Chapter 8 – Hyperfiltration (Reverse Osmosis)
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[1] John N. Weinstein,et al. Transport properties of charge-mosaic membranes I. Theoretical models , 1972 .
[2] S. Sourirajan,et al. Performance of some improved porous cellulose acetate membranes for low pressure reverse osmosis desalination , 1970 .
[3] R. Kesting,et al. The role of formamide in the preparation of cellulose acetate membranes by the phase inversion process , 1969 .
[4] H. Gregor,et al. POLY (STYRENE SULFONIC ACID)-POLY (VINYLIDENE FLUORIDE) INTERPOLYMER ION-EXCHANGE MEMBRANES. I. PREPARATION AND CHARACTERIZATION. , 1976 .
[5] R. Neihof,et al. The A Quantitative Electrochemical Theory of the Electrolyte Permeability of Mosaic Membranes Composed of Selectively Anion-Permeable and Selectively Cation-Permeable Parts and its Experimental Verification. I. An Outline of the Theory and its Quantitative Test in Model Systems with Auxiliary Electr , 1950 .
[6] J. Jagur-grodzinski,et al. Dynamically formed polyelectrolyte membranes on partially cured cellulose acetate , 1973 .
[7] R. Bloch,et al. The mechanism for formation of “skinned” membranes I. Structure and properties of membranes cast from binary solutions , 1970 .
[8] William P. Cooke. Hollow fiber permeators in industrial waste stream separations , 1969 .
[9] T. Coplen,et al. Ultrafiltration by a compacted clay membrane—II. Sodium ion exclusion at various ionic strengths☆☆☆ , 1973 .
[10] R. Neihof,et al. A QUANTITATIVE ELECTROCHEMICAL THEORY OF THE ELECTROLYTE PERMEABILITY OF MOSAIC MEMBRANES COMPOSED OF SELECTIVELY ANION-PERMEABLE AND SELECTIVELY CATION-PERMEABLE PARTS, AND ITS EXPERIMENTAL VERIFICATION , 1955, The Journal of general physiology.
[11] Y. Winograd,et al. Reverse osmosis in shell and tubes , 1974 .
[12] R. L. Riley,et al. Composite membranes for seawater desalination by reverse osmosis , 1971 .
[13] S. Sourirajan,et al. Characteristics of Porous Cellulose Acetate Membranes for Separation of Some Organic Substances in Aqueous Solution , 1965 .
[14] A. Hoffman,et al. Crosslinked poly(hydroxyethyl methacrylate) membranes for desalination by reverse osmosis , 1970 .
[15] A. Katchalsky,et al. Thermodynamic analysis of the permeability of biological membranes to non-electrolytes. , 1958, Biochimica et biophysica acta.
[16] U. Merten,et al. Transport properties of polyvinylpyrrolidone-polyisocyanate interpolymer membranes , 1970 .
[17] C. F. Coleman. Properties of Organic-Water Mixtures. II. Solubilities and Activity Coefficients of Sodium Chloride and Potassium Chloride in N,N-Dialkylamides Containing Water1 , 1965 .
[18] O. Kedem,et al. Hyperfiltration in charged membranes: the fixed charge model , 1967 .
[19] Shoji Kimura,et al. TRANSPORT CHARACTERISTICS OF POROUS CELLULOSE ACETATE MEMBRANES FOR THE REVERSE OSMOSIS SEPARATION OF SUCROSE IN AQUEOUS SOLUTIONS , 1968 .
[20] M. E. Nordberg. PROPERTIES OF SOME VYCOR‐BRAND GLASSES , 1944 .
[21] C. R. Peters,et al. Factors influencing reverse osmosis rejection of organic solutes from aqueous solution , 1972 .
[22] D. Bennion,et al. Mass Transport of Binary Electrolytes in Membranes. Concentration Dependence for Sodium Chloride Transport in Cellulose Acetate , 1969 .
[23] A. S. Berman. Laminar Flow in Channels with Porous Walls , 1953 .
[24] H. G. Spencer,et al. ULTRAFILTRATION OF SALT SOLUTIONS AT HIGH PRESSURES1 , 1960 .
[25] Shoji Kimura,et al. Fouling of cellulose acetate tubular reverse osmosis modules treating the industrial water in Tokyo , 1975 .
