• Environmental engineer
• /
• s.325
• /
• pp.86-93
• /
• 2013

본 발명은 약품 혼합조와 침전조 일체형 초고속침전 수처리 장치 및 이를 이용한 수처리 방법에 관한 것으로서, 일반적인 수처리 공정에서 필요한 각각의 다수의 단위 공정들을 단일 처리조 내에서 수행하게 함으로써 약품혼합, 응집반응, 침전, 슬러지 인출 및 처리수의 배수가 시간 간격을 두어 이루어지도록 하여 전체적인 유체의 체류시간이 줄여 최대 30분 이내의 초고속 수처리가 가능하도록 하는 효과를 갖는다. 또한, 약품 혼합조, 반응조 및 침전조를 별도로 구성하지 않고 단일 처리조로 시설을 컴팩트화하여 시설비 및 소요 부지를 줄일 수 있도록 함과 아울러 처리수의 수질을 SS(Suspended Solids) 기준으로 1ppm 이하로 만족시킴으로써 후단의 여과공정이 불필요하여 시설비를 절감할 수 있는 효과를 갖는다. 또한, pH 감지부에 별도의 pH 지시계 세척부를 설치하여 안정적으로 pH 감지가 이루어지도록 하여 약품 주입을 경제적이고 효율적으로 이루어질 수 있도록 하여 수처리에 따른 유지 및 관리 비용을 절감시킬 수 있도록 하는 효과를 갖는다.

• Proceedings of the Korean Institute of Surface Engineering Conference
• /
• 2015.11a
• /
• pp.224-225
• /
• 2015

폐솔더 박리액으로부터 주석 및 구리의 분리를 위하여 옥살레이트 침전을 통해 각각 금속염으로 회수하기 위한 기초 연구를 실시하였다. 먼저 옥살산의 첨가량에 따라 주석의 침전율이 증가하였으며 당량비(옥살산/주석)의 1.0-1.5배를 첨가할 경우 주석이 99.5%, 구리는 2.0% 정도 침전되었고 철, 납 등은 거의 침전되지 않아 주석만 선택적으로 침전되는 것을 확인 하였다. 반응온도 증가에 따라 주석의 침전율은 증가하여 $60^{\circ}C$ 부근에서 최대값을 보이다가 온도가 더 증가하면 오히려 감소 경향을 보였다. 침전물의 고액분리 용이를 위해 카티온성 고분자 응집제를 이용하여 침강시킨 후, 분리된 침전물을 건조, 분쇄하여 $SnO_2$의 산화물을 얻을 수 있었다. 주석이 제거된 폐솔더 박리액에 옥살산을 첨가하여 구리가 약 91% 이상 침전되어 납, 철 등의 금속과 분리하여 선택적으로 회수가 가능하였다.

• Korean Chemical Engineering Research
• /
• v.59 no.3
• /
• pp.379-392
• /
• 2021

In this study, an improved acetone-water fractional precipitation process for paclitaxel using ultrasonic cavitation bubbles and gas bubbles was developed. Compared to the conventional method, the time required for precipitation has been reduced by 20~25 times. In addition, the particle size of paclitaxel decreased by 3.5~5.5 times and the diffusion coefficient of paclitaxel increased by 3.5~6.7 times. In the case of precipitation using ultrasonic cavitation bubbles, as the ultrasonic power increased and the temperature decreased, the precipitation rate constant increased. In the case of precipitation using gas bubbles, as the gas flow rate increased and the temperature decreased, the precipitation rate constant increased. Thermodynamic parameters revealed the exothermic, irreversible, and nonspontaneous nature of the improved fractional precipitation.

• Resources Recycling
• /
• v.29 no.5
• /
• pp.48-54
• /
• 2020

Sulphuric acid (H₂SO₄) leaching and hydrolysis were experimented for the recovery of titanum dioxide (TiO₂) from the water-leached residue followed by soda-roasting spent SCR catalysts. Sulphuric acid leaching of Ti was carried out with leachate concentration (4~8 M) and the others were fixed (temp.: 70 ℃, leaching time: 3 hrs, slurry density: 100 g/L, stirring speed: 500 rpm). For recovering of Ti from the leaching solution, hydrolysis precipitation was conducted at 100 ℃ for 2 hours in various mixing ratio (leached solution:distilled water) of 1:9 to 5:5. The maximum leachability was reached to 95.2 % in 6 M H₂SO₄ leachate. on the other hand, the leachability of Si decreased dramatically 91.7 to 3.0 % with an increase of H₂SO₄ concentration. Hydrolysis precipitation of Ti was proceeded with leaching solution of 8 M H₂SO₄ with the lowest content of Si. The yield of precipitation increased proportionally with a dilution ratio of leaching solution. Moreover, it increased generally by adding 0.2 g TiO₂ as a precipitation seed to the diluted leaching solution. Ultimately, 99.8 % of TiO₂ can be recovered with the purity of 99.46 % from the 1:9 diluted solution.

