE. Since they have a high permeability for water vapor and none for liquid water, it is combined with fabrics and used for breathable waterproof garments and camping gear. Other uses for these membranes are for special filters, analytical instruments, and in fuel cells.13... 

The third main class of separation methods, the use of micro-porous and non-porous membranes as semi-permeable barriers (see Figure 2c) is rapidly gaining popularity in industrial separation processes for application to difficult and highly selective separations. Membranes are usually fabricated from natural fibres, synthetic polymers, ceramics or metals, but they may also consist of liquid films. Solid membranes are fabricated into flat sheets, tubes, hollow fibres or spiral-wound sheets. For the micro-porous membranes, separation is effected by differing rates of diffusion through the pores, while for non-porous membranes, separation occurs because of differences in both the solubility in the membrane and the rate of diffusion through the membrane. Table 2 is a compilation of the more common industrial separation operations based on the use of a barrier. A more comprehensive table is given by Seader and Henley.1... 

Osmosis involves the transfer, by a concentration gradient, of a solvent through a membrane into a mixture of solute and solvent. The membrane is almost non-permeable to the solute. In reverse osmosis, transport of solvent in the opposite direction is effected by imposing a pressure, higher than the osmotic pressure, on the feed side. Using a non-porous membrane, reverse osmosis successfully desalts water. 

In this chapter, gas-solid systems, with an emphasize on inorganic permeable materials, to produce dense and porous membranes for chemical, sustainable energy, and pollution abatement applications, are considered. However, since the most important membranes currently in use are the polymeric porous membranes, then these are discussed at the end of the chapter. 

Porous membranes with selective permeability to oiganic solvents have been prepared by the extraction of latex films prepared with moderate ratios of PVA—PVAc graft copolymer fractions. The extracted films are made up of a composite of spherical cells of PVA, PVAc microgel, and PVA—PVAc graft copolymers (113). 

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