THIN FILM COMPOSITE POLYAMIDE MEMBRANE PARAMETERS ESTIMATION FOR PHENOL-WATER SYSTEM BY REVERSE OSMOSIS
暂无分享,去创建一个
[1] E. B. Besselievre,et al. The Treatment of Industrial Wastes. , 1978, American journal of public health and the nation's health.
[2] M. Kurihara,et al. Development of the pec-1000 composite membrane for single-stage seawater desalination and the concentration of dilute aqueous solutions containing valuable materials , 1981 .
[3] James S. Johnson,et al. Hyperfiltration studies x. Hyperfiltration with dynamically-formed membranes☆☆☆ , 1967 .
[4] Gunnar Eigil Jonsson,et al. Overview of theories for water and solute transport in9 UF/RO membranes , 1980 .
[5] W. Pusch,et al. Characterization of transport across cellulose acetate membranes in the presence of strong solute–membrane interactions , 1980 .
[6] R. L. Fox,et al. Spiral-wound poly (ether/amide) thin-film composite membrane systems , 1976 .
[7] S. Gupta,et al. Modelling of protein transmission through ultrafiltration membranes , 1994 .
[8] S. Mahajan. Pollution Control in Process Industries , 1987 .
[9] Shoji Kimura,et al. Selective transport mechanism through the reverse osmosis membrane , 1984 .
[10] C. Cooney,et al. Study of protein transmission through ultrafiltration membranes , 1993 .
[11] G. Jonsson. Methods for determining the selectivity of reverse osmosis membranes , 1977 .
[12] A. E. Greenberg,et al. Standard methods for the examination of water and wastewater : supplement to the sixteenth edition , 1988 .
[13] R. L. Riley,et al. Transport properties of cellulose acetate osmotic membranes , 1965 .
[14] C. R. Peters,et al. Factors influencing reverse osmosis rejection of organic solutes from aqueous solution , 1972 .
[15] H. Lonsdale,et al. Permeability of cellulose acetate membranes to selected solutes , 1971 .
[16] Takeshi Matsuura,et al. Physicochemical criteria for reverse osmosis separation of alcohols, phenols, and monocarboxylic acid in aqueous solutions using porous cellulose acetate membranes , 1971 .
[17] K. S. Spiegler,et al. Thermodynamics of hyperfiltration (reverse osmosis): criteria for efficient membranes , 1966 .
[18] Zagabathuni Venkata Panchakshari Murthy,et al. Estimation of mass transfer coefficient using a combined nonlinear membrane transport and film theory model , 1997 .
[19] Shoji Kimura,et al. Analysis of data in reverse osmosis with porous cellulose acetate membranes used , 1967 .
[20] Takeshi Matsuura,et al. Reverse osmosis separation of phenols in aqueous solutions using porous cellulose acetate membranes , 1972 .
[21] W. Gill,et al. REVIEW OF REVERSE OSMOSIS MEMBRANES AND TRANSPORT MODELS , 1981 .
[22] James V. Beck,et al. Parameter Estimation in Engineering and Science , 1977 .
[23] W. Pusch,et al. Determination of Transport Parameters of Synthetic Membranes by Hyperfiltration Experiments Part I: Derivation of Transport Relationship from the Linear Relations of Thermodynamics of Irreversible Processes , 1977 .
[24] A. Katchalsky,et al. Thermodynamic analysis of the permeability of biological membranes to non-electrolytes. , 1958, Biochimica et biophysica acta.
[25] A. Zydney,et al. Diffusive and convective protein transport through asymmetric membranes , 1991 .
[26] Z. Murthy,et al. Simple Graphical Method to Estimate Membrane Transport Parameters and Mass Transfer Coefficient in a Membrane Cell , 1996 .
[27] H. K. Lonsdale,et al. Phenol transport in cellulose acetate membranes , 1967 .