• 대한환경공학회지
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• 제22권5호
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• pp.861-867
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• 2000

무산소 조건에서의 인섭취를 이용한 질소, 인 화합물의 동시 제거 가능성을 연속회분식반응기(SBR)를 사용하여 고찰하였다. 혐기-호기상의 AO SBR 반응기에 점차적으로 무산소상을 도입함으로써 질산염을 전자수용체로 사용하여 탈질이 가능한 인섭취 미생물들(DPAOs)을 다량으로 축적하였다.(혐기-호기-무산소-호기상의 $(AO)_2$ SBR). 무산소상과 호기상에서의 인섭취율을 비교해 보았을 때, 전체 인제거 미생물 내에서 DPAOs의 비율이 약 10%에서 64%까지 증가하였다. $(AO)_2$ SBR은 안정된 질소, 인제거 성능을 보였으며, 유기물질, 질소, 인 화합물의 제거율은 각각 92%, 88%, 100%였다. $(AO)_2$ SBR의 운전결과와 회분식 실험으로 부터 아질산염은 무산소상에서의 인제거 반응에 어떠한 악영향도 미치지 않으며, 오히려 질산염과 함께 전자 수용체로 사용되어짐을 알 수 있었다.

• 상하수도학회지
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• 제9권3호
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• pp.99-107
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• 1995

Various humic substances are widely distributed in natural water body, such as rivers and lakes and cause the yellowish or brownish color to water. The evidence that humic substances are precursors of THMs formation in chlorinated drinking water has been reported m the Jiteratures. For the reason of public health as well as aesthetics, needs for humic substances removal have been increased in the conventional water treatment processes. In this research, the characteristics of aluminium coagulation of humic acids and humic acids were investigated. The optimum pH and coagulants dosage to remove these materials simultaneously by coagulation were alto studied. The results are as followed; 1. UV-254 absorptiometry for measuring the concentration of aquatic humic acids showed good applicability and stable results. 2. The optimal pH range for humic acids removal by aluminium coagulation was 5 to 5.5, however, an increase in aluminium coagulant dosage could enhance the removal rate of humic acids in the wide pH range. 3. Coprecipitation of humic acids in the typical pH range of 6.5 to 8 in water treatment processes may require the sweep coagulation mechanism with the excess aluminium coagulant dosage. 4. Using PAC(poly aluminium chloride) or PASS(poly aluminium silica sulfate) as coagulants was able to expand the operating range for removing humic acids. 5. From the coagulation of humic substances(UV-254) and turbidity at pH range of 5.5 - 6.0 and alum dose of 86 ppm, the removal efficiency of turbidity from the reservoir water was above 90% and that of UV-254 was above 70%. 6. By using the reservoir water, the optimum condition of rapid mixing for simultaneous removal of turbidity and UV-254 absorbance was pH of 5.8 and LAS dose of 86 ppm, in this study.

• Korean Chemical Engineering Research
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• 제40권6호
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• pp.725-728
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• 2002

NOx와 먼지 동시 제거용 기능성 여과포 개발의 일환으로 $V_2O_5/TiO_2$ 계열의 상용촉매를 사용하여 P-84, Nomex, PTFE 여과포에 코팅하였다. 사용된 코팅 방법은 Sol-gel법, Spray 법 그리고 Dip 코팅 방법이었으며 코팅방법이 여과포의 NOx 제거 반응에 미치는 영향을 조사하였다. NOx 제거반응실험은 여과포의 작동온도에 맞는 $100-250^{\circ}C$의 반응온도범위에서, 공간속도 $5,000hr^{-1}$, 산소농도 6%, $NH_3/NO$ 몰비는 1.0의 조건하에서 수행되었다. 본 연구에서 시도된 세 가지 코팅 방법 중 촉매량의 조절 및 균일한 코팅이 용이한 Sol-gel법에 의해 제조된 기능성여과포가 가장 좋은 NOx 전환율을 나타냈다.

• 상하수도학회지
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• 제31권4호
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• pp.329-338
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• 2017

The problem of disposal of brine due to increased MD/RO desalination plant has recently become a big social issue. The chlor-alkali process through electrolysis of brine has been studied as a method to overcome this problem. In order to increase the electrolysis efficiency, a pretreatment process for removal of hard substances must be preceded. In this study, we investigated the mechanism of removal of hardness through chemical precipitation. As a result, Ca was greatly influenced by addition of $Na_2CO_3$, and Mg was strongly influenced by pH. Also, the addition of NaOH and $Na_2CO_3$ enabled simultaneous removal of Ca and Mg, and showed a removal efficiency of 99.9% or more. Finally, the residual concentrations of Ca and Mg in the brine after the reaction were 0.14 and 0.13 mg/L, respectively. Saturation index was calculated using Visual MINTEQ 3.1, and solid phase analysis of the precipitate was performed by FE-SEM and PXRD analysis. It was confirmed that precipitate formed by the formation of calcite and brucite.

