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Membrane layer

By changing the enzyme and mediator, the amperometric sensor in Figure 11.39 is easily extended to the analysis of other substrates. Other bioselective materials may be incorporated into amperometric sensors. For example, a CO2 sensor has been developed using an amperometric O2 sensor with a two-layer membrane, one of which contains an immobilized preparation of autotrophic bacteria. As CO2 diffuses through the membranes, it is converted to O2 by the bacteria, increasing the concentration of O2 at the Pt cathode. [Pg.520]

The simulations to investigate electro-osmosis were carried out using the molecular dynamics method of Murad and Powles [22] described earher. For nonionic polar fluids the solvent molecule was modeled as a rigid homo-nuclear diatomic with charges q and —q on the two active LJ sites. The solute molecules were modeled as spherical LJ particles [26], as were the molecules that constituted the single molecular layer membrane. The effect of uniform external fields with directions either perpendicular to the membrane or along the diagonal direction (i.e. Ex = Ey = E ) was monitored. The simulation system is shown in Fig. 2. The density profiles, mean squared displacement, and movement of the solvent molecules across the membrane were examined, with and without an external held, to establish whether electro-osmosis can take place in polar systems. The results clearly estab-hshed that electro-osmosis can indeed take place in such solutions. [Pg.786]

Controlled removal of the template is especially important when zeolite based membranes are involved consisting of a continuous MFI layer on a ceramic or sintered metal support (ref. 14). In these novel composite ceramic membranes the formation of cracks during template removal would be detrimental. The unique properties (ref. 14) of metal-supported MFl-layer membranes prove that indeed crack formation can be essentially prevented. [Pg.208]

Locke, BR Arce, P Park, Y, Applications of Self-Adjoint Operators to Electrophoretic Transport, Enzyme Reactions, and Microwave Heating Problems in Composite Media—II. Electrophoretic Transport in Layered Membranes, Chemical Engineering Science 48, 4007, 1993. [Pg.615]

Aqueous Apical Tight Basolateral Aqueous Bulk Boundary Layer Membrane Junction Membrane Boundary Layer Bulk... [Pg.314]

Fig. 4.8. (Below) A diagram of the bilipid layer membrane of a vesicle or a cell with (above) a typical lipid, phosphatidylcholine. Large molecules and ions cannot penetrate the membrane as illustrated by the ions surrounding and inside a cell, but the distribution is reversed in vesicles (see Chapter 7). The ions create chemical and electrical field gradients across the membrane. Fig. 4.8. (Below) A diagram of the bilipid layer membrane of a vesicle or a cell with (above) a typical lipid, phosphatidylcholine. Large molecules and ions cannot penetrate the membrane as illustrated by the ions surrounding and inside a cell, but the distribution is reversed in vesicles (see Chapter 7). The ions create chemical and electrical field gradients across the membrane.
Successive H-bond urea self-assembly of 4 and sol-gel transcription steps yield preferential conduction pathways within the hybrid membrane materials. Crystallographic, microscopic and transport data confirm the formation of self-organized molecular channels transcribed in solid dense thin-layer membranes. The ionic transport across the organized domains illustrates the power of the supramolecular approach for the design of continual hydrophilic transport devices in hybrid membrane materials by self-organization (Figure 10.8) [42-44]. [Pg.321]

Teramura Y, Kaneda Y, Iwata H (2007) Islet-encapsulation in ultra-thin layer-by-layer membranes of poly(vinyl alcohol) anchored to poly(ethylene glycol)-lipids in the cell membrane. Biomaterials 28 4818 -825... [Pg.199]

Myelin in situ has a water content of about 40%. The dry mass of both CNS and PNS myelin is characterized by a high proportion of lipid (70-85%) and, consequently, a low proportion of protein (15-30%). By comparison, most biological membranes have a higher ratio of proteins to lipids. The currently accepted view of membrane structure is that of a lipid bilayer with integral membrane proteins embedded in the bilayer and other extrinsic proteins attached to one surface or the other by weaker linkages. Proteins and lipids are asymmetrically distributed in this bilayer, with only partial asymmetry of the lipids. The proposed molecular architecture of the layered membranes of compact myelin fits such a concept (Fig. 4-11). Models of compact myelin are based on data from electron microscopy, immunostaining, X-ray diffraction, surface probes studies, structural abnormalities in mutant mice, correlations between structure and composition in various species, and predictions of protein structure from sequencing information [4]. [Pg.56]