[26] David G. Thomas. Forced Convection Mass Transfer in Hyperfiltration at High Fluxes , 1973 .
[27] B. Erschler. Über die Grenzen der Anwendung der Ultrafiltration zum Nachweis des kolloiden Zustandes , 1934 .
[28] L. Dresner,et al. ION EXCLUSION AND SALT FILTERING WITH POROUS ION-EXCHANGE MATERIALS1 , 1963 .
[29] Richard W. Baker,et al. The formation mechanism of asymmetric membranes , 1975 .
[30] H. D. Cochran,et al. Hyperfiltration studies XIV Porous tubes precoated with filteraids as supports for dynamically formed membranes , 1968 .
[31] O. Kedem,et al. Transport coefficients and salt rejection in unchanged hyperfiltration membranes , 1966 .
[32] Alan S. Michaels,et al. Kinetics of water and salt transport in cellulose acetate reverse osmosis desalination membranes , 1965 .
[33] James S. Johnson,et al. Hyperfiltration of laundry wastes , 1974 .
[34] Y. Trudelle,et al. Etude de la couche dense superficielle des membranes en acetate de cellulose destinees a l'osmose inverse , 1968 .
[35] M. C. Porter. Concentration Polarization with Membrane Ultrafiltration , 1972 .
[36] G. Tanny. The surface tension of polymer solutions and asymmetric membrane formation , 1974 .
[37] M. H. Lietzke,et al. Thermodynamic properties of sea salt solutions , 1967 .
[38] Torsten Teorell,et al. An Attempt to Formulate a Quantitative Theory of Membrane Permeability , 1935 .
[39] S. Manjikian. Desalination Membranes from Organic Casting Solutions , 1967 .
[40] W. Vieth,et al. Performance of solution‐cast membranes of poly(hydroxythyl methacrylate) in osmosis and reverse osmosis , 1969 .
[41] G. Scatchard,et al. Osmotic and activity coefficients for binary mixtures of sodium chloride, sodium sulfate, magnesium sulfate, and magnesium chloride in water at 25.deg.. I. Isopiestic measurements on the four systems with common ions , 1968 .
[42] James S. Johnson,et al. Hyperfiltration studies. XI. Salt-rejection properties of dynamically formed hydrous zirconium(IV) oxide membranes , 1968 .
[43] R. L. Riley,et al. Preparation of ultrathin reverse osmosis membranes and the attainment of theoretical salt rejection , 1967 .
[44] J. O. Gardner,et al. Cellulose Acetate Membranes: Electron Microscopy of Structure , 1964, Science.
[45] H. Lonsdale,et al. Preparation and properties of poly(acrylic acid) composite membranes , 1971 .
[46] Sidney Loeb,et al. Reverse osmosis desalination costs derived from the Coalinga pilot plant operation , 1967 .
[47] Mark E. Cohen,et al. Hollow-Fiber Reverse Osmosis Membranes , 1972 .
[48] L. A. Haugseth. Status of the Yuma desalting plant , 1978 .
[49] H. Plummer,et al. Preparative techniques for the determination of reverse osmosis membrane structure by electron microscopy , 1974 .
[50] K. Sollner,et al. THE ELECTROOSMOTIC EFFECTS ARISING FROM THE INTERACTION OF THE SELECTIVELY ANION AND SELECTIVELY CATION PERMEABLE PARTS OF MOSAIC MEMBRANES. , 1964, Biophysical journal.
[51] K. Meyer,et al. La perméabilité des membranes I. Théorie de la perméabilité ionique , 1936 .
[52] James S. Johnson,et al. Concentration polarization in the reverse osmosis desalination of sea water , 1972 .
[53] C. H. Amundson,et al. USE OF ULTRAFILTRATION/REVERSE OSMOSIS SYSTEMS FOR THE CONCENTRATION AND FRACTIONATION OF WHEY , 1971 .
[54] R. Matz. The structure of cellulose acetate membranes 1. The development of porous structures in anisotropic membranes , 1972 .
[55] R. Raridon,et al. Properties of Organic-Water Mixtures. I. Activity Coefficients of Sodium Chloride, Potassium Chloride, and Barium Nitrate in Saturated Water Mixtures of Glycol, Glycerol, and Their Acetates. Model Solutions for Hyperfiltration Membranes , 1964 .