• 한국환경보건학회지
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• 제34권3호
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• pp.233-239
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• 2008

In order to improve reactor performance of existing sewage treatment plants, the feasibility of enhancing reactor performance by bioaugmentation using EM as bioaugmentation agent and the effects of anoxic: oxic time ratio on reactor performance were investigated. Continuous and intermittent aeration modes were compared under the 6 hr of HRT. Three different types of intermittent aeration modes, that is, 15 min, of anoxic:45 min of oxic, 30 min of anoxic: 30 min of oxic, and 45 min of anoxic: 15 min oxic respectively were chosen as test modes to study the effects of anoxic : oxic time ratios on reactor performance. The optimum anoxic: oxic time ratio was 30 min:30 min when considering simultaneous removal of organic, nitrogen and phosphorus. When applying EM into a continuously aerated reactor under the varying dosing rates of 50-200 ppm, reactor performance in terms of organic and nitrogen removal efficiencies was not improved at all. Nitrogen removal efficiency was increase when the EM dosing rate was increased. However the degree of improvement was slight when the EM was injected above 100 ppm. However optimum phosphorus removal was found at the EM dosing of 200 ppm. Thus it was found that optimum injection concentration of EM is 200 ppm. It is apparent that putting EM into a sewage treatment plant significantly affects the T-N removal efficiency of the reactor by enhancing denitrification efficiency especially in operational conditions of relatively long anoxic periods. To achieve reciprocal condition in a reactor with intermittent aeration it is necessary to enhance the reactor performance by EM injection. In the case of modifying existing continuously aerated reactors into intermittent aerated reactors, it is obvious that operating costs of aeration would be reduced by reducing aeration time when compared with existing conventional sewage treatment plants.

• 한국진공학회:학술대회논문집
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• 한국진공학회 2013년도 제45회 하계 정기학술대회 초록집
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• pp.257-257
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• 2013

In order to selectively remove oil and organic compound from water, silica nanoparticles with hydrophobic coating was used. Since silica nanoparticles are generally hydrophilic, removal efficiency of oil and organic compound, such as toluene, in water can be decreased due to competitive adsorption with water. In order to increase the removal efficiency of oil and toluene, hydrophobic polydimethylsiloxane (PDMS) was coated on silica nanoparticles in the form of thin film. Hydrophobic property of the PDMS-coated silica nanoparticles and hydrophilic silica nanoparticles were easily confirmed by putting it in the water, hydrophilic particle sinks but hydrophobic particle floats. PDMS coated silica nanoparticles were dispersed on a slide glass with epoxy glue on and the water contact angle on the surface was determined to be over $150^{\circ}$, which is called superhydrophobic. FT-IR spectroscopy was used to check the functional group on silica nanoparticle surface before and after PDMS coating. Then, PDMS coated silica nanoparticles were used to selectively remove oil and toluene from water, respectively. It was demonstrated that PDMS coated nanoaprticles selectively aggregates with oil and toluene in the water and floats in the form of gel and this gel remained floating over 7 days. Furthermore, column filled with hydrophobic PDMS coated silica nanoparticles and hydrophilic porous silica was prepared and tested for simultaneous removal of water-soluble and organic pollutant from water. PDMS coated silica nanoparticles have strong resistibility for water and has affinity for oil and organic compound removal. Therefore PDMS-coated silica nanoparticles can be applied in separating oil or organic solvents from water.

• 한국물환경학회지
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• 제23권2호
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• pp.206-215
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• 2007

The objective of this study was to establish the optimal system operating strategies for nitrogen and phosphorus removal through model simulation system built for advanced wastewater treatment targeting on simultaneous temporal/special phase isolation BNR process. The simulation system was built with unit process modules using object modules in GPS-X code. The system was well verified by field experiment data. Simulation study was carried out to investigate performance response to design and operation parameters, i.e. hydraulic retention time (HRT), solids retention time (SRT), and cycle time. The process operated at HRTs of 10~15 hours, longer SRTs, and cycle time of 2 hours showed optimal removal of nitrogen. The HRTs of 10~15 hours, SRTs of 20~25 days, and longer cycle time was optimal for phosphorus removal. Both simulation and field studies showed that optimal operating strategies satisfying both the best nitrogen and phosphorus removals include HRTs ranged 10~15 hours, SRTs ranged 20~25 days, and cycle times of 4~8 hours. The simulation system with modularization of generalized components in BNR processes was, therefore, believed to be a powerful tool for establishing optimal strategies of advanced wastewater treatment.