Ultrastructural examination of nuclei in situ showed they were not surrounded by a continuous double-layered membrane, but that the membrane was interrupted by pores (Callan and Tomlin, 1950). These were not holes but were highly organized structures involved in transport between the nucleus and the cytosol. [Pg.157]

Another in vitro method for permeability screening was parallel artificial membrane permeation assay (PAMPA) initially reported by Kansy. In a PAMPA permeability screen, the Caco-2 cell mono-layer membrane is replaced by an artificially generated membrane. Versions of different artificial membranes that lack active transporter systems and pores have been developed to mimic the in vivo transcellular intestinal epithelial cell barrier. Therefore, the PAMPA screen only measures the intrinsic... [Pg.423]

Jain, Biegler, and Jhon [126] optimized Pt distribution along the width of the CL and found that a significant improvement in current density could be obtained by placing higher amounts of Pt adjacent to the catalyst layer/membrane interface. [Pg.93]

Such new approaches to the diffusion layer increase its importance in the fuel cell as a critical component along with the catalyst layer, membrane, and flow field. [Pg.288]

Another possible solution to the problem of analyzing multiple-layered membrane composites is a newly developed method using NMR spin-lattice relaxation measurements (Glaves 1989). In this method, which allows a wide range of pore sizes to be studied (from less than 1 nm to greater than 10 microns), the moisture content of the composite membrane is controlled so that the fine pores in the membrane film of a two-layered composite are saturated with water, but only a small quantity of adsorbed water is present in the large pores of the support. It has been found that the spin-lattice relaxation decay time of a fluid (such as water) in a pore is shorter than that for the same fluid in the bulk. From the relaxation data the pore volume distribution can be calculated. Thus, the NMR spin-lattice relaxation data of a properly prepared membrane composite sample can be used to derive the pore size distribution that conventional pore structure analysis techniques... [Pg.76]

It is evident, that in any membrane reactor operation mode there are important parameters which determine the performance of the process (Shah, Remmen and Chiang 1970). These are (1) the total and partial pressures on both sides of the membrane, (2) the total and partial pressure differences across the membrane, (3) the diffusion mechanism through the support and the membrane layer (membrane structure), (4) the thickness of the membrane, (5) the reactant configuration (i.e. whether the reactants are supplied from the same or from opposite sides of the membrane, in counter or co-current flow) and (6) the catalyst distribution. [Pg.124]

Three-layer membrane tube (in module configuration, 10 tubes per module, heat exchanger type). [Pg.126]