• Proceedings of the Korea Air Pollution Research Association Conference
• /
• 2000.04a
• /
• pp.245-246
• /
• 2000

공기중의 오염 입자가 인체에 얼마나 많은 영향을 미치는가는 흡입된 입자 (inhaled particles) 중에서 얼마나 많은 양이 폐 (lung)에 침전되는가와 밀접한 관계가 있다. 또한 정상 및 비정상 (diseased) 폐에서, 흡입된 입자의 침전 위치와 침전양 (deposition site and dose)은 입자의 크기와 호흡 양식(breathing pattern)에 따라 큰 차이를 보이며, 이런 차이는 흡입오염입자 (inhaled pollutant particles)에 의한 건강 위험도 평가 (health risk assessment) 및 흡입용 약물 (inhaled drug aerosols)의 치료효과(therapeutic effects) 평가 등에 큰 영향을 미친다. (중략)

• Resources Recycling
• /
• v.12 no.4
• /
• pp.38-43
• /
• 2003

Phosphate is an essential material for the growth of organisms. However. since relatively small amount is required. a large amount of phosphate is abandoned in wastes and wastewater. which contaminate the ecological environment including aquatic system. Purpose of this study is to treat especially high concentrated phosphate wastewater by use of calcium precipitation method. The pH range considered was from 6 to 12 and the maximum removal of phosphate was attained at pH 12. The con-centration of phosphate was observed to decrease rapidly until a half amount of calcium ion to its equivalent for the formation of calcium phosphate precipitate was added. which resulted in the decrease of the remaining concentration of phosphate down to 0.0027 mM. The effect of fluoride ion was examined and the concentration ratio between the phosphate and fluoride ion did not have any significant influence on the removal efficiency of phosphate. The effect of pH was also investigated. With the increasing of the pH in solution, the removal rate of phosphate was increased. Also it was investigated that the effect of fluoride on the phosphate removal was not significant.

• Resources Recycling
• /
• v.23 no.3
• /
• pp.37-43
• /
• 2014

A study has been made on the recovery of tin and copper from waste solder stripper by oxalate precipitation. With the increasing of the oxalic acid addition, tin was precipitated effectively and removed above 99.5% of tin when the oxalic acid, in an amount 1.0-1.5 times the stoichometric requirement, was added. But, in this case, only 2.0% of copper was precipitated and lead, iron were not precipitated. So, tin was selectively removed from the waste solution. With the increasing of the reaction temperature, the removal percentage of tin was increased and maximum value at arounf $60^{\circ}C$ and decreased with increase in the temperature any more. After filtering the precipitate and drying in oven, $SnO_2$ was obtained from the precipitate. After removal of tin in stripping solution, above 91% of copper was selectively removed by Cu-oxalate by addition of oxalic acid.

• Journal of the Korea Organic Resources Recycling Association
• /
• v.26 no.1
• /
• pp.47-53
• /
• 2018

Recovery of lactic acid from fermentation broth using chemical precipitation was investigated with various chemicals. Effects of chemical types, mixing speeds, settling duration, and solvent addition were evaluated to improve the recovery rates of lactic acid. Overall, recovery efficiencies increased as the dosage of chemicals increased. Recovery rate of lactic acid by CaO was higher than those of $Ca(OH)_2$ and $CaCO_3$. Recovery of lactic acid increased by 48% under the optimized reaction conditions which included a mixing speed at 180 rpm, a settling duration of 24 h, and addition of ethanol at 25%(v/v). Practical application needs to consider types and concentrations of other organic acids as well as lactic acid. Based upon the results of fluorescence excitation emission matrix (FEEM), size exclusion chromatography (SEC), characteristics of recovered lactic acid were same as that in the fermentation broth.

• Microbiology and Biotechnology Letters
• /
• v.42 no.2
• /
• pp.114-120
• /
• 2014

This study evaluated the effect of the zeta potential of silica-alumina on the behavior, in terms of purity, yield, fractional precipitation time, precipitate shape, size of fractional precipitation in the increased surface area, and the fractional precipitation process, for the purification of paclitaxel. As the zeta potential value of silica-alumina increased, the yield of paclitaxel concurrently increased while the precipitation time decreased. The use of alumina with the highest value of the zeta potential (+35.41 mV) as a surface area-increasing material dramatically reduced the precipitation time by 12 h compared with the results of the control. On the other hand, the purity of paclitaxel had almost no effect on changes in the zeta potential of silica-alumina. In addition, the precipitate size was inversely correlated with the absolute value of the zeta potential.

• Korean Chemical Engineering Research
• /
• v.50 no.3
• /
• pp.535-544
• /
• 2012

Filtration on horizontal filter medium facing upward is accompanied by sedimentation. When sedimentation phenomenon is not considered, the average specific cake resistance by filtration could be in error more than two times. In the previous paper on this subject, it was insisted that the solid mass fraction of suspension changes in filtration period by sedimentation. But we could not find out the degree of change. At the first half of this paper, the average specific cake resistance measured by permeation will be proved to be exact in several means. The average specific cake resistance conventionally measured by filtration does not give correct results because it uses initial solid mass fraction of suspension. Then we calculated the changed solid mass fraction of suspension due to sedimentation during filtration by the experimental values obtained "filtration-permeation" method. We also determined the solid mass fraction at a certain moment of filtration from the suspension height and a new equation derived in this study. The two results were compared and proven that they almost matched.