[56] David G. Thomas,et al. Membrane Fouling Part IV. Parallel operation of four tubular hyperfiltration modules at different velocities with feeds of high fouling potential , 1972 .
[57] James S. Johnson,et al. Osmotic and activity coefficients for binary mixtures of sodium chloride, sodium sulfate, magnesium sulfate, and magnesium chloride in water at 25.deg.. III. Treatment with the ions as components , 1970 .
[58] F. A. Williams. A Nonlinear Diffusion Problem Relevant to Desalination by Reverse Osmosis , 1969 .
[59] S. Srinivasan,et al. Effect of imperfect salt rejection on concentration polarization in reverse osmosis systems , 1973 .
[60] A. Katchalsky,et al. A Physical Interpretation of the Phenomenological Coefficients of Membrane Permeability , 1961, The Journal of general physiology.
[61] K. S. Spiegler,et al. Transport processes in ionic membranes , 1958 .
[62] Ulrich Merten,et al. Desalination by pressure osmosis , 1966 .
[63] C. Elata. The determination of the intrinsic characteristics of reverse osmosis membranes , 1969 .
[64] David G. Thomas,et al. Effect of high axial velocity on performance of cellulose acetate hyperfiltration membranes , 1970 .
[65] John N. Weinstein,et al. Transport properties of charge-mosaic membranes II. Experimental studies , 1973 .
[66] J. Murkes,et al. Mathematical modelling of reverse osmosis and ultrafiltration processes , 1972 .
[67] W. Holley,et al. Effect of Fillers on Wet Compressive Creep of Cellulose Acetate , 1970 .
[68] F. Morehead,et al. Skin Effect in Viscose Rayon , 1945 .
[69] L. Dresner. Ion exclusion from neutral and slightly charged pores , 1974 .
[70] P. Mazur,et al. Non-equilibrium thermodynamics of separation effects through membrane processes , 1965 .
[71] W. Pusch,et al. Relation between salt rejection r and reflection coefficient σ of asymmetric cellulose acetate membranes , 1974 .
[72] R. L. Merson,et al. Role of Protein in Reverse Osmosis of Cottage Cheese Whey , 1971 .
[73] J. S. Johnson,et al. Salt Rejection by a Porous Glass , 1966, Science.
[74] R. L. Riley,et al. Boundary-Layer Effects in Reverse Osmosis , 1964 .
[75] H. Gibbard,et al. Vapor-liquid equilibriums of synthetic seawater solutions from 25-100.deg. , 1972 .
[76] Charles E. Reid,et al. Physical characteristics of osmotic membranes of organic polymers , 1959 .
[77] U. Merten,et al. Flow Relationships in Reverse Osmosis , 1963 .
[78] Gunnar Eigil Jonsson,et al. Water and solute transport through cellulose acetate reverse osmosis membranes , 1975 .
[79] K. S. Spiegler,et al. Thermodynamics of hyperfiltration (reverse osmosis): criteria for efficient membranes , 1966 .
[80] J N Weinstein,et al. Charge-Mosaic Membranes: Enhanced Permeability and Negative Osmosis with a Symmetrical Salt , 1968, Science.
[81] Six-Month Field Test of Reverse Osmosis Desalination Membrane , 1965 .
[82] L. Dresner. Stability of the extended Nernst-Planck equations in the description of hyperfiltration through ion-exchange membranes , 1972 .
[83] Joseph W. McCutchan,et al. Systems analysis of a multi-stage tubular module reverse osmosis plant for sea water desalination , 1974 .
[84] W. Pusch. Transport coefficients of asymmetric cellulose acetate membranes , 1975 .
[85] S. Srinivasan,et al. A simplified method for the prediction of concentration polarization in reverse osmosis operation for multi-component systems , 1970 .
[86] H. Lonsdale,et al. Boron rejection by cellulose acetate reverse osmosis membranes , 1970 .
[87] W. L. Griffith,et al. Tapered plant geometry , 1972 .
[88] James S. Johnson,et al. Hyperfiltration. XXI. Dynamically formed hydrous Zr(IV) oxide-polyacrylate membranes , 1972 .
[89] H. Strathmann,et al. Control of concentration polarization in reverse osmosis desalination of water , 1969 .
