• 공업화학
• /
• 제20권5호
• /
• pp.522-526
• /
• 2009

다양한 금속(Ru, Mn, Co, Fe)을 $Al_2O_3$와 $CeO_2$에 담지한 촉매를 이용하여 1,2-Dichlorobenzen (1,2-DCB) 제거를 위한 촉매산화 실험을 실시하였다. 이와 더불어 동시에 NOx 제거가 이루어져 단일 촉매층에서 산화/환원 이원 기능이 가능한 촉매를 연구하고자 하였다. 실험결과 1,2-DCB 산화제거효율은 Ru/Co/$Al_2O_3$, Mn-Fe/$CeO_{2}$, 상용촉매인 Cr/$Al_2O_3$ 순으로 나타났다. 또한 1,2-DCB 산화제거효율이 가장 우수하였던 Ru/Co/$Al_2O_3$는 Chlorobenzene (CB)의 분해실험에서도 VOC 제거에 있어서 잘 알려진 Pt-Pd/$Al_2O_3$ 보다 우수한 활성을 나타내었다. 또한 $Cl_2$와 같은 생성물에 의하여 활성의 저하 및 황에 대한 내피독성과 내구성에서 우수한 결과를 얻을 수 있었다. NOx 제거에 있어서도 $260^{\circ}C$에서 NOx 전환율이 70% 정도로 나타났다.

• 대한환경공학회지
• /
• 제32권8호
• /
• pp.761-766
• /
• 2010

본 연구에서는 인 및 암모니아 흡착에 효과적인 La(III) 및 제올라이트를 적절히 결합하여 호소수 및 연못 등의 질소 및 인을 동시에 효과적으로 제거할 수 있는 La(III)-zeolite 복합체 개발을 목적으로 하였다. 연구 결과 La(III)-zeolite 복합체 제조 시 최적 결합 비는 0.0048 La(III) g:1 zeolite g 인 것으로 나타났다. 복합체 제조 시 건조 온도는 인 흡착에 결정적인 영향을 주는 것으로 나타났는데 상온 건조가 가장 적합한 것으로 관찰되었다. La(III)-zeolite 복합체 최적 주입량은 4.052 g/L로 나타났다. La(III)-zeolite 복합체 주입 시 최적 흡착 시간은 90 분으로 나타났다. 수용액상에서 알칼리도의 존재는 암모니아 및 인흡착에 긍정적인 영향을 주는 것으로 관찰되었다. 상온에서 건조시킨 La(III)-zeolite 복합체는 용액 내에서 La(III)의 탈리 현상이 관찰되지 않았으며, 이는 La(III)-zeolite 복합체가 인을 흡착하여 바닥에 가라앉은 후 바닥으로부터 용출되는 인을 효과적으로 차단 할 수 있음을 의미한다.

• 공업화학
• /
• 제32권3호
• /
• pp.237-242
• /
• 2021

미세먼지와 함께 질소산화물, 황산화물, 휘발성 유기화합물, 암모니아 비롯한 유발물질에 대한 동시 저감기술은 엄격해지는 환경규제와 실질적인 저감효과 제고를 위해 꾸준히 주목받아 왔다. 오존산화에 의한 비수용성 질소산화물 고속산화 공정은 전통적으로 적용되고 있는 선택적 촉매환원 공정에 비해 공간절약형 시스템 적용을 가능하게 할 뿐만 아니라 운영비용 절감 측면에서 매우 효과적인 방법으로 평가되고 있으며 황산화물을 비롯한 산성가스와 동시 저감이 가능한 공정 구현이 가능하다는 장점까지 있다. 본 논문에서는 오존 고속산화 공정에 대한 기술 이슈 및 개발 동향을 소개하며 향후 산업적 이용 확대를 위한 개발 방향에 대해서 고찰하고자 한다.

