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  • 11
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Journal of Applied Polymer Science 19 (1975), S. 2889-2895 
    ISSN: 0021-8995
    Keywords: Chemistry ; Polymer and Materials Science
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Mechanical Engineering, Materials Science, Production Engineering, Mining and Metallurgy, Traffic Engineering, Precision Mechanics , Physics
    Notes: The order of ion separation by the NS-100 membrane differed slightly from that of the cellulose acetate membrane. The separation of an ion by the NS-100 membrane increased with increase in the valence of the ion, but decreased with the increase in the ionic radius. The sole criterion determining this separation order for the NS-100 membrane was the enthalpy of hydration. An ion having a higher enthalpy of hydration is bulkier in the hydrated form and is, therefore, separated more effectively by the NS-100 membrane, according to the diffusional model of solute separation. The permeability of an ion through the membrane material can be related to its enthalpy of hydration. By using this relationship, the separation of individual ions in aqueous solution with a given NS-100 membrane can be predicted from a test with a sodium chloride solution.
    Additional Material: 4 Ill.
    Type of Medium: Electronic Resource
    Library Location Call Number Volume/Issue/Year Availability
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  • 12
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Journal of Applied Polymer Science 19 (1975), S. 1347-1358 
    ISSN: 0021-8995
    Keywords: Chemistry ; Polymer and Materials Science
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Mechanical Engineering, Materials Science, Production Engineering, Mining and Metallurgy, Traffic Engineering, Precision Mechanics , Physics
    Notes: Removal of alcohols, amines, and aliphatic acids in single-solute aqueous solution in the concentration range from 0.001 to 0.01M have been studied using the NS-100 membrane. All the tests were conducted at 600 psig, 25°C, and a flow rate of 0.30 gpm. The mechanism of solute separation by the NS-100 membrane differs from that of the cellulose acetate membrane. There was no significant correlation between the removal and the hydrogen bonding ability of the organic solute. Instead, for a given organic solute, its removal increases with the increases in the degree of crosslinkage of the skin layer of NS-100 membrane, and is proportional to its degree of ionization (or degree of dissociation). For organic compounds having a same functional group, the removal of a compound increases with the increase in molecular weight and/or molecular branching. All of these are attributable to the relative nonpolarity and the anion exchanger characteristics of the membrane as well as to the steric resistance for the solute to permeate through the membrane.
    Additional Material: 10 Ill.
    Type of Medium: Electronic Resource
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  • 13
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Journal of Applied Polymer Science 20 (1976), S. 303-314 
    ISSN: 0021-8995
    Keywords: Chemistry ; Polymer and Materials Science
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Mechanical Engineering, Materials Science, Production Engineering, Mining and Metallurgy, Traffic Engineering, Precision Mechanics , Physics
    Notes: The optimization of a newly developed reverse osmosis membrane, NS-100, was studied based upon two series of statistically designed experiments. A total number of 33 experiments was run to evaluate the effects and interaction effects of five independent casting variables. With the aid of a constrained optimization method, SUMT algorithm, the optimum conditions for all casting variables were determined. Flat-sheet membranes cast under these conditions yielded a permeate flux of 10.30 ± 1.95 gal/ft2-day (gfd) and a 99.30 ± 0.18% rejection of salt under a pressure of 600 ib/in.2 (psig). Tubular membranes, on the other hand, yielded a flux of 10.13 ± 3.19 gfd and a 98.51 ± 0.66% rejection of salt. These performances evidently indicate that the optimized NS-100 membrane is superior to those previously developed. The satisfactory performance of tubular membranes indicates the feasibility of applying the results found in this study for the fabrication of tubular modules.
    Additional Material: 3 Ill.
    Type of Medium: Electronic Resource
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