• 대한화장품학회지
• /
• 제25권1호
• /
• pp.89-106
• /
• 1999

폐수 처리장 관리자들로 하여금 경제적으로 효과적인 폐수처리를 위하여 화장품 제조시설을 중심으로 폐수처리공정을 파악한 후 폐수처리 및 관리에 필요한 운전인자 중 폐수 처리비 영향인자 분석을 시행하였다. 폐수처리는 대부분 활성 슬러지법을 이용하여 각업체에 적합하게 설치하여 사용하고 있으며, 폐수처리장의 일평균처리량/설계량이 0.29∼0.56으로 일평균 처리량에 비해 폐수처리장의 설계량이 큰 것으로 나타났다. 오염물질 제거율이 폐수처리비에 큰 영향을 미치고 있으며, 이를 조절하기 위한 폐수처리 운전인자는 MLSS이다. 또한, 폐수처리비를 줄이기 위한 관리 항목은 약품비와 Sludge량이며, 이를 줄이기 위해서는 SV3O의 철저한 관리가 필요하다.

• Membrane and Water Treatment
• /
• 제10권2호
• /
• pp.139-148
• /
• 2019

In this study, the removal of MB from saline solutions was evaluated by two methods by adsorption and electrodialysis; the adsorption of the mixture dye/salt on dried orange peel waste (OPW) was studied in batch method. In this study the biosorption of cationic dye by OPW was investigated as a function of initial solution pH, and initial salt (sodium chloride) concentration. The maximal dye uptake at $pH{\geq}3.6$ in the absence and in the presence of salt and the dye uptake diminished considerably in the presence of increasing concentrations of salt up to 8 g/L. The Redlich Peterson and Langmuir were the most suitable adsorption models for describing the biosorption equilibrium data of the dye both individually and in salt containing medium. As well, this work deals with the electrodialysis application to remove the dye. Synthetic solutions were used for the investigation of the main operational factors affecting the treatment performance; such as applied voltage, pH, initial dye concentration and ionic strength. The experimental results for adsorption and electrodialysis confirmed the importance of electrostatic interactions on the dye. The electrodialysis process with standard ion exchange membranes enabled efficient desalination of cationic dye solutions; there are two main factors in fouling: electrostatic interaction between cations of dyes and the fixed charged groups of the CEM, and affinity interactions.

• 한국폐기물자원순환학회지
• /
• 제35권7호
• /
• pp.647-652
• /
• 2018

The emission of nitrogen oxides has a great environmental impact. It leads to Los Angeles type smog, and it recently has attracted attention as a source of ultrafine dust. The main sources of nitrogen oxides are internal combustion engines and industrial boilers. These emission sources are processes that are essential for human industrial activities, so the regulation of original use is impossible. Therefore, special control methods should be applied to reduce NOx emissions into the atmosphere. In this study, we investigated how the supply of ER and urea influences the removal of nitrogen oxides from SRF combustion boilers. Experimental results show that the removal efficiency of nitrogen oxides can be up to 80% under the conditions of ER 2.0 and a urea feed of 0.5 LPM.

• Advances in nano research
• /
• 제13권6호
• /
• pp.527-543
• /
• 2022

A novel, green, versatile and magnetically retrievable BiFeO₃/CDR (Bismuth ferrite/coriander) nanocomposites were fabricated via simple wet chemical method utilizing in situ functionalized, cheap coriander seed powder (CDR 5%, 10%, 15% and 20 wt%) as a fuel to enhance the efficiency of pristine BiFeO₃. A comparative study was performed between BiFeO₃/CDR and BiFeO₃/CNT (Bismuth ferrite/carbon nanotubes) nanocomposites for the removal of various hazardous pollutants from waste water. The successful synthesis of the fabricated nanomaterials was monitored via FT-IR, Powder XRD, FE-SEM, CV, VSM, CHNS/O and XPS studies. The synthesized nanomaterials were employed for the oxidative degradation of Carbol fuchsin, Reactive black 5, Ciprofloxacin and Doxorubicin; adsorption of a pesticide malathion; and reduction studies for Para-nitrophenol (PNP). The fabricated nanomaterials (BiFeO₃/CDR) showcased excellent efficiency and comparable results with (BiFeO₃/CNT) for the removal of model pollutants. Moreover, synthesized green heterojunction was also testified for mixture of textile and pharmaceutical waste. Hence CDR can be utilized as a better alternative of CNTs.