• 상하수도학회지
• /
• 제23권5호
• /
• pp.527-537
• /
• 2009

Three sets of parallel MBRs (reactor No.1, reactor No.2, reactor No.3) maintaining an MLSS of 4,000 mg/L, 6,000 mg/L and 8,000 mg/L, respectively, were operated to investigate the effect of various HRTs and DO concentration of MBRs on the removal efficiency of organic matters and nitrogen. The HRTs were operated on 4 hr, 6 hr, 8 hr. DO concentrations were ranged 1.5~2.0 mg/L and 0.5~1.0 mg/L respectively on each HRT conditions. MBR was divided into an aerated part and non-aerated part by baffle placed under the water. DO concentrations were controlled by altering the position of baffle. In terms of TSS and CODCr, all systems had a similar level of the removal under varied HRTs and MLSS. TSS removal efficiency was more than 99% and CODCr removal was ranged 94~97% under all conditions. Under the same condition on the HRT and MLSS concentrations, DO concentrations did not affect the organic removal efficiency. On the nitrification efficiency, with high DO concentration, as HRT or MLSS increased, the slight increment of nitrification efficiency was observed. However, under the low DO concentration, increase of MLSS and HRT resulted in larger increase of the nitrification efficiency. At the same HRT and MLSS, the nitrification efficiency increased greatly with up to 16% as DO increased. When the HRT increased from 4hr to 8hr, the denitrification efficiency slightly increased under most of conditions. However, the increase of MLSS resulted in about 19~39% denitrification efficiency increment. MLSS concentrations showed great effect on the denitrification. The increase of the DO concentration at the same HRT and MLSS resulted in decrease of denitrification efficiency with up to 27%. In all systems, the denitrification efficiency had more influence on the TN removal efficiency than nitrification efficiency. So, MLSS concentration has greater effect on the TN removal than HRT and DO. The TN removal efficiency increased as MLSS increased with up to 37%. As a result, the highest TN removal efficiency was observed 79.0% at the condition showed the highest denitrification efficiency that DO of 0.5~1.0 mg/L, an HRT of 8 hr, and 8,000 mg/L of MLSS concentration were maintained.

• 한국물환경학회지
• /
• 제24권6호
• /
• pp.659-669
• /
• 2008

Two sets of four parallel activated sludge reactors (ASRs) maintaining an MLSS of 3000 mg/L were operated to investigate the effect of DO, HRTs and bio-contact media (BCM) packing ratios on the removal efficiency of organic matters and nitrogen. Packing ratios of BCM to BCM-ASR systems 1, 2, 3, and 4 were 0% (suspended growth only), 10%, 15% and 20%, respectively. All systems were operated at an HRT of 4 hr, 6 hr, and 8 hr, respectively; DO concentration was maintained 0.5~1.0 mg/L and 1.5~2.0 mg/L for each HRT condition. In terms of TSS, TCODcr and SCODcr removal efficiency, all systems had a similar level of the removal efficiency under varied HRTs, and DO. But organic removal efficiency of systems with BCM was approximately 3~5% higher than systems without BCM at the same HRT and the DO. About the nitrification efficiency, with high DO (1.5~2.0 mg/L), as HRT (4 hr, 6 hr, 8 hr) or BCM packing ratio increased, the slight increment of nitrification efficiency was observed. However, under the low DO (0.5~1.0 mg/L), increase of BCM packing ratio and HRT resulted in large increase of the nitrification efficiency. At the same HRT and BCM packing ratio, the nitrification efficiency increased greatly with up to 15% as DO increased. When the HRT increased from 4hr to 8hr, the denitrification efficiency slightly increased by 5~10% only, under all DO conditions. Systems with BCM had higher denitrification efficiency, ranged 62.7~91.1% than systems without BCM showed 32.1~65.6%. And the increase in BCM packing ratio from 10% to 20% resulted in about 14~16% denitrification efficiency increment. BCM packing ratio showed great effect on the denitrification. The increase of the DO (from 0.5~1.0 mg/L to 1.5~2.0 mg/L) at the same HRT and BCM packing ratio resulted in slight decrease of denitrification efficiency with up to 7% for systems with BCM. But for systems without BCM, the denitrification efficiency decreased with up to 28%. In all system, the denitrification efficiency had more influence on the TN removal efficiency than nitrification efficiency. So, BCM packing ratio (0%, 10%, 15%, 20%) has greater effect on the TN removal than HRT and DO. The TN removal efficiency increased as packing ratio of BCM increased with up to 45%. As a result, the highest TN removal efficiency was observed 73.7% at the condition showed the highest denitrification efficiency that DO of 0.5~1.0 mg/L, an HRT of 8 hr, and 20% of BCM packing ratio was maintained.

• 한국대기환경학회지
• /
• 제20권2호
• /
• pp.185-193
• /
• 2004

A catalyst with CuO ceramic filter for simultaneous treatment of dust and HAP was prepared and characterized. Catalytic ceramic filter can not only potentially achieve the substantial savings in energy but provide with effective optimization and integration of process for simultaneous removal of SO$_2$, NO$_{x}$ and particulates from flue gases. Catalytic ceramic filters remove simultaneously particulates on exterior surface of filters and reduce NO to $N_2$ and $H_2O$ by SCR (Selective Catalytic Reduction) process. Preparation of catalyst impregnated ceramic filter with disk shape (Ψ 50) follow the processing of alumino-silicate ceramic filter, support impregnation and catalyst impregnation (copper oxide). Preparation routes of alumino-silicate catalyst carrier suitable for production of catalytic filters practically were studied and developed using the sol-gel and colloidal processing, homogeneous precipitation and impregnation method. Characterization of the catalyst, catalyst carrier catalytic filter materials have been performed the using various techniques such as BET, XRD, TGA, SEM. Combination of the sol-gel and colloidal processing and impregnation method is recommended to prepare catalyst carriers economically for catalytic filter applications.s.