[90] R. Baker,et al. A rationale for the preparation of Loeb-Sourirajan-type cellulose acetate membranes , 1971 .
[91] L. Dresner. Some remarks on the integration of the extended Nernst-Planck equations in the hyperfiltration of multicomponent solutions , 1972 .
[92] Shoji Kimura,et al. Mass Transfer Coefficients for Use in Reverse Osmosis Process Design , 1968 .
[93] K. Kraus,et al. Hyperfiltration. Application of Woven Fiber Hoses to Hyperfiltration of Salts and Crossflow Filtration of Suspended Solids , 1970 .
[94] D. Graves,et al. Transmission of water and ions through crosslinked hydrophilic membranes , 1965 .
[95] H. Yasuda,et al. Salt rejection by polymer membranes in reverse osmosis. I. Nonionic polymers , 1971 .
[96] R. Matz. The structure of cellulose acetate membranes II. The physical and transport characteristics of the porous layer of anisotropic membranes , 1972 .
[97] G. Wakley,et al. The structure of cellulose acetate membranes for reverse osmosis. Part 2. Transmission and scanning electron microscopy of membranes cast from an acetone-formamide dope , 1973 .
[98] J. Kwak,et al. Membrane potential measurements on cellulose acetate membranes , 1974 .
[99] K. Shuler,et al. The Kinetics of Membrane Processes. I. The Mechanism and the Kinetic Laws for Diffusion through Membranes , 1949 .
[100] Permeation of water and sodium chloride through cellulose acetate , 1967 .
[101] C. A. Bom,et al. The use of reverse osmosis for the treatment of Rhine river water. Part I , 1974 .
[102] S. Sourirajan,et al. Effect of casting conditions on the performance of porous cellulose acetate membranes in reverse osmosis , 1970 .
[103] W. R. Mixon,et al. Engineering development of hyperfiltration with dynamic membranes Part I. Process and module development , 1974 .
[104] R. Kesting. Semipermeable membranes of cellulose acetate for desalination in the process of reverse osmosis. I. Lyotropic swelling of secondary cellulose acetate , 1965 .
[105] H. Ohya,et al. Application of system analysis in two-stage reverse osmosis process design for water desalination☆ , 1975 .
[106] H. K. Lonsdale,et al. Phenol transport in cellulose acetate membranes , 1967 .
[107] G. Scatchard,et al. Osmotic and activity coefficients for binary mixtures of sodium chloride, sodium sulfate, magnesium sulfate, and magnesium chloride in water at 25.deg.. II. Isopiestic and electromotive force measurements on the two systems without common ions , 1969 .
[108] H. Grethlein,et al. Improved cellulose acetate membranes for reverse osmosis , 1971 .
[109] P. Parrini,et al. New polymer materials for reverse osmosis membranes , 1974 .
[110] U. Merten,et al. Lifetime of Cellulose Acetate Reverse Osmosis Membranes , 1966 .
[111] H. Ohya,et al. Reverse Osmosis Separation of Urea in Aqueous Solutions Using Porous Cellulose Acetate Membranes , 1969 .
[112] C. Tien,et al. Analysis of continuous reverse osmosis systems for desalination , 1966 .
[113] J. Halary,et al. Processus physicochimiques intervenant dans la preparation des membranes de diacetate de cellulose— recherche de criteres pour l'optimisation des performances I—Collodions renfermant des additifs mineraux , 1973 .
[114] R. J. Nunge,et al. Reverse osmosis in laminar flow through curved tubes , 1973 .
[115] S. Munari,et al. Preparation and properties of membranes obtained by radiation induced grafting of 4-vinylpyridine onto polytetrafluoroethylene films☆ , 1973 .
[116] J. W. V. Heuven,et al. Reverse osmosis by dynamically formed cation exchanger membranes , 1974 .
[117] S. Loeb,et al. Sixteen months of field experience on the Coalinga pilot plant , 1967 .
[118] R. Messalem,et al. Mechanism of Membrane Formation. VI. Convective Flows and Large Void Formation during Membrane Precipitation , 1973 .
[119] E. Glueckauf,et al. The Donnan law and its application to ion exchanger polymers , 1962, Proceedings of the Royal Society of London. Series A. Mathematical and Physical Sciences.