• 한국대기환경학회지
• /
• 제25권5호
• /
• pp.402-409
• /
• 2009

Sodium bicarbonate ($NaHCO_3$) was used as a reactant for the removal of acid gases from a waste incinerator. The removal efficiencies of HCl and $SO_x$ were tested with a reactant mixing apparatus and a distributor installed at the bag filter inlet. It was shown that the stoichiometric ratio of $NaHCO_3$ to the acid gases which allows a removal of over 90% for both HCl and $SO_2$ was about 1.2. When a reactant mixing apparatus was installed on the duct, the removal efficiencies of HCl and $SO_2$ at the end of the duct were increased by approximately 1.5 and 3 times respectively, compared to when the apparatus was not installed. At the end of the bag filter, the removal efficiencies of the both were as high as 98% with a stoichiometric ratio of 1.35. Installing a reactant mixing apparatus on the duct and a distributor at the entrance of the bag filter and using $NaHCO_3$ as a reactant helped overcome the problem of low removal efficiencies of acid gases by dry scrubbing.

• Environmental Engineering Research
• /
• 제10권5호
• /
• pp.205-212
• /
• 2005

The study was conducted to investigate the removal of heavy metals by using Hydroxyapatite(HAp) made from waste oyster shells and wastewater with high concentration of phosphorus. The maximum calcium concentration for the production of HAp in this study was released up to 361 mg/L at pH of 3 by elution experiments. When the pH was at adjusted 6, the maximum calcium released concentration was 41 mg/L. During the elution experiment, most of the calcium was released within 60 minutes. This reaction occurred at both pH levels of 3 and 6. The result of the XRD analysis for the HAp product used in this study shows the main constituent was HAp, as well as OCP. The pH was 8.6. As the temperature increased, the main constituent did not vary, however its structure was crystallized. When the pH was maintained at 3, the removal efficiency decreased as the heavy metal concentration increased. The order of removal efficiency was as follows: $Fe^{2+}$(92%), $Pb^{2+}$(92%) > $Cu^{2+}$(20%) > $Cd^{2+}$(0%). Most of these products were dissolved and did not produce sludge in the course of heavy metals removal. As the heavy metal concentration increased at pH of 6, the removal efficiency increased. The removal efficiencies in all heavy metals were over 80%. From the analysis of the sludge after reaction with heavy metals, the HAp was detected and the OCP peak was not observed. Moreover, lead ion was observed at the peaks of lead-Apatite and lead oxidant. In the case of cadmium, copper and iron ions, hydroxide forms of each ion were also detected.

• 한국식품영양과학회지
• /
• 제30권2호
• /
• pp.344-349
• /
• 2001

클로렐라는 건강보조식품으로 이용될 뿐만 아니라 수용액상에서 중금속 제거를 위한 흡착제로 많이 연구되고 있다. 본 연구에서는 클로렐라를 이용하여 수도물의 소독제로 사용되는 염소의 제거 효과를 확인하였으며 그 결과를 녹차, activated carbon과 비교하였다. 수용액상에서 pH와 초기염소의 농도가 염소의 제거에 미치는 영향을 조사하였다. 최적의 제거 pH는 10이었으며, 염소의 제거량은 초기 염소의 농도가 1.62 g/L까지 증가함에 따라 2.46 mg/mg까지 증가하였다. 녹차의 경우 초기 염소의 농도가 1.0 g/L 이상으로 증가하여도 제거량은 약 1.5mg/mg 정도에 더 이상 증가하지 않았다. 클로렐라와 녹차에 의한 염소의 제거 결과는 Langmuir 흡착모델과 Freundlich 흡착모델에 대단히 잘 맞았으며 Langmuir 흡착모델에 의한 클로렐라의 최대 흡착량은 녹차와 activated carbon의 최대 흡착량에 비하여 약 2배로 나타나 클로렐라의 염소의 제거효능이 매우 우수한 것으로 사료되었다.

