LIQUID-LIQUID PHASE SEPARATION IN MULTICOMPONENT POLYMER SYSTEMS .10. CONCENTRATION DEPENDENCE OF PAIR INTERACTION PARAMETER IN SYSTEM CYCLOHEXANE-POLYSTYRENE
LIQUID-LIQUID PHASE SEPARATION IN MULTICOMPONENT POLYMER SYSTEMS .10. CONCENTRATION DEPENDENCE OF PAIR INTERACTION PARAMETER IN SYSTEM CYCLOHEXANE-POLYSTYRENE
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DOI:
10.1021/ma60023a026
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发表时间:
1971-01-01
期刊:
影响因子:
5.5
通讯作者:
KLEINTJENS, LA
中科院分区:
文献类型:
--
作者:
KONINGSVELD, R;KLEINTJENS, LA
ConclusionsTypical flux-rejection data for the membrane systems de-scribed, with various feed solutions, are summarized in Table V. These aromatic polyamide membranes are characterized by their good mechanical strength, as illustrated in Figure 7. Here a comparison of flux-pressure response between polymer I and celluloseacetate is made. A straight line plot for flux is observed up to pressures of 1800 psi, with some departure from linearity evident after 1 hr. The deflection in the flux line for celluloseacetate is seen to coincide with a decrease in rejection, indicating development of a membrane defect. Typical mechanical properties for asymmetric membranes prepared from these polymers are shown in Table VI. In addition to their good mechanical properties, these aromatic polyamides show remarkable chemical resistance, especially in the high-pH range. This is in marked contrast to the cellulose acetate systems. 1 23456789 Membrane reverse osmosis per-formance for aqueous salt rejections appears unaltered after 1 week of storage in 1 A solutions of H2S04, HC1, HNOs, CHsCOOH, NaOH, andNH4OH. Selectivity of these membranes to solutes other than NaCl is quite good, as illustrated by results for polymer III in Table VII.Acknowledgments. The authors wish to thank Dr. J. R. Holsten for his assistance in preparing the polymers used in this study andMessrs. L. C. Locust and P. B. Woodson and Mrs. N. Wildman for their contributions in carrying out the measurements described. Additional thanks are due Dr. VF Holland for his assistance in carrying out the electron microscopy. This work was carried out under Contract No. 14-01-0001-1720 granted by the Office of Saline Water, Membrane Division, U. S. Department of the Interior.