• Magazine of the Korean Society of Agricultural Engineers
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• v.39 no.4
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• pp.98-105
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• 1997

Compacted clay materials are often used to form barriers for waste disposal by means of landfill. The performance of clay barrier depends on its permeability characteristics under the site environments. The study discusses permeability characteristics of 4 types of permeants through a compacted clayey soil. Permeabilities are measured using the modified rigid-wall permeater and with water, PEG, Ethanol, and TCE, ranging 80 to 3.4 of dielectric constants. Results of the study are as follows : 1) Absolute permeabilities of Ethanol and TCE that their dielectric constants are lower than that of water are $K=1.0{\times} 10^{-12} cm^2$, and $5.8{\times} 10^{-12} cm^2$, respectively, that is, 1.67, and 9.67 times of permeability of water, respectively. Absolute permeability and dielectric constant of water are $K=6{\times} 10^{-13} cm^2$, and 80, respectively. 2) Changes in absolute permeability of Ethanol and TCE converge to a constant after 3.5 pore volume of permeant flows through the clay sample. This can be explained that diffuse double layer of clay is no longer reacted with permeants and contracted their pores. However there is no change in absolute permeability when water is used as a per-meant. 3) It is found that absolute permeability in reversely proportional to the value of dielectric constant of the permeants. Change in absolute permeability of the permeants with 40 or over of dielectric constant is not significant. However change in absolute permeability of the permeant with 30 or lower dielectric constant is abruptly increased. 4) A lower absolute permeability of PEG is found because of its high viscosity.

• Applied Chemistry for Engineering
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• v.7 no.6
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• pp.1087-1095
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• 1996

Pervaporation experiments of ternary ethanol/isopropanol/water mixtures were performed using poly(dimethyl siloxane)(PDMS) membrane at $45^{\circ}C$ and the mutual effects of ethanol and isopropanol on the permeation characteristics were studied. Compared to the case of the binary aqueous ethanol or isopropanol solutions, the existence of ethanol or isopropanol in the ternary mixtures resulted in the depression of each other's permeation rate. The depression effect of ethanol on the isopropanol permeation was more considerable than the depression effect of isopropanol on the ethanol permeation. These decreases in the permeation rate were thought to be due to the larger interactions between permeants than the plasticizing effects of ethanol or isopropanol on the polymer membrane. The strong interactions between permeants reduced the driving forces for both ethanol and isopropanol permeation in the ternary mixtures.

• Magazine of the Korean Society of Agricultural Engineers
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• v.39 no.2
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• pp.26-31
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• 1997

Abstract A series of permeability tests was performed on the mixtures with specific mixing rates of sand and bentonite using modified rigid-wall permeameter. Sand-bentonite mixtures were permeated by organics, ethanol and TCE. Permeability of bentonite with several mixing rates had a tendency to decrease up to initial one pore volume and permeability was thereafter converged to a constant value. When sand-bentonite mixtures was permeated by water, permeability was decreased at the beginning but it was thereafter converged to a constant. Among several mixing rates, permeability was greatly decreased at 15% of mixing rate. When sand-bentonite mixtures with 15% mixing rate was permeated by ethanol, permeability was about 10 times larger value than permeability of water. Peameability was shown greater values when permeated by TCE (TrichloroEthylene) followed by ethanol. Suitable mixing rate of sand-bentonite for a liner of waste landfills was detected.

• Proceedings of the Membrane Society of Korea Conference
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• 1994.04a
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• pp.55-56
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• 1994

There has been many attempts to improve the membrane performance using pervaporation processes[l-3]. They are 1) blending polymer with the high flux and one with high selectivity, 2) an incorporation of functional groups interacting with permeants into a membrane through copolymerization or modification, 3) composite membrane or asymmetric membrane structure with a thin skin layer which acts as a selective layer. Among them, a polymeric membrane containing ion complex group receives an extensive attention recently because ionic complex is known to activate the water transport through ion-dipole interaction. It is especially advantageous in the separation of organic-water system. We applied the ideas of the activation of water transport through ion-dipole. We have reported on the in-sire complex membrane to separate water from aqueous aceiic acid and pyridme solution[4-5] based on the simple acid-base theory. Water transport was enhanced through in-situ complex between pyridine moiety in the membrane and the incoming acetic acid in the feed. In this case, catalytic transport mechanism was proposed. In the present study we used pyridine solution as a feed and the sulfonic acid group in the membrane.

