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2008, Desalination
Application of the liquid emulsion membrane (LEM) technology to the industrial scale is hindered by the challenges imposed by stability of the emulsion during the transfer of the solute (pertraction). One of the important factors which leads to the instability is swelling. Emulsion undergoes swelling due to the osmotic gradient across the membrane as well as due to the occlusion of the external phase into the membrane phase; the latter is caused by the hydrodynamic deformation of the membrane globules. In the present work, we have studied swelling of the emulsion phase in a water-in-oil-in-water type LEM system. Nitric acid is the internal aqueous phase and is encapsulated in organic membrane phase composed of DEHPA-kerosene-SPAN80. Demineralised water is used as the external phase. The effect of the composition of the system and the hydrodynamic condition on the rate of swelling has been studied. A mathematical model has been developed to describe the effects of the relevant parameters on swelling of the emulsion. The globules of the emulsion are viewed as having a core-shell structure, based on the visual evidence. The model takes into account both the osmotic and the occlusion modes of swelling and also the leakage of the internal phase. The predictions of the model are found to be in good agreement with the experiments. The model would be useful for evaluating the rate of pertraction of a solute through the membrane-strip combination used in the present study. The study would also be useful for tuning the design and the operating parameters in LEM pertraction to achieve minimum swelling of the emulsion.
Separation Science and Technology, 2003
Emulsion liquid membrane (ELM) systems can efficiently extract and concentrate dilute solutes in a variety of applications and chemistries. Internal phase leakage and swell reduce extraction efficiency and concentration, which limits their use. Nearly all studies of ELM leakage and swell have been conducted in batch systems, although continuous flow systems are preferred for industrial applications. The objective of this investigation was to assess the ability of batch experiments to predict continuous system performance with respect to internal phase leakage and swell. The effects of five factors (surfactant concentration, osmotic pressure, membrane viscosity, internal phase volume fraction, and extraction vessel stir rate) on leakage and swell were measured in a continuous stirred-tank reactor (CSTR) system without solute extraction. The results were compared with those reported previously for a batch system with the same experimental conditions and vessel geometry. Overall, the effects of the five factors in the CSTR system are qualitatively consistent with the batch system observations, suggesting that the influential variables in the batch system are similarly influential in the CSTR system. Leakage and swell in the CSTR and batch systems are correlated with similar amounts of swell in both systems but consistently smaller leakage in the CSTR configuration.
2007
Operation of emulsion process illustrated on the basis of a oil-inwatcr (O/W) emulsion with water soluble surfactants (modification of Karbstein, 1994) 5 2.3 Principle of membrane emulsification (exemplified with a W/O/W emulsion) 8 2.4 Mechanisms of the production of either a double emulsion or a simple emulsion by phase inversion under similar conditions. ... 9 2.5 Droplet creation by different mechanical emulsification processes (personal communication with Prof. H. Schuchmann) 2.6 Schematic diagram of forces acting on a droplet detaching from a membrane pore 17 2.7 Entwicklung auf die drei wichtigsten Emulsionstypen O/W, W/O und W/O/W. Die vorliegende Arbeit kann als erster experimenteller Schritt angesehen werden, welcher den Einfluss einzelner Parameter auf die Qualität der hergestellten Emul¬ sionen beschreibt.
Journal of Industrial and Engineering Chemistry, 2020
Emulsion liquid membrane (ELM) systems can efficiently extract and concentrate dilute solutes in a variety of applications and chemistries. Internal phase leakage and swell reduce extraction efficiency and concentration, which limits their use. Nearly all studies of ELM leakage and swell have been conducted in batch systems, although continuous flow systems are preferred for industrial applications. The objective of this investigation was to assess the ability of batch experiments to predict continuous system performance with respect to internal phase leakage and swell. The effects of five factors (surfactant concentration, osmotic pressure, membrane viscosity, internal phase volume fraction, and extraction vessel stir rate) on leakage and swell were measured in a continuous stirred-tank reactor (CSTR) system without solute extraction. The results were compared with those reported previously for a batch system with the same experimental conditions and vessel geometry. Overall, the effects of the five factors in the CSTR system are qualitatively consistent with the batch system observations, suggesting that the influential variables in the batch system are similarly influential in the CSTR system. Leakage and swell in the CSTR and batch systems are correlated with similar amounts of swell in both systems but consistently smaller leakage in the CSTR configuration.
