A Commemorative Issue in Honor of Victor Starov: Influence of Surface Forces on Membrane Separations

A special issue of Membranes (ISSN 2077-0375). This special issue belongs to the section "Membrane Surfaces and Interfaces".

Deadline for manuscript submissions: closed (28 February 2022) | Viewed by 25772

Special Issue Editors


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Guest Editor
Department of Higher Mathematics, National University of Oil and Gas “Gubkin University”, Leninsky Prospect, 65-1, Moscow 119991, Russia
Interests: mathematical modelling of reverse osmosis, nano-, ultra-, microfiltration and electrodialysis; interaction between colloidal particles and charged membrane surface; asymmetry of transport characteristics of step-charged bi-layer and linearly-charged one-layer membranes; hybrid and nanocomposite membranes; modelling of complex porous media (like ion-exchange membranes) using the cell method; magnetic and electric field action on Newtonian and non-Newtonian (micropolar) fluid flows through a porous membrane

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Guest Editor
Department of Environmental Engineering, Istanbul University-Cerrahpaşa, 34452 Istanbul, Turkey
Interests: water chemistry; membrane electrolyzer; water splitting; wastewater treatment and reuse; separation and purification technologies; electrodialysis; desalination; control of membrane fouling; membrane pre-treatment processes; membrane processes; recovery of waste liquors; ion exchange membrane; ion exchange resins; coating technologies; self-cleaning nano-films; cost analysis of reuse; circular economy; solar treatment

Special Issue Information

Dear Colleagues,

Our journal is pleased to publish a Special Issue in honour of Professor Victor Mikhailovich Starov, Doctor of Science in Chemistry, Fellow of the Royal Society of Chemistry. Victor is a Professor at the Department of Chemical Engineering, Loughborough University, UK. June 14, 2021 will be the 75th birthday of Professor Starov.

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Victor graduated from Moscow State University in 1969. He was awarded his PhD entitled “Capillary Hysteresis and the Structure of Isotropic Porous Media” in 1973 by USSR Academy of Sciences and Doctor of Sciences “Equilibrium and Kinetics of Thin Liquid Layers” in 1981 by Petersburg University. Starting in 1974, over many years, Victor has collaborated in his research with Fellow of Russia Academy of Sciences B.V. Derjaguin and Profs. N.V. Churaev, V.D. Sobolev, and other colleagues from the Institute of Physical Chemistry, USSR Academy of Sciences (now Frumkin Institute of Physical Chemistry and Electrochemistry, Russian Academy of Sciences).

In 1983, Victor became the head of the Department of Pure and Applied Mathematics, Moscow State University of Food Production, where, in addition to teaching, he was involved in research together with A.N. Filippov, V.V. Kalinin, V.I. Ivanov, S.I. Vasin, and Yu.E. Solomentsev. After the collapse of the Soviet Union, Victor worked for about three years as a Visiting Professor at the Department of Chemical Engineering, University of Texas at Austin (US), then in Toulouse University (France), Instituto Pluridisciplinar (Madrid, Spain), and in Swansea University of Wales (UK). In 1998, he moved permanently to the Department of Chemical Engineering, Loughborough University (UK) as a Professor in Chemical Engineering.

For many years, Victor was involved in various aspects of membrane separation, including reverse osmosis, ultra- and microfiltration, and electrodialysis. He organised Special Issues of Advances in Colloid and Interface Science and Journal of Membrane Science, which published a collection of papers of membrane scientists from Russia and later co-organised the publication of a Special Issue of Desalination journal with Professor Gangasalam Arthanareeswaran, which published a collection of papers presented by membrane scientists from India. In the case of reverse osmosis, Victor determined the maximum value of the rejection coefficient and corresponding optimum velocity of filtration, which were calculated through all physico-chemical parameters of the process. The negative rejection of some ions from the mixture is explained, as well as a change in the pH of the permeate. The streaming potential is calculated as a function of Peclet number, distribution coefficients, membrane charge; a theory of reverse osmosis of multicomponent electrolyte solutions was developed and verified against available experimental data, which demonstrated very good agreement between the theory predictions and experimental data. Victor developed a theory of the formation and compressibility of cake layers formed on membrane surfaces during ultra- and microfiltration based on colloidal interactions between particles and membranes, and a new theory of the sieve mechanism of microfiltration was suggested, which was verified by experimental investigations. A new phenomenon of concentration of electrolytes in the permeate during ultrafiltration in the presence of polyelectrolytes in the feed solution was predicted and verified. Victor investigated the electrodialysis of bilayer membranes and predictions were verified against experimental data.

