• Transactions of the Korean Society of Mechanical Engineers B
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• v.36 no.6
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• pp.619-624
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• 2012

In this study, we demonstrated the operation of an electroosmotic pump with cylindrical porous glass frits and evaluated its long-term operation. The performance of this electroosmotic pump was characterized in terms of maximum flow rate, current, and pressure using deionized water and 1 mM borate buffer. The maximum flow rate, current, and pressure linearly increase with voltage. The maximum flow rate is normalized by the pumping area and voltage for comparison of the performance between the electroosmotic pumps with cylindrical and planar frits. The normalized maximum flow rate of the cylindrical-type pump is higher than that of the planar-type pump because of their different geometries. The cylindrical-type electroosmotic pump has five times better performance than the planartype electroosmotic pump for a given pump package volume. It can operate stably for over 3 hours.

• Journal of the Korean Geotechnical Society
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• v.16 no.6
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• pp.69-77
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• 2000

본 연구에서는 전기삼투 배수와 제타포텐셜과 상관성을 규명하고자 하였다. 실험으로 직경 10cm, 길이 16cm의 원형 압밀시료에 일정 전압경사법으로 1V/cm의 직류접압을 가하여 0, 500, 3000 ppm의 납농도와 0, 230, 2300, 23000 ppm의 염분농도에서 각각 12일 과 14일 동안 전지삼투 배수량을 측정하였고, 같은 농도에서 kaolinite 현탁액의 제타포텐셜을 pH2부터 14범위에서 측정하였다. 실험결과 제타포텐셜은 전해질 농도와 pH 변화에 의존적이고, 전기삼투 투수계수와 비례관계가 있음을 확인할 수 있었다. 제타포텐셜에 따른 전기삼투 배수량과 비교한 결과, 전해질 농도가 낮을수록 제타포텐셜은 음의 값은 크고, 전기삼투 배수량도 더 증가하였다.

• Proceedings of the Membrane Society of Korea Conference
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• 1997.04b
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• pp.3-10
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• 1997

제염농축공정은 증류, 증발법을 일반적으로 사용하나, 에너지 절약차원에서 전기투석 (Electro dialysis)장치를 증발기 선단에 도입한 복합공정을 국내에서도 사용하고 있는 실정이다. 그러나, 전기투석장치는 전기적인 소모와 막의 재생, 교체처리비가 문제점이 되므로 역삼투 장치를 제염농축 공정 최선단에 도입한 복합공정을 이용할 경우 전기 투석 및 증발 복합공정에 비해 40%의 에너지 절감 효과를 기대할 수 있다. 이와 같은 장점에도 불구하고 역삼투 공정은 공급용액의 삼투압보다 큰 적용압력을 막표면에 가하여 물질분리를 수행하므로 농축공정에서 유발되는 배제액 농도의 상승은 삼투압의 증가를 일으켜 실적적용압력의 효과를 떨어뜨리게 되며 결과적으로 농축효과를 감소시키게 된다. 본 연구에서는 효과적인 염농축 공정을 위하여 막모듈 투과부에 고농도 삼투압 감소액(osmotic sink solution)을 향류식(막투과흐름을 맞받아치며 흐르는 방식)으로 유입시키는 향류식 역삼투 (counter-current reverse osmosis, CCRO) 나권형 모듈을 고안 제작하였으며, 제작된 모듈을 기존 역삼투 공정과 향류식 염삼투 공정에 적용하여 염농축도의 성능을 상호 비교하고 염농축에 관계되는 공급농도, 공급유량, 투과유량, 배제유량, 향류 유입유량, 압력구배, 삼투압차 및 농축단수 등의 인자들을 이용하여 두 공정에 대한 염농축 분리조작의 제반조건과 제작된 모듈 내의 농축관련 특성을 실험 및 수치적으로 비교, 고찰하였다.

• Proceedings of the Korean Geotechical Society Conference
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• 1996.10a
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• pp.135-140
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• 1996

• Journal of the Korean Geotechnical Society
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• v.19 no.1
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• pp.131-142
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• 2003

The characteristics of electroosmosis drainage in clayey soil were investigated, when an electrokinetic technique was applied for the purpose of separating heavy metals in contaminated ground. A series of laboratory tests, considering voltage, zeta potential, pH distribution, and current, were performed for a lead-contaminated kaolin. The results of laboratory tests were compared with numerical analysis of finite difference method. The 1311owing conclusions were obtained: The flow velocity in electroosmosis was very sensitive to the chemical and electrical characteristics of the clay. As the concentration of ion increases, the flow rate decreases and the amount of drainage also decreases as time elapses.

