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CO membranes

Table 6.6 The properties ofthe Tokuyama Soda Co. membranes, used in the referenced works... [Pg.304]

Figure 3.11 Schematic diagram of the construction of the Asahi Chemical Co, membrane cell... Figure 3.11 Schematic diagram of the construction of the Asahi Chemical Co, membrane cell...
An example of the active transport of Na through poly-(1 -co- ) membrane is shown in Figure 2. In this case, the driving force for the transport of metal ions is considered to be the concentration gradient. The transport rate of metal ions was proportional to the concentration. [Pg.319]

An example of the time-transport curves of Na " is shown in Figure 8. The mechanism of the active transport is considered to be similar to the case of poly(l -co- ) membrane. The active transportability of the present membrane was also observed under the condition that the initial concentration was 1.0x10 mol dm . ... [Pg.323]

The initial condition and the maximum values of the concentration of Na" by the active transport with the present membrane and poly (]L-co- ) are summarized in Table 3. The present membrane has high capability to transport of Na " even at a low concentration, in contrast to the poly(1 -co- ) membrane. [Pg.323]

The interest in vesicles as models for cell biomembranes has led to much work on the interactions within and between lipid layers. The primary contributions to vesicle stability and curvature include those familiar to us already, the electrostatic interactions between charged head groups (Chapter V) and the van der Waals interaction between layers (Chapter VI). An additional force due to thermal fluctuations in membranes produces a steric repulsion between membranes known as the Helfrich or undulation interaction. This force has been quantified by Sackmann and co-workers using reflection interference contrast microscopy to monitor vesicles weakly adhering to a solid substrate [78]. Membrane fluctuation forces may influence the interactions between proteins embedded in them [79]. Finally, in balance with these forces, bending elasticity helps determine shape transitions [80], interactions between inclusions [81], aggregation of membrane junctions [82], and unbinding of pinched membranes [83]. Specific interactions between membrane embedded receptors add an additional complication to biomembrane behavior. These have been stud-... [Pg.549]

The method has severe limitations for systems where gradients on near-atomic scale are important (as in the protein folding process or in bilayer membranes that contain only two molecules in a separated phase), but is extremely powerful for (co)polymer mixtures and solutions [147, 148, 149]. As an example Fig. 6 gives a snapshot in the process of self-organisation of a polypropylene oxide-ethylene oxide copolymer PL64 in aqueous solution on its way from a completely homogeneous initial distribution to a hexagonal structure. [Pg.27]

Watanabe and co-workers described a new membrane electrode for the determination of cocaine, which is a weak base alkaloid with a piC of 8.64d The response of the electrode for a fixed concentration of cocaine was found to be independent of pH in the range of 1-8, but decreased sharply above a pH of 8. Offer an explanation for the source of this pH dependency. [Pg.536]

Tacoma, Wash. Cedar Chemical Co. 82.6 1929 ICI FM21 membrane 85 1... [Pg.479]

Asahi Chemical Membrane Chlor—Alkali Process, Asahi Chemical Industry Co., Ltd., Tokyo, Japan, 1987. [Pg.520]

Polymer Electrolyte Fuel Cell. The electrolyte in a PEFC is an ion-exchange (qv) membrane, a fluorinated sulfonic acid polymer, which is a proton conductor (see Membrane technology). The only Hquid present in this fuel cell is the product water thus corrosion problems are minimal. Water management in the membrane is critical for efficient performance. The fuel cell must operate under conditions where the by-product water does not evaporate faster than it is produced because the membrane must be hydrated to maintain acceptable proton conductivity. Because of the limitation on the operating temperature, usually less than 120°C, H2-rich gas having Htde or no ([Pg.578]

J. C. Gomez and co-workers. Progress in Membrane biotechnology, Birkhauser Vedag, Boston, 1991. [Pg.156]

R. W. Baker and co-workers. Membrane Separation Systems, Recent Developments and Future Directions, Noyes Data Corp., Park Ridge, N.J., 1991. [Pg.156]

W. C. Hiatt and co-workers, in D. R. Lloyd, ed.. Materials Science of Synthetic Membranes, ACS Symposium Series 269, American Chemical Society,... [Pg.89]

L. T. RozeUe and co-workers, in S. Sourirajan, ed.. Reverse Osmosis and Synthetic Membranes, National Research Council of Canada Pub. NRCC 15627, Ottawa, 1977, pp. 249—262. [Pg.89]

A. H. BaHweg and co-workers, "Pervaporation Membranes," Proceedings of the Fifth InternationalMlcohol Fuels Symposium, Auckland, New Zealand, May 13—18, John Mclndoe, Dunedin, New Zealand, 1982. [Pg.90]

T. Hodder, P. Crewther, M. Lett, and co-workers, "Apical Membrane Antigen 1 A potential Malaria Vaccine Candidate," 7th Malaria Meeting of British Society ofParasilolgy, London, Sept. 19—21,1995. [Pg.363]


See other pages where CO membranes is mentioned: [Pg.344]    [Pg.581]    [Pg.47]    [Pg.75]    [Pg.35]    [Pg.217]    [Pg.158]    [Pg.61]    [Pg.344]    [Pg.581]    [Pg.47]    [Pg.75]    [Pg.35]    [Pg.217]    [Pg.158]    [Pg.61]    [Pg.546]    [Pg.2502]    [Pg.2697]    [Pg.146]    [Pg.201]    [Pg.201]    [Pg.479]    [Pg.520]    [Pg.322]    [Pg.579]    [Pg.586]    [Pg.145]    [Pg.155]    [Pg.463]    [Pg.69]    [Pg.82]    [Pg.89]    [Pg.564]    [Pg.298]    [Pg.200]    [Pg.157]    [Pg.102]    [Pg.249]   
See also in sourсe #XX -- [ Pg.352 ]




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Recent High Performance Polymer Membranes for CO

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