Victor also studied, in detail, the simultaneous action of capillary forces and disjoint pressure in thin liquid layers and a transition zone (in the vicinity of liquid layers near the three-phase contact line) under equilibrium, quasi-equilibrium, and dynamic conditions. This made it possible to identify stability conditions of the transition zone, to predict the existence and stability of equilibrium non-flat liquid layers, to investigate the influence of the roughness of the solid surface on the measured values of the disjoining pressure, and to predict an instability threshold for thin liquid layers on outer cylindrical or spherical surface in the case of complete wetting. He explained the phenomenon of static hysteresis of contact angle on a smooth homogeneous surface that allowed him to calculate both advancing and receding contact angles via the disjoining pressure isotherm and to predict the presence of thick films behind receding meniscus (the latter phenomenon was discovered and studied by N.V. Churaev and his group).

Victor expressed the line tension via the disjoining pressure and calculated its value; he studied the deformation of soft solids caused by the disjoining pressure in the transition zone. He also predicted both the exponent and pre-exponential factor in the spreading law in the case of complete wetting (excellent agreement between theory and experimental data was disclosed later); he investigated the motion of bubbles and oil droplets in thin cylindrical and/or tapered capillaries under the applied pressure or temperature gradient.

Together with his colleagues, Starov predicted the adsorption of surfactant molecules on bare hydrophobic surfaces in front of moving aqueous surfactant solutions. This allowed them to formulate and experimentally confirm the kinetics of spreading of surfactant solutions over hydrophobic surfaces and the imbibition of surfactant solutions into hydrophobic capillaries.

Victor developed a new theory of the spreading of liquids over dry and liquid-saturated porous substrates. Based on this theory, the universal law of spreading was predicted, which turned out to be in excellent agreement with experimental observations. He also developed a theory on foam drainage placed on a thin, porous substrate.

Victor developed a new theory on the effective viscosity of suspensions and emulsions on the consideration of cluster formation and proposed a new method of calculation of the effective properties of porous media.

Prof. Starov always invested a lot of effort into the training of young scientists. More than 30 PhDs and four Doctor of Sciences degrees were successfully awarded to his younger colleagues under his supervision in Russia, United States, Bulgaria, Spain, France and UK. Starov is a well-respected authority among his colleagues all over the world. At present, he is the member of the Editorial Boards of 14 scientific journals, including Desalination journal, Colloid journal, Advances in Colloid and Interface Science, and Current Opinion in Colloid and Interface Science. He is an Editor in Chief of Journal of Chemical Engineering & Process Technology and an Associate Editor of Journal of Colloids and Interfaces. Prof Starov is a Member of the Council of International Association of Colloid and Interface Scientists, an Honorary Professor of Moscow State University of Food Production, and a Fellow of the Royal Society of Chemistry.

Prof. Starov has published around 300 papers:

http://scholar.google.co.uk/citations?hl=en&user=HxpVycEAAAAJ&view_op=list_works

Prof. Dr. Anatoly Filippov
Prof. Dr. Hüseyin Selçuk
Guest Editors

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Keywords

  • reverse osmosis
  • nano-, ultra-, microfiltration
  • electrodialysis
  • surface interactions of colloidal particles with membranes
  • modelling of ion transfer through porous media (membranes)
  • cake and gel formation on the membrane surface
  • cell models of membranes

Published Papers (8 papers)

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Editorial

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6 pages, 383 KiB  
Editorial
Influence of Surface Forces on Membrane Separations
by Anatoly N. Filippov and Huseyin Selcuk
Membranes 2022, 12(4), 400; https://doi.org/10.3390/membranes12040400 - 2 Apr 2022
Viewed by 1588
Abstract
This Special Issue of Membranes, entitled “Influence of Surface Forces on Membrane Separation”, is published in honour of Professor Victor Mikhailovich Starov, Doctor of Science in Chemistry, Fellow of the Royal Society of Chemistry [...] Full article
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Research