• Environmental Engineering Research
• /
• 제10권5호
• /
• pp.257-263
• /
• 2005

A batch and a continuous type experiments were conducted to test the conditions for simultaneous phosphorus release and uptake, and denitrification, taking place in one process. The bacteria able to denitrify as well as to remove phosphorus were evaluated for the application to biological nutrient removal(BNR) process. In the batch-type experiment, simultaneous reactions of phosphorus release and uptake, and also denitrification were observed under anoxic condition with high organic and nitrate loading. However the rate and the degree of P release were lower than that occurred under anaerobic condition. BNR processes composed of anaerobic-anoxic-oxic(AXO), anoxic-anaerobic-oxic(XAO) and anoxic-oxic(XO) were operated in continuous condition. The anoxic reactors in each process received nitrate loading. In the AXO process, P release in anaerobic reactor and the luxury uptake in oxic reactor proceeded actively regardless to nitrate loading. However in XAO and XO processes, P release and luxury uptake occurred only with the nitrate loading less than $0.07\;kg{NO_3}^--N$/kgMLSS-d. With higher nitrate load, P release increased and the luxury uptake decreased. Therefore, it appeared that the application of denitrifying phosphorus-removing bacteria (DPB) to BNR process must first resolve the problem with decrease of luxury uptake of phosphorus in oxic reactor.

• Journal of the Korean Association of Oral and Maxillofacial Surgeons
• /
• 제38권2호
• /
• pp.110-115
• /
• 2012

Ankylosed tooth is defined as 'the discontinuance of normal passive tooth eruption without any mechanical barrier'. Ankylosed tooth treatment is a challenge to dental clinicians. In treatment of maxillary molar ankylosis cases there are risks of oro-antral fistula, displacement of root fragments into the maxillary sinus, as well as the necessity for providing additional sinus bone augmentation for future implant placement. In this study, we suggested a new technique using a piezoelectric device and a lateral side approach to the maxillary sinus leading to the simultaneous removal of the ankylosed maxillary molar and sinus grafting for the purpose of implant site development.

• 공업화학
• /
• 제27권1호
• /
• pp.1-9
• /
• 2016

미세조류와 박테리아의 공배양 시스템은 두 미생물종이 공생적 관계가 있다면 한 배양기에서 BOD와 영양염류의 동시 제거가 가능하다. 이때 영양염류는 미세조류의 바이오매스 성분으로 전환된다. 이 총설은 미세조류와 박테리아의 공생적 혼합배양을 이용한 하폐수처리, 특히 질소와 인의 제거에서의 중요성과 최근의 연구동향을 살펴보았다. 미세조류는 광합성을 통해 산소를 발생시키고 박테리아는 이 산소를 전자수용체로 이용하여 유기물의 산화분해에 활용할 수 있다. 호기성 박테리아가 유기물을 산화할 때 발생되는 $CO_2$는 미세조류의 탄소원으로 섭취되어 탄소동화작용에 사용된다. 미세조류와 박테리아의 공배양은 상호 이익이 될 수도 있고 저해가 될 수도 있으므로 지속적인 영양염류 제거를 위해서는 상호 이익이 되는 공생적 관계가 필수적으로 요구된다. 이를 위해서는 하폐수처리에 사용되는 상용적인 두 미생물 종의 선택이 중요하다.

• 대한환경공학회지
• /
• 제37권6호
• /
• pp.340-348
• /
• 2015

본 연구에서는 해양퇴적물 내에 자연적으로 존재하는 철 성분과 과산화수소수를 이용한 유사-펜톤 공정에서 퇴적물의 입자크기 별 분율 내의 PCBs제거효율을 파악하고 여러 가지 계면활성제(Triton X-100, Tween 60, Tween 80)의 동시 사용에 따른 효율을 실험하였다. 퇴적물 시료를 1%와 15%의 과산화수소수와 Triton X-100, Tween 60, Tween 80을 이용하여 1시간 동안 처리 시 tPCBs제거효율은 24.1~46.7%로 나타났다. 퇴적물의 입자 크기, 오염형태에 따라 제거 효율의 차이는 있었으나, 과산화수소수와 계면활성제를 동시에 사용하여 처리한 퇴적물의 tPCBs 농도는 수저준설토사 유효활용 기준을 충족하였다. 또한 적절한 계면활성제를 유사-펜톤 반응에 첨가제로 사용시 낮은 산화제 농도 조건에서도 보다 높은 산화제 농도 조건에서의 제거효율과 유사하게 나타났다. 그러므로 유사-펜톤 반응과 계면활성제에 의한 처리에서 해양오염퇴적물의 미세입자에 함유된 PCBs를 효율적으로 정화하는 것이 가능한 것으로 확인되었다.