• 한국산학기술학회논문지
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• 제19권1호
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• pp.25-33
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• 2018

화석 연료의 고갈과 온난화 현상으로 인해 새로운 에너지원에 대한 관심이 급증하고 있다. 그 중에서 바이오가스는 유기성 폐기물 및 바이오매스를 혐기성 소화과정인 가수분해(hydrolysis), 산발효(acidogenesis), 유기산발효(acetogenesis), 메탄발효(methanogenesis)의 단계를 거쳐 발생되기 때문에 친환경적인 에너지자원으로 각광받고 있다. 그러나 바이오가스는 기존의 정제설비로는 제거할 수 없는 높은 미세분진 및 수분 함량으로 인해, 직접연소, 도시가스, 자동차용 연료 등 효율적인 이용을 위해서 정제시스템이 필요하다. 따라서 본 연구는 미세분진과 수분을 동시에 제거할 수 있는 정제과정의 전처리 방법으로써 원심력을 이용하는 냉각공정을 설계하였다. 원심력을 이용하여 분진을 제거하는 Cyclone 내 외부에 열교환기와 ID fan을 구성하여 주입되는 가스를 어는점 이하로 냉각시킴으로써 물안개를 형성시켜 분진입자를 제거하고, 일부 가스를 ID fan을 이용하여 재순환시켜 제거하는 고효율 냉각제어공정을 개발하였다. 수분제거는 유량(25~150L/min) 및 상대습도(60~95%)의 조건에서 시험하였다. 수분제거율은 상대습도 $95{\pm}5%$일 때 평균 80.8%, 입자제거율은 입자크기 $2.5{\mu}m$에서 평균 99.78%의 제거효율을 보였고, 수분과 입자의 동시제거효율은 수분 70.86%, 입자 99.67%의 평균값을 보여주었다.

• 유기물자원화
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• 제13권4호
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• pp.136-147
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• 2005

난분해성 유기물과 암모니아성 질소의 동시제거를 위해 간헐폭기 생물활성탄 유동상법을 이용하여 고농도 유기물함유 침출수에 대하여 실험을 수행하였다. 간헐폭기시 고려되어야 하는 폭기 시간과 비폭기 시간에 대하여 실험적 검토를 수행하였고 자동컴퓨터제어 가능성에 대하여 고찰하여 보았다. 그 결과 생물활성탄 유동상 반응조에 충전한 활성탄의 물리적 흡착능은 초기의 처리효율에 크게 기여하였으며 간헐폭기 생물활성탄 유동상에 의한 침출수 처리시 정상상태에 도달하는 시간은 40일 정도이었고 TOC와 암모니아성 질소 처리시 양호한 프로세스임을 알 수 있었다. 폭기 및 비폭기시간은 60분 폭기/60분 비폭기의 조건이 30분 폭기/90분 비폭기에 비해 처리효율이 양호하게 나타났고 고농도 유기물함유 침출수 처리실험에서 간헐폭기 생물활성탄 유동상에 의한 처리방법은 높은 TOC제거율, 질산화율 및 탈질율, 난분해성 유기탄소 제거율을 확인할 수 있었다. 또한 간헐폭기시 ORP 곡선의 변화에서 나타나는 굴곡점은 무산소상태의 종결점을 나타내는 파라메터로 이용가능하며 이를 간헐폭기 반응조의 최적 운전모드를 설정하는데 응용할 경우 소규모 자동화가 가능할 것으로 판단되었다.

• KSBB Journal
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• 제14권2호
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• pp.212-219
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• 1999

섬유성바이오매스로부터 lactic acid를 생산하기 위한 동시당화 및 추출발효공정의 성능과 조업특성을 조사하였다. 섬유소 가수분해효소 Cytolase CL과 lactic acid 발효군주 L. delbruecku를 사용한 동시당화발효(SSF)에서 생성물인 lactic acid의 저해작용이 심각하였다. SSF 도중 lactic acid의 제거를 위하여 선정한 IRA-400 수지의 lactic acid 흡착성능은 200mg/g dry resin 이었다 Lactic acid 제거의 효과는 초기 기질(cellulose)의 농도에 따라 Lactic acid 제거의 효과는 초기 기질(cellulose)의 농도에 따라 다르게 나타난다. 기질의 농도가 50g/L인 경우 단순 SSF의 반응시간 72시간에서 lactic acid의 농도가 304g/L이었고, 이온교환수지를 첨가한 SSF에서는 32.0g/L이었다. 반면에, 모사실험 결과, 초기 기질사용량이 100g/L 인 경우에는 수지첨가에 의한 lactic acid 제거시 lactic acid 생산수율이 약 60%에서 90%이상까지 증가된다. SSF의 각 반응식에서 pH의 의존성을 조사하여 실험식으로 표현하였다. pH에 따라 lactic aic의 생산량이 크게 변화하였으며, pH 4.5-5.0에서 최대의 생산량을 나타내었다.