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13 pages, 6114 KiB  
Article
Modeling Asymmetry of a Current–Voltage Curve of a Novel MF-4SC/PTMSP Bilayer Membrane
by Anatoly N. Filippov, Natalia A. Kononenko, Natalia V. Loza and Daria A. Petrova
Membranes 2022, 12(1), 22; https://doi.org/10.3390/membranes12010022 - 24 Dec 2021
Cited by 3 | Viewed by 2448
Abstract
A novel bilayer cation-exchange membrane—consisting of a thick layer of a pristine perfluorinated membrane MF-4SC (Russian equivalent of Nafion®-117) and a thinner layer (1 μm) of the membrane, on a base of glassy polymer of internal microporosity poly(1-trimethylsilyl-1-propyne) (PTMSP)—was prepared and [...] Read more.
A novel bilayer cation-exchange membrane—consisting of a thick layer of a pristine perfluorinated membrane MF-4SC (Russian equivalent of Nafion®-117) and a thinner layer (1 μm) of the membrane, on a base of glassy polymer of internal microporosity poly(1-trimethylsilyl-1-propyne) (PTMSP)—was prepared and characterized. Using the physicochemical characteristics of one-layer membranes MF-4SC and PTMSP in 0.05 M HCl and NaCl solutions, the asymmetric current–voltage curves (CVC) of the bilayer composite were described with good accuracy up to the overlimiting regime, based on the “fine-porous membrane” model. The MF-4SC/PTMSP bilayer composite has a significant asymmetry of CVC that is promising for using it in electromembrane devices, such as membrane detectors, sensors, and diodes. Full article
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17 pages, 3754 KiB  
Article
Desalination and Detoxification of Textile Wastewater by Novel Photocatalytic Electrolysis Membrane Reactor for Ecosafe Hydroponic Farming
by Muhammed Iberia Aydin, Damla Ozaktac, Burak Yuzer, Mustafa Doğu, Hatice Inan, Hatice Eser Okten, Serdar Coskun and Huseyin Selcuk
Membranes 2022, 12(1), 10; https://doi.org/10.3390/membranes12010010 - 23 Dec 2021
Cited by 5 | Viewed by 2681
Abstract
In this study, a novel photoelectrocatalytic membrane (PECM) reactor was tested as an option for the desalination, disinfection, and detoxification of biologically treated textile wastewater (BTTWW), with the aim to reuse it in hydroponic farming. The anionic ion exchange (IEX) process was used [...] Read more.
In this study, a novel photoelectrocatalytic membrane (PECM) reactor was tested as an option for the desalination, disinfection, and detoxification of biologically treated textile wastewater (BTTWW), with the aim to reuse it in hydroponic farming. The anionic ion exchange (IEX) process was used before PECM treatment to remove toxic residual dyes. The toxicity evaluation for every effluent was carried out using the Vibrio fischeri, Microtox® test protocol. The disinfection effect of the PECM reactor was studied against E. coli. After PECM treatment, the 78.7% toxicity level of the BTTWW was reduced to 14.6%. However, photocatalytic desalination during treatment was found to be slow (2.5 mg L−1 min−1 at 1 V potential). The reactor demonstrated approximately 52% COD and 63% TOC removal efficiency. The effects of wastewater reuse on hydroponic production were comparatively investigated by following the growth of the lettuce plant. A detrimental effect was observed on the lettuce plant by the reuse of BTTWW, while no negative impact was reported using the PECM treated textile wastewater. In addition, all macro/micronutrient elements in the PECM treated textile wastewater were recovered by hydroponic farming, and the PECM treatment may be an eco-safe wastewater reuse method for crop irrigation. Full article
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14 pages, 2064 KiB  
Article
Recovery of Biologically Treated Textile Wastewater by Ozonation and Subsequent Bipolar Membrane Electrodialysis Process
by Burak Yuzer and Huseyin Selcuk
Membranes 2021, 11(11), 900; https://doi.org/10.3390/membranes11110900 - 21 Nov 2021
Cited by 14 | Viewed by 2248
Abstract
The Bipolar Membrane Electrodialysis process (BPMED) can produce valuable chemicals such as acid (HCl, H2SO4, etc.) and base (NaOH) from saline and brackish waters under the influence of an electrical field. In this study, BPMED was used to recover [...] Read more.
The Bipolar Membrane Electrodialysis process (BPMED) can produce valuable chemicals such as acid (HCl, H2SO4, etc.) and base (NaOH) from saline and brackish waters under the influence of an electrical field. In this study, BPMED was used to recover wastewater and salt in biologically treated textile wastewater (BTTWW). BPMED process, with and without pre-treatment (softening and ozonation), was evaluated under different operational conditions. Water quality parameters (color, remaining total organic carbon, hardness, etc.) in the acid, base and filtrated effluents of the BPMED process were evaluated for acid, base, and wastewater reuse purposes. Ozone oxidation decreased 90% of color and 37% of chemical oxygen demand (COD) in BTTWW. As a result, dye fouling on the anion exchange membrane of the BPMED process was reduced. Subsequently, over 90% desalination efficiency was achieved in a shorter period. Generated acid, base, and effluent wastewater of the BPMED process were found to be reusable in wet textile processes. Results indicated that pre-ozonation and subsequent BPMED membrane systems might be a promising solution in converging to a zero discharge approach in the textile industry. Full article
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16 pages, 1042 KiB  
Article
Mixed-Gas Selectivity Based on Pure Gas Permeation Measurements: An Approximate Model
by Alexander O. Malakhov and Vladimir V. Volkov
Membranes 2021, 11(11), 833; https://doi.org/10.3390/membranes11110833 - 28 Oct 2021