[120] K. C. Channabasappa. Status of reverse osmosis desalination technology , 1975 .
[121] Joseph W. McCutchan,et al. Selective Properties of High Flux Cellulose Acetate Membranes toward Ions Found in Natural Waters , 1966 .
[122] H. G. Spencer,et al. Ultrafiltration of salt solutions by ion‐excluding and ion‐selective membrances , 1960 .
[123] S. Srinivasan,et al. Reverse osmosis in multicomponent systems , 1968 .
[124] W. R. Mixon,et al. Effect of Axial Velocity and Initial Flux on Flux Decline of Cellulose Acetate Membranes in Hyperfiltration of Primary Sewage Effluents , 1972 .
[125] P. Meares,et al. Diffusion of Radiotracer Ions in a Cation‐Exchange Membrane , 1969 .
[126] O. Levenspiel,et al. The Osmotic Pump: In principle, but probably not in practice, fresh water can be extracted from our oceans for no expenditure of energy. , 1974, Science.
[127] L. Dresner. Ionic transport through porous ion-exchange membranes in hyperfiltration and piezodialysis , 1974 .
[128] S. Sourirajan. Separation of Hydrocarbon Liquids by Flow Under Pressure Through Porous Membranes , 1964, Nature.
[129] M. H. Lietzke,et al. THE BISULFATE ACID CONSTANT FROM 25 TO 225° AS COMPUTED FROM SOLUBILITY DATA1 , 1961 .
[130] A. Katchalsky,et al. Permeability of composite membranes. Part 1.—Electric current, volume flow and flow of solute through membranes , 1963 .
[131] James S. Johnson,et al. Hyperfiltration studies x. Hyperfiltration with dynamically-formed membranes☆☆☆ , 1967 .
[132] S. Srinivasan,et al. Reverse osmosis in a curved tubular membrane duct , 1971 .
[133] C. W. Saltonstall,et al. A new method for measuring diffusion coefficients of electrolytes in nonionic membranes , 1968 .
[134] Sidney Loeb,et al. Sea Water Demineralization by Means of an Osmotic Membrane , 1963 .
[135] P. L. T. Brian,et al. Concentration Polar zation in Reverse Osmosis Desalination with Variable Flux and Incomplete Salt Rejection , 1965 .
[136] G. Scatchard. The Effect of Dielectric Constant Difference on Hyperfiltration of Salt Solutions , 1964 .
[137] K. Kraus,et al. Anion Exchange Studies. V. Adsorption of Hydrochloric Acid by a Strong Base Anion Exchanger1,2 , 1953 .
[138] K. Spiegler. On the measurement of streaming potentials with silver-silver chloride electrodes , 1974 .
[139] K. Spiegler,et al. The Concentration-Clamp Method for Transport Measurements in Membranes , 1971 .
[140] K. Shuler,et al. The Kinetics of Membrane Processes. III. The Diffusion of Various Non‐Electrolytes through Collodion Membranes , 1949 .
[141] D. Spedding. Detection of Latent Fingerprints with 35SO2 , 1971, Nature.
[142] Allan Hodgson. Comparison of practical operating data and computer simulation of seawater reverse osmosis plant , 1972 .
[143] R. Kesting. Concerning the microstructure of dry‐RO membranes , 1973 .
[144] James S. Johnson,et al. Hyperfiltration studies VI. Salt rejection by dynamically-formed polyelectrolyte membranes , 1966 .
[145] John D. Sheppard,et al. Engineering development of hyperfiltration with dynamic membranes Part III. The pilot plant and its performance with brackish water feed , 1974 .
[146] A. Katchalsky,et al. Thermodynamics of flow processes in biological systems. , 1962, Biophysical journal.
[147] James S. Johnson,et al. Hyperfiltration. Concentration Polarization in Tubular Systems with Dynamically Formed Membranes , 1968 .
[148] K. Kraus,et al. Anion-exchange studies. XXIII. Activity coefficients of some electrolytes in the resin phase , 1958 .
[149] R. Raridon,et al. Properties of organic-water mixtures. IV. The effect of various salts on the miscibility gap of the glycerol triacetate-water system , 1965 .
[150] S. Sourirajan,et al. Reverse Osmosis Separation and Concentration of Sucrose in Aqueous Solutions Using Porous Cellulose Acetate Membranes , 1967 .
