황산은 뛰어난 촉매제로서의 특성과 경제성으로 산업현장에서 다양한 화학 반응에 널리 사용되고 있다. 그러나 황산은 사용 후 재활용이 불가능하고 대량의 폐수를 발생시키는 특성이 있어 폐기과정에서 환경오염의 위험이 있으며 폐수 처리 과정에서 추가적인 비용 과 에너지가 소모된다. 본 연구는 황산을 대신할 수 있는 친환경 촉매제를 활용하여 폐수 의 배출을 줄이고 기업의 친환경 경영을 강화할 수 있는 방안을 모색하고자 실시되었다. 연구에서는 아민 산화반응을 위해 사용되는 말레인산 무수물 기반 고분자 촉매인 PIMA 과 POMA을 평가하여 피리딘 유도체의 아민 산화반응을 최적화하였다. POMA 촉매는 아연 피리치온 합성에 적용되었으며, 98% 이상의 선택성과 93% 이상의 합성 수율로 높은 촉매 활성을 보였다. 또한 촉매는 여과 과정을 통해 쉽게 회수되었으며, 회수율은 99.8% 를 초과하였고, 여러 번 사용 후에도 활성을 유지하였다. POMA 촉매는 전통적인 황산 촉매를 대체하여 폐수 발생에 의한 환경 부담을 최소화하고 기업의 ESG 경쟁력을 높이는 데 기여할 것으로 기대한다.

This paper aims to review the odor removal performance and operating parameters of pilot and full-scale chemical scrubbers, bioscrubbers, biofilters, and biotrickling filters for odor control in wastewater treatment plants. Based on the performance of full-scale facilities installed in wastewater treatment plants, empty-bed residence times were the shortest for bioscrubbers (7.5±2.5s), followed by chemical scrubbers (20±8.1s), biotrickling filters (22.2±26.2s), and biofilters (48±30s). The removal efficiencies of complex odors by biofilters, biotrickling filters, bioscrubbers, and chemical scrubbers were 97.7±1.9%, 87.7±15.6%, 89.0±9.0%, and 70.0%, respectively. The investment cost was the lowest for biofilters, followed by biotrickling filters, bioscrubbers, and chemical scrubbers. In addition, the operating costs of these deodorization technologies were in the following order: biofilters < bioscrubbers and biotrickling filters < chemical scrubbers. However, most studies on odor control for wastewater treatment processes have been conducted on a laboratory scale with model odors (single odorous compound or mixtures of 2-3 odorous compounds). Therefore, field research to develop deodorization technologies for wastewater treatment plants should be more actively conducted to accumulate data for the design and operation of full-scale deodorizing systems.

This study is to manufacture a titanium dioxide (TiO2) photocatalyst by recycling sludge generated using titanium tetrachloride (TiCl4) as a coagulant. Compared to general sewage, a TiCl4 coagulant was applied to dyeing wastewater containing a large amount of non-degradable organic compounds to evaluate its performance. Then the generated sludge was dried and fired to prepare a photocatalyst (TFS). Scanning electron microscope-energy dispersive X-ray spectroscopy (SEM-EDX), X-ray diffraction (XRD), and nitrogen oxide reduction experiments were conducted to analyze the surface properties and evaluate the photoactive ability of the prepared TFS. After using titanium tetrachloride (TiCl4) as a coagulant in the dyeing wastewater, the water quality characteristics were measured at 84 mg/L of chemical oxygen demand (COD), 10 mg/L of T-N, and 0.9 mg/L of T-P to satisfy the discharge water quality standards. The surface properties of the TFS were investigated and the anatase crystal structure was observed. It was confirmed that the ratio of Ti and O, the main components of TiO2, accounted for more than 90 %. As a result of the nitric oxide (NO) reduction experiment, 1.56 uMol of NO was reduced to confirm a removal rate of 20.60 %. This is judged to be a photocatalytic performance similar to that of the existing P-25. Therefore, by applying TiCl4 to the dyeing wastewater, it is possible to solve the problems of the existing coagulant and to reduce the amount of carbon dioxide generated, using an eco-friendly sludge treatment method. In addition, it is believed that environmental and economic advantages can be obtained by manufacturing TiO2 at an eco-friendly and lower cost than before.