Cited by 5 | Viewed by 2978
Abstract
An approximate model based on friction-coefficient formalism is developed to predict the mixed-gas permeability and selectivity of polymeric membranes. More specifically, the model is a modification of Kedem’s approach to flux coupling. The crucial assumption of the developed model is the division of [...] Read more.
An approximate model based on friction-coefficient formalism is developed to predict the mixed-gas permeability and selectivity of polymeric membranes. More specifically, the model is a modification of Kedem’s approach to flux coupling. The crucial assumption of the developed model is the division of the inverse local permeability of the mixture component into two terms: the inverse local permeability of the corresponding pure gas and the term proportional to the friction between penetrants. Analytical expressions for permeability and selectivity of polymeric membranes in mixed-gas conditions were obtained within the model. The input parameters for the model are ideal selectivity and solubility coefficients for pure gases. Calculations have shown that, depending on the input parameters and the value of the membrane Peclét number (the measure of coupling), there can be both a reduction and an enhancement of selectivity compared to the ideal selectivity. The deviation between real and ideal selectivity increases at higher Peclét numbers; in the limit of large Peclét numbers, the mixed-gas selectivity tends to the value of the ideal solubility selectivity. The model has been validated using literature data on mixed-gas separation of n-butane/methane and propylene/propane through polymeric membranes. Full article
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13 pages, 2126 KiB  
Article
Influence of Membrane Vibration on Particles Rejection Using a Slotted Pore Membrane Microfiltration
by Asmat Ullah, Kamran Alam, Saad Ullah Khan and Victor M. Starov
Membranes 2021, 11(9), 709; https://doi.org/10.3390/membranes11090709 - 15 Sep 2021
Cited by 5 | Viewed by 1962
Abstract
A new method is proposed to increase the rejection in microfiltration by applying membrane oscillation, using a new type of microfiltration membrane with slotted pores. The oscillations applied to the membrane surface result in reduced membrane fouling and increased separation efficiency. An exact [...] Read more.
A new method is proposed to increase the rejection in microfiltration by applying membrane oscillation, using a new type of microfiltration membrane with slotted pores. The oscillations applied to the membrane surface result in reduced membrane fouling and increased separation efficiency. An exact mathematical solution of the flow in the surrounding solution outside the oscillating membrane is developed. The oscillation results in the appearance of a lift velocity, which moves oil particles away from the membrane. The latter results in both reduced membrane fouling and increased oil droplet rejection. This developed model was supported by the experimental results for oil water separation in the produced water treatment. It was proven that the oil droplet concentration was reduced notably in the permeate, due to the membrane oscillation, and that the applied shear rate caused by the membrane oscillation also reduced pore blockage. A four-times lower oil concentration was recorded in the permeate when the membrane vibration frequency was 25 Hz, compared to without membrane vibration. Newly generated microfiltration membranes with slotted pores were used in the experiments. Full article
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16 pages, 1463 KiB  
Article
Aminophosphonates in Nanofiltration and Reverse Osmosis Permeates
by Ramona Kuhn, Carsten Vornholt, Volker Preuß, Isaac Mbir Bryant and Marion Martienssen
Membranes 2021, 11(6), 446; https://doi.org/10.3390/membranes11060446 - 15 Jun 2021
Cited by 3 | Viewed by 3002
Abstract
Aminophosphonates such as aminotris(methylenephosphonic acid) (ATMP) are common constituents of antiscalants. In nanofiltration (NF) and reverse osmosis (RO) processes, ATMP prevents inorganic scaling leading to more stable membrane performance. So far, little attention has been paid to the possible permeation of aminophosphonates through [...] Read more.
Aminophosphonates such as aminotris(methylenephosphonic acid) (ATMP) are common constituents of antiscalants. In nanofiltration (NF) and reverse osmosis (RO) processes, ATMP prevents inorganic scaling leading to more stable membrane performance. So far, little attention has been paid to the possible permeation of aminophosphonates through NF and RO membranes. We have investigated the permeability of these membrane types for ATMP and its potential metabolites iminodi(methylenephosphonic acid) (IDMP) and amino(methylenephosphonic acid) (AMPA) with two different NF membranes (TS40 and TS80) and one RO membrane (ACM2) and three different water compositions (ultra-pure water, synthetic tap water and local tap water). We found traces of phosphonates in all investigated permeates. The highest phosphonate rejection occurred with local tap water for all three membranes investigated. Filtration experiments with a technical antiscalant formulation containing ATMP indicated similar trends of phosphonate permeability through all three membranes. We assume that the separation mechanisms of the membranes are the results of a very complex relationship between physico-chemical properties such as Donnan exclusion, feed pH, feed ionic strength and feed concentration, as well as solute–solute interactions. Full article
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Review