Coatings
Double emulsions are ternary systems commonly used in several disciplines in areas such as food technology, applied chemistry, chemical engineering, materials science, pharmacology and environmental science. In several courses related to these areas, the implementation of laboratory experiment is required to strengthen the knowledge acquired by students during the theoretical lessons. However, it is difficult to find published practical experiments in this field. This work presents a four-hour hands-on laboratory experiment in which students can easily formulate and prepare water-in-oil-in-water double emulsions for vitamin B12 encapsulation. In this experiment, students can analyze the effect of the osmotic pressure produced by the addition of different NaCl concentrations in each aqueous phase, which could lead to the swelling and deswelling phenomena of the inner aqueous droplets and, therefore, affect the encapsulation efficiency of the formulated systems. The double emulsions a...
2014
For the prediction of the process of separation of emulsions and selection of optimal conditions for these processes an appropriate mathematical description is required. Thereby, a mathematical model of the convective diffusion of the continuous process in the space between the membrane and the impermeable wall, and the molecular diffusion in membrane was developed in the form of an analytical solution of the corresponding differential equations of transient diffusion for substance transfer in the moving fluid in the membrane, where due to membrane’s selective properties the constant separation of substances takes place. In this study authors addressed and analytically solved a diffusion boundary-value problem describing the mechanism of baromembrane emulsions separation. This value problem may find an application in the study of confectioner\u27s cream production cycle
Journal of Physics: Conference Series, 2019
Water-in-oil-in-water (W/O/W) emulsion system in Emulsion liquid Membrane (ELM) consist of three main phases which are membrane phase, internal phase and external phase. However, ELM performance is reported to be heavily affected by the emulsion stability. Instability of emulsions occurred as a result of metastable colloids that are made of two immiscible liquids, where one being dispersed in the other with the presence of surface-active agent. Membrane breakage was identified as one of the causes of emulsion instability. This research work focuses on identifying best condition that records minimal breakage hence, high efficiency of solute removal can be anticipated. Influence of homogenization time and speed, carrier concentration and surfactant concentration on membrane breakage were investigated. Data recorded shows that the emulsion needs to be homogenized at 8000 rpm for 15 mins to obtain minimal breakage of membrane. On top of that, membrane phase consists of 4 wt% of carrier ...
Chemical Engineering & Technology, 2018
This article has been accepted for publication and undergone full peer review but has not been through the copyediting, typesetting, pagination and proofreading process, which may lead to differences between this version and the final Version of Record (VOR). This work is currently citable by using the Digital Object Identifier (DOI) given below. The final VoR will be published online in Early View as soon as possible and may be different to this Accepted Article as a result of editing. Readers should obtain the final VoR from the journal website shown below when it is published to ensure accuracy of information. The authors are responsible for the content of this Accepted Article.
2018
Emulsion liquid membrane (ELM) systems are water-in-oil emulsions dispersed in water, which, with appropriate chemistry, can efficiently extract and concentrate metals (e.g., cadmium, chromium, copper, cobalt, nickel, lead, zinc, mercury, gold and silver), weak acids and bases (e.g., phenolics and amines), inorganic species and pharmaceuticals (e.g., acetaminophen and amino acids) from the external water phase. Since their invention in 1968, ELM systems have been studied extensively. Most studies in the literature have investigated the extraction performance of ELM systems. This dissertation reports experimental investigations of several formulation and operating parameters on leakage and swell of the internal water droplets, which reduce extraction efficiency and concentration of extracted substances. Leakage and swell were measured in both batch and continuous stirred tank reactor (CSTR) systems for the same formulation and operating conditions. The batch and CSTR results are compared to test, for the first time, whether leakage and swell in the CSTR system can be predicted from measurements in the batch system, which is easier to study. Several other researchers have used pH change in the external water phase to quantify leakage of internal droplets containing acid or base. Often the equations they used to calculate leakage contain unstated simplifying assumptions that can produce significant error for some experimental conditions, including those observed in several of these studies. In this dissertation general equations are developed and compared with simplified equations reported in the ELM literature over more than 30 years to identify the underlying assumptions and the magnitude of the potential error. A detailed analysis of one previously reported ELM leakage study based on pH measurements was performed. The original leakage results are corrected, which led to revised conclusions about the effects of formulation and operating conditions on leakage.
Malaysian Journal of Fundamental and Applied Sciences
The stability of emulsion is crucial in the emulsion liquid membrane (ELM) process. It has been discovered that the size of emulsion droplets and globules is related to ELM stability and can be predicted using a correlation model. In this study, the best correlation for the emulsion size prediction was determined for ELM extraction of succinic acid. Several parameters affecting the emulsion sizes and stability including emulsification speed, emulsification time, agitation speed, and treat ratio were evaluated. A new correlation for the succinic acid system was obtained that fit experimental data between 0.1-0.5 dispersed phased holdup fraction. From the study, the Weber number depended on the emulsification speed, emulsification time, and agitation speed, which consequently affected the predicted emulsion size. This study demonstrates that mathematical correlations can be used to predict the size of emulsion droplets and globules in the ELM process of organic compound extraction.