Figure 11. Tafel plot of flooded porous-electrode simulation results for the cathode at three different values of xp = 2.2nFIfQ 2 02, z=dbK. The z coordinate ranges from 0 (catalyst layer/membrane interface) to L (catalyst layer/diffusion medium interface), the dimensionless overpotential is defined as // = —o FIRT r]oRR, - ), and the ORR rate constant is defined as A = hFFq 2 (Reproduced with permission from ref 36. Copyright 1998 The Electrochemical Society, Inc.)... Figure 11. Tafel plot of flooded porous-electrode simulation results for the cathode at three different values of xp = 2.2nFIfQ 2 02, z=dbK. The z coordinate ranges from 0 (catalyst layer/membrane interface) to L (catalyst layer/diffusion medium interface), the dimensionless overpotential is defined as // = —o FIRT r]oRR, - ), and the ORR rate constant is defined as A = hFFq 2 (Reproduced with permission from ref 36. Copyright 1998 The Electrochemical Society, Inc.)...
Figure 5.25 — Flow-through ion-selective optrode based on a multilayer lipidic membrane prepared by the Langmuir-Blodgett method. (A) Cross-sectional view of the composite six-layer membrane (four layers of arachidic acid/ valinomycin covered by an arachidic acid and rhodamine dye bilayer). (B) Optical arrangement integrated with the sensor, which is connected to a flow system. LS light source Ml and M2 excitation and emission monochromator, respectively FI and F2 primary filters M mirror LB lipid-sensitive membrane in a glass platelet FC flow-cell A amplifier D display P peristaltic pump. (Reproduced from [107] with permission of the Royal Society of Chemistry). Figure 5.25 — Flow-through ion-selective optrode based on a multilayer lipidic membrane prepared by the Langmuir-Blodgett method. (A) Cross-sectional view of the composite six-layer membrane (four layers of arachidic acid/ valinomycin covered by an arachidic acid and rhodamine dye bilayer). (B) Optical arrangement integrated with the sensor, which is connected to a flow system. LS light source Ml and M2 excitation and emission monochromator, respectively FI and F2 primary filters M mirror LB lipid-sensitive membrane in a glass platelet FC flow-cell A amplifier D display P peristaltic pump. (Reproduced from [107] with permission of the Royal Society of Chemistry).
An interesting feature of the structure of Nitrobacter is the presence of several double-layered membranes... [Pg.1052]

The theory of composite membranes with one active layer whose permeability varies with solute concentration is developed. The case of exponential dependence of permeability on concentration is treated in detail, but the case of a general dependence follows the same pattern and leads to the treatment of multi-layered membranes. [Pg.345]

Cell Membrane 10-20 nm Doubled-layered membrane main semi-permeable barrier of cell 5-10% of cell dry wt 50% protein, 30% lipid and 20% carbohydrate... [Pg.265]

Cell membrane 0.007-0.01 Much-folded, double-layered membrane semipermeabie to nutrients... [Pg.267]


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Alterations in Electrical Double Layer Structure by an External Field Coupling to the Membrane

Asymmetric membranes with porous separation layer, structure

Bilipid layer membrane 155

Biological membranes unstirred water layer

Boundary layer, membrane extraction

Catalyst Layers for Anion Exchange Membrane Fuel Cells

Catalyst layer membrane degradation

Cation exchange membranes layers

Cell membrane Lipid layers

Composite membranes support layer, importance

Double-layered membrane cross section

Double-layered membranes

Dual-layer asymmetric hollow fiber membranes

Dual-layer hollow fiber membranes

Dual-layer hollow fiber membranes mixed-matrix

Dual-layer membranes

Envelope membrane inner layer

Gas-diffusion layer membrane

Hollow fiber membrane single-layer asymmetric

Integrally-skinned membranes skin layer

Integrally-skinned membranes substrate layer

LB Membranes for the Alignment Layer

Layer on membrane

Layer shrinkage membranes

Layered bulk liquid membrane modules

Layered membrane

Layered membrane

Layers, unstirred near membranes

Membrane Boundary Layer Concentrations

Membrane barrier layers

Membrane biomimetic layer

Membrane encapsulated soil layers

Membrane filtration concentration polarization boundary layer

Membrane filtration layers

Membrane layer visualization

Membrane lipids boundary layer

Membrane methods steady layers

Membrane mucous layer

Membrane selective layer thickness

Membrane-electrode assembly catalyst layer

Membranes aleurone layer

Membranes carboxylate layer

Membranes gel layer

Membranes hydrophilic layers

Membranes layer phase formation

Membranes permselective layer

Membranes selective layers

Membranes separation layer

Photocatalytic membranes separation layer

Polymeric membranes layer

Porous layers, membrane wafer

Procedures for Analyzing the Fouling Layer Structure During a Membrane Filtration Process

Proton exchange membrane fuel cell catalyst layers

Reverse osmosis membranes barrier layer

Reverse osmosis membranes layer

S-layers ultrafiltration membranes

Thin layer chromatography membranes

Thin selective membrane layers

Tissue layers basement membrane

Two-layer membrane

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