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22 pages, 2493 KiB  
Review
Advances in Membrane Distillation Module Configurations
by Lijo Francis, Farah Ejaz Ahmed and Nidal Hilal
Membranes 2022, 12(1), 81; https://doi.org/10.3390/membranes12010081 - 12 Jan 2022
Cited by 42 | Viewed by 7331
Abstract
Membrane Distillation (MD) is a membrane-based, temperature-driven water reclamation process. While research emphasis has been largely on membrane design, upscaling of MD has prompted advancements in energy-efficient module design and configurations. Apart from the four conventional configurations, researchers have come up with novel [...] Read more.
Membrane Distillation (MD) is a membrane-based, temperature-driven water reclamation process. While research emphasis has been largely on membrane design, upscaling of MD has prompted advancements in energy-efficient module design and configurations. Apart from the four conventional configurations, researchers have come up with novel MD membrane module designs and configurations to improve thermal efficiency. While membrane design has been the focus of many studies, development of appropriate system configurations for optimal energy efficiency for each application has received considerable attention, and is a critical aspect in advancing MD configurations. This review assesses advancements in modified and novel MD configurations design with emphasis on the effects of upscaling and pilot scale studies. Improved MD configurations discussed in this review are the material gap MD, conductive gap MD, permeate gap MD, vacuum-enhanced AGMD/DCMD, submerged MD, flashed-feed MD, dead-end MD, and vacuum-enhanced multi-effect MD. All of these modified MD configurations are designed either to reduce the heat loss by mitigating the temperature polarization or to improve the mass transfer and permeate flux. Vacuum-enhanced MD processes and MD process with non-contact feed solution show promise at the lab-scale and must be further investigated. Hollow fiber membrane-based pilot scale modules have not yet been sufficiently explored. In addition, comparison of various configurations is prevented by a lack of standardized testing conditions. We also reflect on recent pilot scale studies, ongoing hurdles in commercialization, and niche applications of the MD process. Full article
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