Journal of Radioanalytical and Nuclear Chemistry, 1992
Potassium leakage was studied in liquid membrane systems containing various emulsifiers and compared with emulsion, stability in the storage test. The effects of various parameters upon emulsion stability and the leakage of standard traces are discussed. The transfer of cations can be caused by emulsion breaking, by transport with the specific carrier and/or with surfactants used as emulsifiers. The latter case becomes especially important when hydrophilic surfactants, e.g. ones containing polyoxyethylene chains, are present in liquid membranes. In systems containing hydrophobic emulsifiers the transfer of potassium is relatively low. In each case considered the effect of emulsifiers upon the transfer of the standard tracer should be checked prior to using the leakage test to characterize emulsion stability.
2017
This paper analyses the impact of two types of emulsifiers originating from milk: milk protein concentrate (MPC) and whey protein concentrate (WPC), on droplet size distribution using an asymmetric membrane process. The results indicated that the size, span and uniformity of oil droplets in emulsions depend on the velocity of shear stress on the internal surface of a membrane channel and on the physical and chemical parameters of the medium used as an emulsifier. The use of WPC produced an emulsion with optimum (the lowest) parameters of oil droplet size distribution. Switching from WPC to MPC resulted in an increase in the average characteristic diameter of the emulsion droplets and simultaneously caused widening of the distribution and a reduction in the uniformity index. STUDIA NAD ROZKŁADEM WIELKOŚCI KULECZEK TŁUSZCZOWYCH EMULSJI TYPU O/W OTRZYMANYCH Z WYKORZYSTANIEM MEMBRAN ASYMETRYCZNYCH Fabian Dajnowiec, Paweł Banaszczyk, Aleksander Kubiak, Malwina Biegaj, Lidia Zander Katedr...
ACS Omega
The purpose of this study is to explore the emulsion liquid membrane stability for acetaminophen (ACTP) removal from aqueous solution. In this work, the membrane phase was prepared by dissolving trioctylamine (TOA) with kerosene and Span80. The stability of the emulsion in terms of emulsion size, membrane breakage, and its efficiency in removing ACTP was considered for the optimization of parameters. Investigation on the stability of emulsion was carried out by manipulating the concentration of stripping agent, agitation speed, extraction time, and treat ratio. The best condition to produce a very stable emulsion was achieved at 0.1 M of stripping agent concentration, with 300 rpm of agitation speed for 3 min of extraction time with a treat ratio of 3:1. Eighty-five percent of ACTP successfully stripped into the emulsion with minimum membrane breakage of 0.17% through this experiment.
INTERNATIONAL RESEARCH JOURNAL OF PHARMACY, 2014
Emulsions are thermodynamically unstable heterogeneous biphasic system. There are certain parameters which if and emulsion follow considered as stable. There are lots of sign of physical and chemical instability of emulsion are creaming, cracking, phase inversion, flocculation. There are several methods of detect stability of prepared emulsion. Rheological assessment, macroscopic examination, globule size analysis and accelerated stability test. Many types of emulsifying agents are interfacial tension, film formation and electric potential and emulsion rheology. Emulgents form three types of films around dispersed phase globules are monomolecular, multimolecular and particulate film. Regard to the improvement in the effectiveness and stability several enhancements have been made in the emulsion technology micro emulsion, multiple emulsions, non aqueous emulsions, liposome emulsions, nanoemulsions and emulsions polymerization are few advances with the advancement in application of emulsion incorporate in this review.
Separation and Purification Technology, 2019
Leakage of the internal phase droplets reduces the extraction efficiency of emulsion liquid membrane systems by spilling the stripping agent and previously extracted solute into the bulk phase. When the stripping agent is acid or base, internal phase leakage can be determined from bulk phase pH measurements. New equations for calculating leakage from these pH measurements are presented, which account for bulk phase chemistry and volume changes due to leakage and emulsion swell. We show that equations used in several studies published over more than 30 years include unidentified assumptions that can cause erroneous leakage estimates for systems with weak acid or base stripping agents or bulk phase solutions that are not initially neutral. Guidelines identifying when these approximate equations will underestimate leakage by 10% or more are presented. Based on these guidelines and calculations quantifying errors in examples from the literature, we expect that many results calculated from pH underestimate the actual leakage. The new equations use the same experimental data as the approximate equations with minimal increased complexity and are recommended whenever leakage is calculated from pH measurements in systems without solute extraction. Methods for extending the equations to systems with simultaneous solute extraction are described.