The production process of ultra-pure water (UPW) involves dozens of unit processes such as reverse osmosis (RO), pretreatments, membrane degasifier, and several ion exchange processes. Recently, continuous electrodeionization (CEDI) has replaced the 2-bed and 3-tower (2B3T) ion exchange process. As a result, the majority of wastewater in UPW production now comes from the RO concentrate. The important of RO in UPW production is to produce high-quality water with a low ion concentration (around 1 mg/L) for CEDI feed water. Minimizing RO concentrate is essential to reduce the wastewater produced in the UPW production process. This can be achieved by maximizing the recovery of the RO system. However, increasing the recovery is limited by the water quality of the RO permeate. To ensure high-quality permeate water, the RO system is designed with a two-pass configuration. The recovery of each pass in the RO system is limited (e.g., < 85%) due to the expected increase in permeate water concentration at higher RO feed water concentrations. Interestingly, tests using 4-inch RO modules with low concentration feed water (≤ 35 mg/L as NaCl) revealed that the permeate concentration remains almost constant regardless of the feed water concentration. This implies that the recovery of the first RO pass can be increased as long as the average feed/concentrate concentration of the second RO pass is less than 35 mg/L. According to this design criterion for the RO system, the recovery of the first and second RO pass, with a feed water concentration of 250 mg/L as NaCl, can be increased up to 94.8% and 96.0%, respectively. Compared to the conventional RO system design (e.g., 70% and 80% for the first and second RO pass) for UPW production, this maximum recovery design reduces the volume of RO feed and concentrate by up to 38.4% and 89.2%, respectively.

합성폐수 내의 유기물(COD), 질산성 질소, 인산이온을 제거하기 위한 폐수처리 시스템 개 발을 위한 연구를 수행하였다. 먼저 COD는 HClO의 산화 반응에 의해 거의 100 % 제거되었으며 전기 화학적 처리에 의해 질산성 질소가 암모니아성 질소로 환원되지만, 암모니아성 질소는 HClO 처리에 의 해 질산성 질소로 재 산화 되었다. 암모니아성 질소는 가열 증발 처리에 의하여 거의 100% 제거 되었 으며 HClO 처리를 하여도 재 산화되는 암모니아성 질소는 나타나지 않았다. 인산 이온은 pH에 따라 금속 착염을 형성함으로써 침전 처리에 의해 제거할 수 있었으며 전기화학적 처리와 HClO 처리를 통 하여 COD 99.5 % 이상, 질소 97.3 %, 인 91.5 %의 제거 효율을 얻을 수 있었다.

터널 내 축적된 다양한 오염원들은 간헐적으로 수행되는 세척과정 중에 폐수로 배출되게 되며, 서울 시내 3개 터널 지점에서 수행된 수질분석결과 SS, CODCr, T-N, NH3-N, NO3-N, Zn, Cu, Cr(+6). Mn, Mg, Phenol. CN-, E-Coli 등이 고농도 형태로 배출되는 것으로 나타났다. 한편, 이러한 오염수질의 배출농도 특성은 터널 세척 폐수의 채취 방법, 세척횟수, 세척수량, 터널내벽 특성, 통행량, 배수 특성 등에 따라 다양한 농도범위를 보여주는 것으로 나타났다. 한편, 수집된 터널 세척폐수를 단순 중력침전을 이용하여 저감실험을 수행한 결과, CODCr는 80%, T-N, T-P는 각각 30, 90% 제거됨을 확인하였고, 중력침전 분리를 통하여 제거되지 않은 잔여 오염물질에 대하여 GAC 소재를 통한 흡착실험(터널 세척폐수 1l에 대하여 GAC를 50g을 투입) 결과, CODCr, T-N, Zn, Cu, Mn, Phenol, CN 항목에서 80% 이상 제거됨을 확인하였다.