This study was conducted to evaluate the applicability of a carrier media with natural minerals as packing material in a biofilter to remove odor-causing compounds. The carriers were prepared by mixing powdered zeolite, barley stone, and clay. They have a pellet type with a length of 5m m to 10 mm, 3.2 m2/g of a specific surface area, and 0.04 cm3/g of a pore volume. The adsorption capacity and the biodegradation by biomass formation on the media were experimented with toluene and ammonia as the test compounds. The carrier possessed the ability to adsorb toluene and ammonia. The adsorption capacity of toluene and ammonia at the inlet concentration of 100 ppmv was 58 g/g and 96 g/g, respectively. In the biofilter using the carrier as the packing material, the biofilter performances were different depending on the supply of moisture and liquid-nutrient. The critical loading was found to be 33.13 g/m3/hr for toluene removal and 6.5g /m3/hr for ammonia removal even when no nutrients were supplied. The proposed material has been confirmed to be capable of adsorbing inorganic and organic compounds, and can be effectively applied as packing materials for the biofiltration.

Although membrane bio-reactor (MBR) has been widely applied for wastewater treatment plants, the membrane fouling problems are still considered as an obstacle to overcome. Thus, many studies and commercial developments on mitigating membrane fouling in MBR have been carried out. Recently, high voltage impulse (HVI) has gained attention for a possible alternative technique for desalting, non-thermal sterilization, bromate-free disinfection and mitigation of membrane fouling. In this study, it was verified if the HVI could be used for mitigation of membrane fouling, particularly the internal pore fouling in MBR. The HVI was applied to the fouled membrane under different conditions of electric fields (E) and contact time (t) of HVI in order to investigate how much of internal pore fouling was reduced. The internal pore fouling resistance (Rf) after HVI induction was reduced as both E and t increased. For example, Rf decreased by 19% when the applied E was 5 kV/cm and t was 80 min. However, the Rf decreased by 71% as the E increased to 15 kV/cm under the same contact time. The correlation between E and t that needed for 20% of Rf reduction was modeled based on kinetics. The model equation, E1.54t = 1.2 × 103 was obtained by the membrane filtration data that were obtained with and without HVI induction. The equation states the products of En and t is always constant, which means that the required contact time can be reduced in accordance with the increase of E.

막 생물 반응기(MBR)에서, 활성화 된 슬러지는 생물학적 성분을 분해하고 막 공정은 이 부유 물질인 박테리아를 분리시킨다. 그러나 MBR에서의 주요 문제는 ‘막 오염’이다. 이 리뷰에서는 ‘막 오염’을 극복하기 위하여 제시된 ‘복합막’을 논의하고 있다. ‘복합막’은 탄소 또는 비탄소 재료 포함하는 막으로 분류할 수 있다. 이 복합막의 친수성은 그래핀, 산화그래핀 (GO) 및 탄소 나노 튜브 또는 그들의 변형 된 부분을 깨끗한 막에 도입시킬 때 향상된다. 이산화규소(SiO2) 또는 이산화티타 늄(TiO2)과 같은 무기 물질 또한 막의 물 흐름을 증가시키기 위해 복합막 형성에 통합된다.

정삼투 여과막(FO) 기술 분야는 해수 담수화에서 이미 다양한 연구가 진행되었으나, 하폐수 처리 분야의 적용에서는 상대적으로 많은 연구가 필요한 상황이다. FO 기술은 비 다공성 특성막과 각 용액 사이의 삼투압 차이를 이용하여 원폐수로부터 수분을 비롯하여, 질소-인과 같은 이온성 물질까지 분리할 수 있다. 본 연구에서는 FO 막을 혐기성 유동상 미생물반응기(AFBR)를 통해 처리된 처리수 내 존재하는 질소(주로 암모니아성 질소)를 제거하기 위해 적용되었다. 유도용액(Draw Solution, DS)의 종류(NaCl, CaCl2, Na2CO3)에 따라 투과량은 NaCl, CaCl2, Na2CO3 순으로 높게 나타났으며, 암모니아성 질소의 배제율은 각각 42.25%, 78.83%, 70.35%으로 나타났다.

하폐수처리를 위한 분리막 생물반응기에서 막오염을 유발시키는 원인물질로 알려진 정족수감지 신호분자인 AHL과 AI-2를 동시 억제하는 연구를 하였다. AHL 분해 효소를 생산하는 BH4와 AI-2 불활성 물질을 분비하는 DKY-1를 각각 하이드로겔 담체에 고정시켜 분리막 생물반응기에 적용시킴으로써 막오염을 효과적으로 제어하고자 한다. 주기적으로 반응기의 신호분자 농도를 LC/MS/MS로 측정하였으며, 막투과 압력 증가 데이터를 바탕으로 막오염의 완화 정도를 살펴보았다. 이외에 총질소, 화학적 산소요구량, 미생물 플록 크기, 미생물 농도 등을 측정하여 반응기의 상태와 폐수의 처리효율을 비교 고찰하였다. 본 연구는 연구재단 이공분야 기초연구사업(NRF-2016R1A2B2013776)의 지원을 받아 수행되었습니다.