• Membrane Journal
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• v.6 no.4
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• pp.227-235
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• 1996

poly(acrylic acid)(PAA)-poly(vinyl alcohol)(PVA) membranes have been prepared by crosslinking reaction between the carboxylic acid groups of PAA and the hydroxylic groups of PVA. In the measurements of the swelling and preferential sorption of the membranes, sorption behaviors of the membranes in pure water, pure acetic acid and a mixture of them have been investigated, respectively. From the measurements of the preferential sorption in 90wt% acetic acid of aqueous mixture, the sorption of water component was found to be more enhanced at high PAA content in the membrane than that of acetic acid component due to the interaction of water with acetic acid. The sorption behavior and the degree of crosslinking influenced competitively the permeation behavior of permeants. Permeation behavior of perrecants through the membranes was analyzed by using permeation activation energies which had been obtained from the Arrhenius plots of fluxes.

• Membrane Journal
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• v.9 no.3
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• pp.163-169
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• 1999

The effects of interactions between permeant molecules or permeant and membrane material have been investigated on the permeation behavior of permeants in pervaporation of water/alcohol mix¬tures. A poly(vinyl alcohol) (PVA) membrane crosslinked with glutaraldehyde was employed in this study. A homologous series of alcohols in aqueous solution were used as feed. The pervaporation experiments were carried out with feed having 70-97 wt.% of alcohol contents and at various feed temperatures. In a high alcohol content above 92 wt.%, the permeation rate was increased in the order of interaction strength between alcohol and water in feed. However, in a low alcohol content below 90 wt.%, the tendency of the permeation rate was found to be opposite. These observations were discussed in terms of changes in interaction between permeant/permeant or permeant/membrane in varying feed composition and feed temperature.

• Bulletin of the Korean Chemical Society
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• v.25 no.5
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• pp.687-693
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• 2004

Composite membranes with a titania layer were prepared by soaking-rolling method with the titania sol of nanoparticles formed in the sol-gel process and investigated regarding the vapor permeation of various organic mixtures. The support modification was conducted by pressing $SiO_2$ xerogel of 500 nm in particle size under 10 MPa on the surface of a porous stainless steel (SUS) substrate and designed the multi-layered structure by coating the intermediate layer of ${\gamma}-Al_2O_3$. Microstructure of titania membrane was affected by heat-treatment and synthesis conditions of precursor sol, and titania formed at calcination temperature of 300$^{\circ}C$ with sol of [$H^+$]/[TIP]=0.3 possessed surface area of 210 $m^2$/g, average pore size of 1.25 nm. The titania composite membrane showed high $H_2/N_2$ selectivity and water/ethanol selectivity as 25-30 and 50-100, respectively. As a result of vapor permeation for water-alcohol and alcohol-alcohol mixture, titania composite membrane showed water-permselective and molecular-sieve permeation behavior. However, water/methanol selectivity of the membrane was very low because of chemical affinity of permeants for the membrane by similar physicochemical properties of water and methanol.

• Membrane Journal
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• v.6 no.1
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• pp.22-31
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• 1996

Pervaporation experiments of isopropanol-water mixtures through a polydimethytsiloxane(PDMS) membrane were carried out at 35$^{\circ}$C and the effect of isopropanol concentration on the separation characteristics was investigated. The total permeation rate showed the largest deviation from the ideal permeation rate at the isoprpanol volume fraction from 0.5 to 0.7, which resulted from the interaction effect between permeants. The plasticizing effect of isopropanol enhanced the permeation of water, while the existance of water resulted in the depression of isopropanol permeation. Both the permeation rate and the selectivity were predicted using Flory-Huggins thermodynamics and modified Maxwell-Stefan equation. The concentration-dependent diffusion coefficients were expressed by Vignes equation. The Flory-Huggins interaction parameter between isopropanol and water was calculated using excess Gibbs energy correlation and the interaction parameters between liquid and polymer membrane were determined by equilibrium swelling experiments. The predicted permeation rates were in accord with the experimental ones within maximum error range of 35 %. The predicted permeation selectivities were in good agreement with the experimental values.

• Applied Chemistry for Engineering
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• v.10 no.3
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• pp.374-381
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• 1999

Poly(vinyl alcohol) (PVA) membranes crosslinked with poly(styrene-maleic anhydride) (PSMAn) were prepared, and the pervaporation characteristics of the membranes were studied for the separation of water/ethanol mixtures. The prepared PVA membranes showed that the permeation rate and separation factors were increased with increasing of PSMAn contents in the feed of 92/8 wt. % ethanol/water composition. However, when the water content in the feed composition was increased highly, the overall permeation rate was increased in the order of 2%>1%>0.5% in spite of the increase of the crosslinking contents, and the separation factor was decreased due to the higher sorbed water contents and the consequent plasticization action of membrane. Also, with respect to operating temperature, the permeation rate of the membranes obeyed the Arrhenius type. Especially, in the case of 2% crosslinked membrane, it was shown based on the pervaporation characteristics that both the permeation rate and separation factor were increased with increasing operating temperature from $30^{\circ}C$( to $50^{\circ}C$. From these results, it can be known that the hydrophilic groups introduced in the membrane by PSMAn highly affected the transport of permeants.