• 멤브레인
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• 제28권3호
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• pp.143-156
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• 2018

본 총설은 다양한 저널 게재 논문으로부터 분리막 및 광촉매의 혼성 정수/하수 처리 공정을 요약하였다. 이 총설에는 (1) 분리막 광촉매 반응기(membrane photoreactor, MPR), (2) 분리막 결합 광촉매 공정에서 막오염 관리, (3) 유기 오염물의 분해를 위한 광촉매 분리막 반응기, (4) 정수처리용 막분리 공정과 광촉매 분해의 결합, (5) 휴믹산 분해를 위한 광촉매 및 세라믹 막여과의 혼성공정, (6) 활성슬러지 여과를 위한 한외여과의 막오염에 이산화티타늄 나노입자의 영향, (7) 정수처리용 광촉매 및 정밀여과의 혼성시스템, (8) 선박 평형수 처리용 한외여과 및 광촉매의 혼성공정 및 (9) 분리막 및 광촉매 코팅 프로필렌 구의 혼성수처리 공정이 포함되어 있다.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2000년도 춘계학술발표대회
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• pp.133-136
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• 2000

In recent years, hybrid neural network approaches which combine neural networks and mechanistic models have been gaining considerable interests. These approaches are potentially very efficient to obtain more accurate predictions of process dynamics by combining mechanistic and neural models in such a way that the neural network model properly captures unknown and nonlinear parts of the mechanistic model. In this work, such an approach was applied in the modeling of a full-scale coke wastewater treatment process. First, a simplified mechanistic model was developed based on the Activated Sludge Model No.1 and the specific process knowledge, Then neural network was incorporated with the mechanistic model to compensate the errors between the mechanistic model and the process data. Simulation and actual process data showed that the hybrid modeling approach could predict accurate process dynamics of industrial wastewater treatment plant. The promising results indicated that the hybrid modeling approach could be a useful tool for accurate and cost-effective modeling of biochemical processes.

• Membrane and Water Treatment
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• 제10권2호
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• pp.155-163
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• 2019

The roles of polypropylene (PP) beads and pH on membrane fouling and treatment efficiency were investigated in a hybrid advanced water treatment process of tubular carbon fiber membranes (ultrafiltration (UF) or microfiltration (MF)) and PP beads. The synthetic feed including humic acid and kaolin flowed inside the membrane, and the permeated contacted the PP beads fluidized in the space between the membrane and the module with UV irradiation and periodic water back-flushing. In the hybrid process of UF ($0.05{\mu}m$) and PP beads, final resistance of membrane fouling ($R_f$) after 180 min increased as PP beads increased. The turbidity treatment efficiency was the maximum at 30 g/L; however, that of dissolved organic matters (DOM) showed the highest at PP beads 50 g/L. The $R_f$ strengthened as pH of feed increased. It means that the membrane fouling could be inhibited at low alkali condition. The treatment efficiency of turbidity was almost constant independent of pH; however, that of DOM showed the maximum at pH 5. For MF ($0.1{\mu}m$), the final $R_f$ was the minimum at PP beads 40 g/L. The treatment efficiencies of turbidity and DOM were the maximum at PP beads 10 g/L.

• 한국환경과학회지
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• 제23권9호
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• pp.1627-1634
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• 2014

Odor control technology include absorption, adsorption, incineration and biological treatments. But, most of processes have some problems such as secondary organic acids discharge at the final odor treatment facility. In order to solve the problems for effective treatment of organic acids in odor, it is necessary to develop a new type advanced odor control technology. Some of the technology are plasma only process and plasma hybrid process as key process of the advanced technology. In this study, odor removal performance was compared DBD(Dielectric Barrier Discharge)plasma process with PCHP(plasma catalysis hybrid process) by gaseous ammonia, formaldehyde and acetic acid. Plasma only process by acetic acid obtained higher treatment efficiency above 90%, and PCHP reached its efficiency up to 96%. Acetic acid is relatively easy pollutant to control its concentration other than sulfur and nitrogen odor compounds, because it has tendency to react with water quickly. To test of the performance of DBD plasma process by applied voltage, the tests were conducted to find the dependence of experimental conditions of the applied voltage at 13 kV and 15 kV separately. With an applied voltage at 15 kV, the treatment efficiency was achieved to more higher than 13 kV from 83% to 99% on ammonia, formaldehyde and acetic acid. It seems to the odor treatment efficiency depends on the applied voltage, temperature, humidity and chemical bonding of odors.

• 분석과학
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• 제18권6호
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• pp.535-541
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• 2005

본 연구에서는 오존/활성탄 혼합공정에서 부식산의 초기 pH(pH 3~pH 11)와 반응온도 ($0^{\circ}C$, $20^{\circ}C$, $40^{\circ}C$)를 변화시켰을 때 생성되는 알데히드류의 생성을 조사하였으며, 오존/활성탄 혼합공정 외에 활성탄 흡착과 오존 단독공정을 실험하여 공정에 따른 차이를 비교하였다. 오존 주입농도는 0.08g $O_3/g$ DOC, 활성탄 충진율은 16.5 v/v%였으며, 생성되는 알데히드류는 PFBOA법으로 전처리하여 GC/PDECD로 분석하였다. 오존/활성탄 혼합공정에서 생성되는 알데히드류를 분석한 결과, 포름알데히드와 글리옥살만이 검출되었으며, 그 생성량은 오존단독 공정에 비하여 오존/활성탄 혼합공정에서 더 적게 생성되었다. 오존/활성탄 혼합공정에서 부식산의 초기 pH를 변화시켰을 때, pH 11과 pH 7 에서 반응초기에 포름알데히드가 높은 농도(약 400 ppb)로 생성되었으며, 반응이 진행됨에 따라 포름알데히드와 글리옥살 농도는 모두 감소하는 경향을 나타냈다. 반응온도에 따른 실험에서는 온도가 가장 높은 $40^{\circ}C$에서 포름알데히드와 글리옥살이 가장 많이 생성되었으며, 이때 반응초기의 최고 농도는 각각 약 520 ppb, 120 ppb이었다.