The lack of seed sludges for Ammonium Oxidizing Bacteria (AOB) and slow-growing ANaerobic AMMonium OXidation (ANAMMOX) bacteria is one of the major problem for large-scale application. In this study, 24m3 of single-stage SBR (Sequencing Batch Reactor) was operated to remove nitrogen from reject water using AOB and ANAMMOX bacteria cultivated from activated sludge in the field. The ANAMMOX activity was found after 44 days of cultivation in the ANAMMOX cultivation reactor, and then 0.66 kg N/m3/d of the nitrogen removal rate was achieved at 0.78 kg N/m3/d of the nitrogen loading rate at 153 days of cultivation. The AOB cultivation reactor showed 0.2 kg N/m3/d of nitrite production rate at 0.4 kg N/m3/d of nitrogen loading rate after 36 days of operation. The cultivated ANAMMOX bacteria and AOB was mixed into the single-stage SBR. The feed distribution was applied to remove total nitrogen stably in the single-stage SBR. The nitrogen removal rate in the single-stage SBR was gradually enhanced with an increase of specific activities of both AOB and ANAMMOX bacteria by showing 0.49 kg N/m3/d of the nitrogen removal rate at 0.56 kg N/m3/d of the nitrogen loading rate at 54 days of operation.

하수처리 혐기성 유동상 생물반응기(Anaerobic Fluidized Bed Bioreactor : AFBR)는 높은 표면적을 갖는 입상활 성탄을 유동 메디아로 적용함으로써 생물막 형성 및 유지에 유리하며 이로 인해 우수한 유기물 제거 효율을 나타내나 처리된 유출수 내의 질소와 같은 영양염류의 잔존이 여전히 문제로 남아있다. 본 연구에서는 AFBR에 의해 처리된 유출수 내의 질소 배제를 위하여 정삼투막(FO membrane)을 유도용액의 종류와 농도에 따라 적용하였다. 실험결과 유출수의 총질소 배제 효율 은 FO막에 적용하는 유도용액(draw solution : DS)의 종류 및 농도에 크게 의존하였다. 유도용액 농도가 증가함에 따라 FO막의 수투과량이 증가하였으며, 1 M의 NaCl을 유도용액으로 사용한 경우 총질소 배제 효율은 55%이었으나 1 M의 glucose를 유도용액을 사용한 경우 거의 완벽한 총질소 배제 효율을 나타내었다. AFBR 유출수를 FO막으로 24시간 동안 여과를 진행하 였으나 파울링에 의한 수투과량의 감소는 관찰되지 않았다.

The Anaerobic fluidized bed bioreactor (AFBR) treating synthetic wastewater to simulate domestic sewage was operated under GAC fluidization to provide high surface area for biofilm formation. Although the AFBR achieves excellent COD removal efficiency due to biological activities, concerns are still made with nutrient such as nitrogen remaining in treated wastewater. In this study, FO membrane was applied to treat the effluent produced by AFBR. Removal efficiency with total nitrogen (TN) was investigated with draw solution (DS, NaCl) and hydrodynamic condition (i.e., recirculation flow rate) along FO membranes. Permeability of FO membrane increased with increasing DS concentration. About 85% of TN removal efficiency was observed with the FO membrane using 1 M of NaCl DS. During operational period of a day, no permeate flux decline was observed.

Core/shell CdSe/ZnS quantum dots (QDs) are synthesized by a microfluidic reactor-assisted continuous reactor system. Photoluminescence and absorbance of synthesized CdSe/ZnS core/shell QDs are investigated by fluorescence spectrophotometry and online UV-Vis spectrometry. Three reaction conditions, namely; the shell coating reaction temperature, the shell coating reaction time, and the ZnS/CdSe precursor volume ratio, are combined in the synthesis process. The quantum yield of the synthesized CdSe QDs is determined for each condition. CdSe/ZnS QDs with a higher quantum yield are obtained compared to the discontinuous microfluidic reactor synthesis system. The maximum quantum efficiency is 98.3% when the reaction temperature, reaction time, and ZnS/CdSe ratio are 270℃, 10 s, and 0.05, respectively. Obtained results indicate that a continuous synthesis of the Core/shell CdSe/ZnS QDs with a high quantum efficiency could be achieved by isolating the reaction from the external environment.

Because freesia is a crop that is typically vegetatively propagated from offsets, a degradation in its genetic character or an onset of after successive culturing over a long period. To produce virus-free freesia corms, apical meristem culture and rapid mass propagation must be established. This study aimed to establish the rapid mass production of in vitro freesia corms using a bioreactor. Shoots (12 – 15 cm in height) obtained from tissue culture were used as the plant material in a balloon-type bubble bioreactor in which medium strength, sucrose concentration, inoculation plant volume, and medium exchange method were determined. Medium strengths tested included full strength (1), 1/2, and 1/4 strength MS medium; sucrose concentration 9% 12%, and 15%, and inoculation plant volumes were tested at 40, 80, 120, and 160 shoots/1L medium. MS medium was supplemented with a 1/2 volume of the initial volume or the medium was completely exchanged with a new medium or not exchanged at all throughout the experiment. Results indicated the best growth of freesia corms at 1/2 strength medium, 9% sucrose, 120 shoots/L medium, with complete medium exchange 4 weeks after initiating the experiment. Under these culturing conditions, corms with 0.5 g fresh weight, 0.15 g d ry w eight, 1 3 mm h eight, a nd 0 .9 mm diaeter were harvested from the bioreactor within only 6 weeks, which were large enough to be planted in field. Thus, our results indicated that the cost and period for the production of freesia corms in vitro can be markedly decreased.