Adsorption and Aggregation of Surfactants in Solution. Mittal K. L., Shah D. O., Eds., Surfactant Science Series N° 109 (Chap. 24) pp 501-524. M. Dekker New York (2003), 2003
Emulsion properties depend mainly upon three kinds of variables: physicochemical formulation, composition, and manufacturing protocol. The current state of the art allows the interpretation of the effects of these variables on such properties in the framework of a generalized phenomenology that includes temporal changes, either instantaneous or delayed, as they take place in manufacturing processes. The know-how can be readily translated into guidelines and constraints concerning the process operation and equipment design. This approach is referred to as formulation engineering.
Soft Matter, 2016
2019
The hydrophilic-lipophilic balance (HLB) system provides distinctive feature in deciding the role of surfactants and co surfactants combinations (Smix), oil content and ratio of aqueous phase in a microemulsion system. Also, it has definitive role in the formulation of different types of microemulsion systems including O/W, W/O and bicontinuous microemulsions asit offers a strategic approach to determine on the choice and selection of suitable emulsifiers.The present study is based on the evaluation of hydrophilic-lipophilic balance (HLB) system in fabrication of various types of microemulsions. Microemulsions can be made through two different methods i.e. Phase titration method wheremicroemulsion can be prepared by a spontaneous emulsification method (phase titration method) and Phase inversion Methodwhere phase inversion of the microemulsion occurs as a result of addition of surplus amount of the dispersed phase. Hence, in this review we studied the effect of HLB values of excipie...
2018
INTRODUCTION Emulsion An emulsion is a dynamically ambiguous system subsisting of partially two nonmiscible liquidstate, upon which is diffuse as drop (the dispersed phase) in the other liquid state (the continuous phase), preserved by the existence of an emulsifying agent. The molecule diameter of the diffuse states usually develop from about 0.1 to 10 μm, despite particle diameters as slight as 0.01 μm and as extensive as 100 μm are not infrequent in some formations. Type of Emulsion Oil in water (o/w) in the departed system the oil (or internal) phase is disappearing as droplets over the extrinsic aqueous phase. ABSTRACT Emulsion is a biphasic liquid dosage form. These are of two type oil in water and water in oil, it is a conventional method now days novel dosage forms are used like microemulsion and nanoemulsion. These are prepared by using different process and provide better bioavilability and response. There size are also differ and provide good result as comparison of emuls...
Langmuir, 2004
A method was developed allowing in situ adjustment of water-in-oil-in-water double emulsion (W/O/W) morphologies by tailoring the osmotic pressure of the water phases. The control of internal droplet size is achieved by altering the chemical potential of the external and internal water phases by dissolving neutral linear polysaccharides of suitable molecular weights. As a consequence of the different chemical potentials in the two aqueous phases, transport of water takes place modifying the initial morphology of the double emulsion. Self-diffusion 1 H nuclear magnetic resonance ( 1 H NMR) was used to assess transport mechanisms of water in oil, while a numerical model was developed to predict the swelling/shrinking behavior of W/O/W double emulsions. The model was based on a two-step procedure in which the equilibrium size of a single internal water droplet was first predicted and then the results of the single droplet were extended to the entire double emulsion. The prediction of the equilibrium size of an internal droplet was derived by the equalization of the Laplace pressure with the osmotic pressure difference of the two aqueous phases, as modeled by mean-field theory. The double emulsion equilibrium morphologies were then predicted by upscaling the results of a single drop to the droplet size distribution of the internal W/O emulsion. Good agreement was found between the theoretical predictions and the measurement of double emulsion droplet size distribution. Therefore, the present model constitutes a valuable tool for in situ control of double emulsion morphology and enables new possible applications of these colloidal systems.
Desalination, 2005
The effect of factors influencing the on separation of water in oil emulsions was investigated. A hydrophobic PTFE membrane with 0.45 mm pore size was used. Gas oil, distilled water and Span 80 were selected as continuous phase, dispersed phase and emulsifier, respectively. The prepared emulsions contained 5-20 vol% water and 0.2-0.8 vol% emulsifier. Taguchi experimental design was used to plan a minimum number of experiments. A L 16 orthogonal array (Five factors in four levels) was employed to evaluate effect of water and emulsifier content in feed, operating pressure, operating temperature and feed residence time in module on the response (permeate flux and water content in permeate). Preliminary experiments were carried out to identify critical feed conditions. It was shown that increasing emulsifier content and decreasing water content feed decrease permeate flux and water content in permeate. Obviously, minimum and maximum permeate flux was observed when emulsifier and water content in feed were held at their maximum and minimum levels, respectively. It was found that decreasing residence time to its lower limit causes permeate flux to increase. It was also found that, contrary to other microfiltration processes, temperature is an effective factor on the response and increasing pressure decreases permeate flux. Analyzing of variance was finally applied to determine the optimum operating condition as well as contribution of each factor on the response.
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