• 한국대기환경학회지
• /
• 제6권1호
• /
• pp.85-96
• /
• 1990

Simultaneous removal efficiencies of hydrophilic and hydrophobic gaseous pollutants are experimentally determined, and the macroscopic removal mechanism of pollutants in a dry scrubber is analyzed using the extended model of three phase equilibrium distribution of pollutant at high temperatures that can describe the different morphological conditions of adsorbent and water at varying relative humidities. For the simplicity, the inside of spray dryer is divided into three regions of ; (1) absorption, (2) three-phase equilibrium, and (3) adsorption, and the removal efficiencies of each pollutants at three regions are observed at different experimental conditions to estimate the effects of important parameters of dry scrubber. The laboratory experiments simulate the three regions of spray dryer with the temperature control and thus evaporation rate of water from the slurry particle. $SO_2$ as a hydrophilic gaseous pollutant and vinyl chloride as a hydrophobic toxic gas are selected for the future field application to soid waste incineration, and the two types of slurry are made of the two sorbents ; 10 wt.% $Ca(OH)_2$, and 10 wt.% NaOH. Result of temperature effect shows the height of absorption plus three-phase region is decreased as the operation temperature is increased, which results in the lower removal efficiency of $SO_2$ but higher removal for vinyl chloride in the adsorption region of dry scrubber. The removal efficiency of $SO_2$ is higher by NaOH slurry than by $Ca(OH)_2$ slurry due to the hygroscopic nature of NaOH, while the removal of vinyl chloride is higher in $Ca(OH)_2$ case. From the analysis of redults using three-phase equilibrium distribution model, the effective two-phase partition coefficients can be obtained, and the possible extention in the application of the three-phase equilibrium model in a dry scrubber design has been demonstrated.

• 방사성폐기물학회지
• /
• 제7권3호
• /
• pp.153-160
• /
• 2009

방사성 토양을 복원하기 위해 원자력시설 주변 부지의 수리지질 특성을 분석하여 국내 방사성 토양 복원에 적합한 수직형 동전기세정장치를 개발하였다. 또한, 이 수직형 동전기세정장치를 이용한 실험을 통해 원자력시설 주변 방사성토양을 복원하기 위한 최적 세정제를 선정하고 단기간에 높은 제거효율을 확보할 수 있는 최적제염조건들을 도출하였다. 초산을 세정제로 사용하였을 때 토양으로부터 코발트와 세슘의 제거효율이 가장 높으므로 동전기제염을 위한 최적 세정제로 초산을 선정하였다 동전기세정제염 시 세정제 주입량을 증가 시켰을 때 토양으로부터 코발트와 세슘의 제거효율은 평균 약 4.6% 제거효율이 증가했고 토양폐액 발생량도 동전기제염의 1.5배 인 2.4mL/g이었다. 동전기토양셀의 전압구배를 2배로 증가시켜 4 V/cm를 적용시켰을 때, 코발트와 세슘의 제거효율은 각각 98.9%와 96.7%로 평균 약 4.3% 제거효율이 증가했다. 그리고 세정제 농도를 0.01M로부터 0.05M로 증가시킨 후 제염실험 결과 코발트의 제거효율은 상승했지만 세슘의 제거효율은 감소하였다. 위 실험결과 개발한 수직형 동전기세정장치의 최적제염조건으로 제염시간은 20일 동안 초산 $0.01M{\sim}0.05M$을 세정제로 사용하여 동전기토양셀의 전압구배는 4 V/cm를 가하고, 2.4mL/g의 세정제를 주입하는 것이다.

• Korean Chemical Engineering Research
• /
• 제60권1호
• /
• pp.100-115
• /
• 2022

교대로 운전되는 광촉매반응기 공정 및 바이오필터 공정[전통적 바이오필터(L 반응기)와 두 개의 유닛(R_up 및 R_dn)을 가지는 개선된 바이오필터(R 반응기)]으로 구성된 통합 하이브리드시스템(통합처리시스템)에서 에탄올과 황화수소를 동시 함유한 폐가스 처리를 성공적으로 수행하였다. 통합처리시스템의 운전 단계로서 HA1, HA2 및 폐가스의 공급 방향이 뒤바뀐 HA3T stage의 광촉매 공정에서 각각 55, 50 및 45%의 에탄올 제거효율과 각각 70, 60 및 37%의 황화수소 제거효율을 보였다. 특히, HA3T stage에서 통합처리시스템으로 공급되는 폐가스(feed)의 황화수소 농도가 10 ppmv에서 20 ppmv로 급증함에 따른 황화수소 부하량의 증가로 인하여 특히 황화수소 제거효율의 급격한 감소를 관찰하였다. 통합처리시스템의 HA1, HB1, HA2 및 HB2 stage 및 HA3T stage의 초반에, 개선된 바이오필터(R 반응기)의 각 유닛에 설치한 sampling 구들의 에탄올의 파과 순서 및 에탄올 처리효율의 크기 순서는, HA3T stage 후반과 HB3T stage의 경우에서 각각 거꾸로 바뀌었다. 한편 개선된 바이오필터(R 반응기)에서 황화수소의 경우는 파과 정도가 에탄올의 경우만큼 두드러지지는 않았으나 비슷한 추세가 관찰되었다.