[151] S. Srinivasan,et al. A finite difference solution for reverse osmosis in turbulent flow , 1969 .
[152] D. Lancet,et al. An apparatus for studying the mechanism of membrane formation , 1971 .
[153] J. P. Agrawal,et al. Specification, Selectivity, and Performance of Porous Cellulose Acetate Membranes in Reverse Osmossis , 1969 .
[154] Shoji Kimura,et al. Performance of Porous Cellulose Acetate Membranes during Extended Continuous Operation under Pressure in Reverse Osmosis Process Using Aqueous Solutions , 1968 .
[155] O. Kedem,et al. Negative rejection of acids and separation of ions by hyperfiltration , 1968 .
[156] R. Probstein,et al. Brackish water salt rejection by porous hyperfiltration membranes , 1973 .
[157] J. Carter,et al. The effect of precipitating media on the performance of porous cellulose acetate reverse osmosis membranes , 1973 .
[158] Sidney Loeb,et al. Electrolytic Additives in Casting Solutions for Cellulose Acetate Desalination Membranes , 1965 .
[159] Thomas K. Sherwood,et al. Desalination by Reverse Osmosis , 1967 .
[160] J. Kopeček. Performance of Porous Cellulose Acetate Membranes for the Reverse Osmosis Separation of Mixtures of Organic Liquids , 1970 .
[161] R. D. Lanier. Properties of Organic—Water Mixtures. III. Activity Coefficients of Sodium Chloride by Cation-Sensitive Glass Electrodes1 , 1965 .
[162] M. Wyllie,et al. Salt Filtering by Ion Exchange Grains and Membranes , 1957 .
[163] S. Sourirajan,et al. Membrane Separation Studies with Some Polyoxyethylated Alkylphenols in Aqueous Solution , 1966 .
[164] R. L. Riley,et al. Replication electron microscopy of cellulose acetate osmotic membranes , 1966 .
[165] J. S. Johnson,et al. Osmotic Coefficients of Synthetic Sea-Water Solutions at 25° C. , 1966 .
[166] C. Tien,et al. Nonlinear convective diffusion: A hyperfiltration application , 1967 .
[167] L. Dresner. The Exclusion of Ions from Charged Microporous Solids1 , 1965 .
[168] M. Modell,et al. Polyacrylic desalination membranes. I. Synthesis and characterization , 1969 .
[169] W. Pusch,et al. Asymmetric behaviour of cellulose acetate membranes in hyperfiltration experiments as a result of concentration polarisation , 1970 .
[170] A. Haute,et al. Hyperfiltration by dynamically formed hydrous zirconium oxide and aluminum oxide membranes , 1972 .
[171] G. Wakley,et al. The structure of cellulose acetate membranes for reverse osmosis. Part I. Membranes prepared from a dioxan based dope , 1970 .
[172] L. Dresner. A VARIATIONAL PRINCIPLE FOR THE POISSON—BOLTZMANN EQUATION. ACTIVITY COEFFICIENT OF A SALT IN A CHARGED MICROCAPILLARY1 , 1963 .
[173] W. L. Marshall,et al. Calcium sulfate solubility in brackish water concentrates and applications to reverse osmosis processes; polyphosphate additives , 1974 .
[174] R. Matz,et al. Mechanism of Formation of Reverse Osmosis Membranes. Precipitation of Cellulose Acetate Membranes in Aqueous Solutions , 1971 .
[175] J. Anderson,et al. Mathematical analysis of factors influencing the skin thickness of asymmetric reverse osmosis membranes , 1973 .
[176] T. D. Hodgson. Selective properties of cellulose acetate membranes towards ions in aqueous solutions , 1970 .
[177] D. Landolt,et al. About the mechanism of formation of iron hydroxide fouling layers on reverse osmosis membranes , 1973 .
[178] L. Monnerie,et al. Physicochemical processes occurring during the formation of cellulose diacetate membranes, research of criteria for optimizing membrane performance. II. Influence of cellulose diacetate chain hydration on the effect of heat treatment , 1974 .
[179] Chi Tien,et al. Concentration Polarization Effects in a Reverse Osmosis System , 1965 .