• Korean Chemical Engineering Research
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• 제46권3호
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• pp.516-520
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• 2008

우리나라는 상수도시설의 노후화와 그 동안의 상수원 수질변화에 대응한 정수처리공정의 개량과 개선이 요구되어지고 있는 상황에 있어서, 기존의 정수처리공정에 어떠한 시설개량이나 설비의 보완 없이 DAF 공정을 추가하여 점토와 조류입자를 효과적으로 제거할 수 있는 DAF hybrid 공정의 적용성을 살펴보고자 일련의 실험을 실시하였다. DAF 공정의 설치위치는 조류입자의 제거에는 응집지나 침전지 전단을 이용하는 DAF-CGS 공정조합보다는 침전지 후단 또는 여과지 전단을 이용하는 DAF-CSF 방식이 더 효과적인 것으로 나타났다. 또한, DAF-CSF hybrid 공정을 도입함으로써 기존의 상수처리조건과 동일한 처리속도(수리학적 부하량)에서 처리효율이 향상될 것이며, 높은 수리학적 부하에서도 재래식 상수도시설에 적용하여 안정된 처리효율을 얻을 수 있을 것으로 판단되었다.

• Membrane and Water Treatment
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• 제11권4호
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• pp.275-282
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• 2020

Hranfa's marl, a local natural mineral, is selected for the decontamination by adsorption of aqueous effluents in textile industry. Its physicochemical characterization is first performed. It is composed mainly of Calcite, Quartz, Ankerite and Muscovite. Its specific surface area is 40 ㎡ g^-1. Its adsorption performance is then tested in batch conditions using an industrial organic dye, Bemacid Red E-TL, as a model pollutant. The measured adsorption capacity of Hranfa's marl is 16 mg g^-1 which is comparable to that of other types of natural adsorbents. A hybrid process is tested coupling adsorption of the dye on marl in suspension and microfiltration. An adsorption reactor is inserted into the circulation loop of a microfiltration pilot using ceramic membranes. This makes possible a continuous extraction of the treated water provided that a periodic replacement of the saturated adsorbent is done. The breakthrough curve obtained by analyzing the dye concentration in the permeate is close to the ideal one considering that no dye will cross the membrane as long as the adsorbent load is not saturated. These first experimental data provide proof of concept for such a hybrid process.

• 멤브레인
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• 제28권2호
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• pp.90-95
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• 2018

LNG-FPSO 산성가스 제거 공정에서 막-흡수 하이브리드 시스템 적용을 위한 설계를 수행하였다. 상용 공정 모사기인 Promax version 4.0을 이용하여 아민 흡수 공정과 하이브리드 공정의 산성가스 제거 성능을 비교하였다. 전사 모사 결과를 통해 하이브리드 공정은 아민 용매 순환량, 에너지 소모량, 장치 사이즈가 아민 흡수 공정에 비하여 작아지는 것을 확인할 수 있었다. 따라서, 컴팩트한 장치 사이즈와 에너지 절감 공정인 하이브리드 공정은 LNG-FPSO 천연가스 전처리 공정에 적용하기에 적합한 방안임을 확인하였다.

• 산업기술연구
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• 제28권B호
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• pp.47-52
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• 2008

In this study, GAC adsorption, ozonation and $O_3/GAC$ hybrid processes were investigated for treatment of humic acid. The degradation characteristics and efficiencies of humic acid in each process were evaluated through pH variation, $UV_{254}$ decrease, DOC removal, change of molecular size distribution and by-products formation. DOC removal rate in $O_3/GAC$ hybrid process (80%) was higher than arithmetic sum of ozonation (38%) and GAC adsorption process (19%) by synergism. $UV_{254}$ decrease rate of humic acid was also the highest than any other processes when treated in $O_3/GAC$ hybrid process. Molecular size distribution was not significantly changed in the GAC adsorption process. Main distribution of molecular size of humic acid was converted from 3 k~30 kDa into 0.5 k~3 kDa in ozonation. But the most of large molecular sizes of humic acid converted into small molecules(smaller than 0.5 kDa) in $O_3/GAC$ hybrid process. Quantities of formaldehyde and glyoxal formed in $O_3/GAC$ hybrid process were less than the ones in ozonation.

• 한국산업융합학회 논문집
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• 제26권6_2호
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• pp.1171-1181
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• 2023

In this study, a sweep gas - vacuum hybrid type membrane degassing process was proposed for ammonia wastewater treatment. In addition, the ammonia selective recovery of the hybrid type membrane degassing process was also investigated. As a result, the hybrid type membrane degassing process showed better degassing performance (54.9 mg NH₃/m²min for 360 min) than the sweep gas type (32.3 mg NH₃/m²min) or vacuum type (22 mg NH₃/m²min). Additionally, the hybrid type membrane degassing process showed an excellent ammonia selectivity (103 times compared to Na+ Na⁺, 133 times compared to Ca²⁺). The ammonia selectivity was appeared to be due to the conversion characteristics of ammonium ion / dissolved ammonia depending on pH. The results in this study are expected to be used in the development of ammonia wastewater treatment and ammonia recovery in the future.