막여과 생물반응기는 분리막 공정을 기반으로 한 생물학적 고도 하폐수 처리기술이다. 최근, 막여과 생물반응기 내의 고질적인 문제인 생물막오염을 근본적으로 해결하고자 미생물 간의 정족수 감지(quorum sensing)를 차단하는 정족수감지 억제(quorum quenching) 기술을 적용한 연구가 활발히 보고되고 있다. 이 기술을 침지형 중공사막 생물반응기에 적용할 때 중공사막 간격에 따라 막오염과 정족수 감지 억제 효과가 다를 수 있는데, 그러한 효과를 비교한 연구는 없었다. 따라서 본 연구에서는, 정족수 감지 억제 담체를 적용한 침지형 중공사막생물반응기 안에서 막 사이의 간격에 따른 막오염 정도와 막오염 방지 효과를 비교하였다.

평관형 알루미나 세라믹 멤브레인을 적용한 실험실 규모의 단독 혐기성 유동상 멤브레인 생물반응기 (Anaerobic Fluidized Bed Ceramic Membrane Bioreactor, AFCMBR) 하수처리 적용 가능성을 평가하였다. 단독 AFCMBR은 25℃에서 395일 간 합성폐수의 평균 유입 COD 260 mg/L에서 연속운전 되었다. 운전기간 동안 약 25 mg/L의 NaOCl 용액을 주입하여 주기적인 유지세정으로 멤브레인 투과플럭스 14.5-17 L/m².hr 달성이 되었다. 투과수의 용해성 COD는 1시간 HRT 에서 23 mg/L 이었고 고형물 발생량은 0.014 gVSS/gCODremoved였다. 단독 AFCMBR 운전 요구 전기에너지는 0.038 kWh/m³ 이었고 생산되는 메탄발생 전기에너지의 약 17%에 해당되었다.

In this study, UV irradiation reactors were used to eliminate 4 types of volatile organic compounds (VOCs) in various experimental conditions. The 4 types of VOCs used include acetone (AC), chlorobenzene (CB), dichloromethane (DCM) and methylbenzene (MB). An ozone producing low-pressure mercury lamp that emits UV irradiance at 254 nm and 185 nm was used. The tested operating conditions included UV light intensity, inlet VOCs concentrations, empty bed retention time (EBRT), background gas and relative humidity (RH) of the gas. Firstly, higher UV light intensity is confirmed to have higher VOCs removal efficiency (RE). Higher inlet VOCs concentration will result in lower VOCs RE, and the decreasing trends of different VOCs are not identical. At the same inlet VOCs concentrations, increasing the EBRT will result in a rise in VOCs RE, but a further increase in EBRT will bring about less enhancement in RE. Moreover, UV irradiation in oxygen has the highest VOCs RE compared with that in air and nitrogen gas (N2), indicating that photolysis and photooxidation are both important. Finally, there was no increase the VOCs RE at the increase in RH. All the experimental results indicate that an identical set of operating conditions should be applied when the removal capacities of different VOCs according to the UV irradiation amount are compared.

The objective of this study was to investigate design factors of the electrolysis reactor through the CFD(computational fluid dynamics) simulation technique. Analyses of velocity vector, streamline, chloride ion concentration distribution showed differences in flow characteristics between the plate type electrode and the porous plate type electrode. In case of the porous plate type electrode, chlorine gas bubbles generated from the anode made upward density flow with relatively constant velocity vectors. Electrolysis effect was more expected with the porous plate type electrode from the distribution of chloride ion concentration. The upper part of the electrolysis reactor with the porous plate type electrode had comparatively low chloride concentration because chloride was converted to the chlorine gas formation. Decreasing the size and increasing total area of rectifying holes in the upper part of cathodes, and widening the area of the rectifying holes in the lower part of cathodes could improve the circulation flow and the efficiency of electrolysis reactor.

An up-flow botanical bioreactor was proposed as an economical and environmentally-friendly control process to remove the odorants, specifically ammonia and hydrogen sulfide, in exhaust gas. Liriope Platyphylla and Hedera Helix were selected as the test plants, and were put into the lab-scale reactor filled with the ceramic media. During 52 days of operation with ammonia loading of 1.16 g/m3·d, Liriope Platyphylla showed better performance in ammonia removal. Liriope Platyphylla was further tested by the simultaneous loading of 6.96 g/m3·d for ammonia and 1.00 g/m3·d for hydrogen sulfide. Microbial activity in the botanical reactor was greatly enhanced by mixed odorants rather than single odorants, and can contribute to removing odor in the exhaust gas. Biological uptake by plants reached up to 20% of total nitrogen loading to the botanical reactor.