[180] J. Klinowski,et al. Differential conductance coefficients in a cation-exchange membrane , 1974, Proceedings of the Royal Society of London. A. Mathematical and Physical Sciences.
[181] H.Kirk Johnston,et al. Reverse osmosis rejection of heavy metal cations , 1975 .
[182] James S. Johnson,et al. Hyperfiltration studies. III. Effect of certain metal ions on the salt filtration properties of cellophanes , 1966 .
[183] Lars Onsager,et al. The Surface Tension of Debye‐Hückel Electrolytes , 1934 .
[184] O. Kedem,et al. The mechanism for formation of “skinned” membranes , 1970 .
[185] James S. Johnson,et al. Hyperfiltration Studies. IV. Salt Rejection by Dynamically Formed Hydrous Oxide Membranes1 , 1966 .
[186] L. Dresner. Geometric effects in piezodialysis through charge-mosaic membranes , 1972 .
[187] Issam Jamjoom,et al. The world's first large seawater reverse osmosis desalination plant, at Jeddah, Kingdom of Saudi Arabia , 1978 .
[188] S. Sourirajan,et al. Reverse Osmosis Separation of Some Inorganic Salts in Aqueous Solution Using Porous Cellulose Acetate Membranes , 1966 .
[189] S. Kimura,et al. Correlations of Reverse Osmosis Separation Data for the System Glycerol-Water Using Porous Cellulose Acetate Membranes , 1967 .
[190] James S. Johnson,et al. Hyperfiltration studies XVI: Salt filtration by dynamically formed and cast poly (glutamic acid) and poly (acrylic acid) membranes☆☆☆ , 1969 .
[191] A. Acrivos,et al. Concentration Polarization in Reverse Osmosis under Natural Convection , 1969 .
[192] R. L. Riley,et al. Kinetic study of the hydrolysis of cellulose acetate in the pH range of 2–10 , 1966 .
[193] Thomas K. Sherwood,et al. Salt Concentration at Phase Boundaries in Desalination by Reverse Osmosis , 1965 .
[194] S. G. Kimura. Reverse Osmosis Performance of Sulfonated Poly(2,6-dimethylphenylene Ether) Ion Exchange Membranes , 1971 .
[195] D. G. Thomas,et al. Concentration-Gradient-Driven Convection: Experiments , 1968, Science.
[196] S. Srinivasan,et al. Correction to “reverse osmosis in a curved tabular membrane duct” , 1973 .
[197] S. Sourirajan. Mechanism of Demineralization of Aqueous Sodium Chloride Solutions by Flow, under Pressure, through Porous Membranes , 1963 .
[198] E. Meinecke,et al. Influence of some processing variables on the properties of cellulose acetate membranes I. Ultimate properties and birefringence , 1972 .
[199] Charles E. Reid,et al. Water and ion flow across cellulosic membranes , 1959 .
[200] J. Ferry,et al. Ultrafilter Membranes and Ultrafiltration. , 1936 .
[201] T. J. Larson. Reverse osmosis pilot plant operation: A spiral module concept , 1970 .
[202] M. H. Lietzke,et al. Calculation of Some Thermodynamic Properties of Sea Salt Solutions at Elevated Temperatures from Data on NaCI Solutions. , 1965 .
[203] Sidney Loeb. A composite tubular assembly for reverse osmosis desalination , 1966 .
[204] A. Solan,et al. Concentration build-up in reverse osmosis in turbulent flow , 1969 .
[205] R. L. Riley,et al. Transport properties of cellulose acetate osmotic membranes , 1965 .
[206] Robert M Keller,et al. Turbulence promoters for hyperfiltration with dynamic membranes. , 1970, Environmental science & technology.
[207] C. Peri,et al. REVERSE OSMOSIS OF COTTAGE CHEESE WHEY 2. Influence of Flow Conditions , 1971 .
[208] John Roger Grover,et al. Development and field trial evaluation of a new reverse osmosis module system , 1974 .
[209] K. Umezawa,et al. Piezodialysis: styrene-butadiene copolymer membranes , 1974 .
[210] G. L. Hassler,et al. Osmosis through a Vapor Gap Supported by Capillarity , 1960 .
[211] H. D. Cochran,et al. Hyperfiltration. Processing of pulp mill sulfite wastes with a membrane dynamically formed from feed constituents , 1967 .