• Applied Chemistry for Engineering
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• v.34 no.3
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• pp.272-278
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• 2023

In this study, we analyzed the effects of current density and electroosmotic phenomena on the desalination performance of electrodialysis (ED). We conducted ED experiments under constant voltage conditions, changing the concentration of the concentrate solution from 10 to 200 g/L. During the ED operation, we measured the current density and charge supplied to the stack, the concentration of the diluted and concentrated solutions, and the amount of water transported by electroosmosis to analyze desalination performance. As the concentration of the concentrated solution increased, the selectivity of the ion exchange membrane decreased, resulting in a decrease in current efficiency. Moreover, the current efficiency was found to be influenced by the current density supplied. When the current density exceeded 15 mA/cm², back diffusion of ions was suppressed, leading to an increase in current efficiency. We also investigated the specific water transport by electroosmosis during the ED operation. We found that the amount of water transported increased proportionally to the concentration ratio of the concentrated and diluted solutions. When the concentration ratio exceeded 100, the specific water transport rapidly increased due to osmotic pressure, making it challenging to obtain a concentrated solution greater than 200 g/L.

• Proceedings of the KIEE Conference
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• 2001.11a
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• pp.69-71
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• 2001

본 논문에서는 FACS(fluorescence activated cell sorting)의 초소형화를 위한 미세 유체소자들을 플라스틱 기판에 집적하여 제작하고 전기삼투를 이용해서 세포가 일렬로 이송되는 특성을 시험한다. 제작된 미세 유체 소자는 유리 하부 기판과 플라스틱 상부 기판 및 전원장치로 구성된다. 상부기판은 세포를 주입하기 위한 샘플 측 레저버와 세포를 운반 및 일렬 이송이 가능하게 하는 버퍼를 저장할 두 개의 레저버가 있고 이들이 배출되는 레저버로 구성된다. 마이크로머시닝 기술을 이용하여 실리콘 기판 위에 미세 채널 몰드를 제작한 후 PDMS(polydimethylsiloxane)로 주물을 제작한다. $O_2$ 플라즈마를 이용하여 유리 기판과 PDMS 주물을 접합하며 제작된 채널에 적색 잉크와 bead를 샘플 측에 충전하고 버퍼 측에 sodium borate를 충전한 후 전기삼투로 구동시킨다. bead가 일렬로 이송되도록 전장을 조절하고 이때의 유속과 유량을 측정한다. 다양한 전장에 따른 실험을 통하여 채널의 구조를 최적화한다.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.36 no.7
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• pp.753-757
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• 2012

This paper presents the performance of a porous glass electroosmotic pump using an iodide/triiodide aqueous solution. The porous glass electroosmotic pump is characterized in terms of the flow rate and voltage. The flow rate and voltage increases linearly with current. A point where the voltage significantly increases is observed owing to an excess in redox capacity. The transition time monotonously decreases with current. The normalized flow rate (flow rate per membrane surface area) is used to compare previous results with results obtained in this study. The normalized flow rate of porous glass frits is three times higher than that of Nafion 117.

• KSCE Journal of Civil and Environmental Engineering Research
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• v.26 no.6B
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• pp.661-667
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• 2006

In this study, an experiment of sewage sludge dewatering is carried by using electrokinetic method, and the electrokinetic dewatering efficiency of digested sludge is analyzed. Digested sludge without coagulants is selected and gravitational and pressing dewatering methods are applied in combination with electro-osmotic and electro-osmotic pulse technology. After the test of digested sludge, dewatering test of thickened sludge is carried to evaluate the electrokinetic dewatering feasibility of thickened sludge. Under the condition of constantly applied voltage, however, electrical resistance increases with decreasing of water content so that dewatering rate decreases with time. To reduce such a hindrance caused by constantly applied voltage, electro-osmotic pulse technology which is considered to reduce the difference of water content with height, is applied. For the application of electro-osmotic pulse, the dewatered flow rate and the dewatered volume became more increasing from the middle of the dewatering process than that of continuous voltage. Through the test of thickened sludge, electro-osmotic dewatering combined with gravitational and expression also showed high dewatering rate, which proved the possibility of using electrokinetic dewatering.

• Clean Technology
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• v.16 no.2
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• pp.145-152
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• 2010

Various technical methods are applied for removing water from the water-retaining media, and the energy efficiency is the main concern in those methods. The electroosmotic process is studied as an efficient way for dewatering. An experimental electroosmotic reactor is designed and used for evaluating the effects of operational variables. The operational variables such as the electrical fields and the structure of water-retaining medias were studied. Three different shapes of polarized electric fields in ranges of 0-100 V/cm and 0-10 kHz are used as the source of electric voltage. The effect of electroosmotic process with respect to the structural variation is estimated by filling the electroosmotic reactor with the glass beads in 0.18 mm, 0.35 mm and 1.2 mm in diameters. 6% of water removal is obtained in the simulating electroosmotic reactor of glass beads. The estimated energy consumption in the simulating electroosmotic was 330~490 cal/g-water.