Bioreactors are devices used by sewage treatment plants to process sewage and which produce active sludge, and sediments separated by solid-liquid are treated in anaerobic digestion tanks. In anaerobic digestion tanks, the volume of active sludge deposits is reduced and biogas is produced. After dehydrating the digestive sludge generated after anaerobic digestion, anaerobic digested wastewater, which features a high concentration of organic matters, is generated. In this study, the decomposition of organic carbon and nitrogen was studied by advanced oxidation process. Ozone-microbubble flotation process was used for oxidation pretreatment. During ozonation, the TOC decreased by 11.6%. After ozone treatment, the TOC decreased and the removal rate reached 80.4% as a result of the Ultra Violet-Advanced Oxidation Process (UV-AOP). The results with regard to organic substances before and after treatment differed depending on the organic carbon index, such as CODMn, CODCr, and TOC. Those indexes did not change significantly in ozone treatment, but decreased significantly after the UV-AOP process as the linkage treatment, and were removed by up to 39.1%, 15.2%, and 80.4%, respectively. It was confirmed that biodegradability was improved according to the ratio of CODMn to TOC. As for the nitrogen component, the ammonia nitrogen component showed a level of 3.2×102 mg/L or more, and the content was maintained at 80% even after treatment. Since most of the contaminants are removed from the treated water and its transparency is high, this water can be utilized as a resource that contains high concentrations of nitrogen.

To suppress mold generation of yujacheong, Penicillium chrysogenum LB31 was cultured, and spores were harvested and put into yujacheong. Antioxidant activity, useful ingredients, mold size and incidence were investigated while storing yujacheong for 30 days, after sterilization with different methods (nontreatment, ozone gas emission, heating after ozone gas emission and heating). The results showed that the content of narirutin, naringin, hesperidin, or neohesperidin, which are functional components of yuzu, increased as the storage period increased in all the treatment units. In addition, mold generation was not observed until the 15th day in the heat treatment group after ozone gas emission. As the treatment group emitted ozone gas. molds of 34.8 and 112 mm2 in size were observed on the 30th day. These results suggested that ozone sterilization can prevent microbial contamination, further extending the shelf life of yuzacheong and maintaining a fresh state.

The purpose of this study was to investigate the effects of sterilization, storage period and washing yuzu, according to the washing method, during the storage period. The results showed that the fungus size increased as the storage period increased, and no mold occurred in the yuzu washed with ozone water until 20 days. After 30 days of storage, a mold of 124.1±13.9 mm2 was observed. The no-treatment sample had a fungus of 814.5±72.8 mm2 in size on day 0 and the fungus the largest fungus was 6,362±636.7 mm2 on day 30. In the case of water treatment, the fungus was 286.4±31.5~4,836.4±484.6 mm2 in size. The results of the study confirmed that washing yuzu with ozone water has a sterilizing effect.

This study aims to investigate the proper mixing treatment concentration of ozone (O3) and sucrose to preserve and extend the vase life of the cut rose flowers ‘Dominica’. The vase solution was prepared using tap water, 3% sucrose, ozone 5.5 mg L-1, and 3% sucrose with ozone 5.5 mg L-1. The vase life was the highest in the tap water and ozone treatments at 16.3 and 16.1 days, respectively. The vase life of ozone with sucrose treatment was 6.9 days, which was 9.4 days lower than that of the control. Compared to a single treatment, the vase life termination symptoms for ozone with sucrose treatment decreased petal wilting and increased bent necks. Relative fresh weight and vase solution uptake increased up to 4 days after treatment and decreased from 2 days before vase life termination. The rate of change in petal color was high in L*, a*, and b* for the sucrose treatment than after harvest, and low for the ozone treatments. The maximum relative flower size increase rates after treatment were 195% in the control, 186% in the sucrose treatment, 171% in the ozone treatment, and 155% in the ozone with sucrose treatment.

To investigate the effects of ozonated water concentration and soaking time on adventitious root formation of willow, we studied the efficiency of root cuttings in the revegetation technology of biological engineering of willows. The ozonated water concentrations were used for 5 minutes and 2 hours at 1, 5, 10, 15, 20 ppm by soaking method and then the shoot characteristics were observed. The number and length of adventitious roots were determined. The results indicated that 20 ppm of ozonated water for 2 hours and 1 ppm of ozonated water for 5 minutes resulted in leaves turned wither away and no adventitious root production. Considering the appearance, number and length of the adventitious root, soaking willow cuttings into the ozonated water with dissolved ozone concentration, 5 ppm for 2 hours and 10-15 ppm for 5 minutes were suitable for generating adventitious roots.

In this study, a manganese catalyst on the surface of a ceramic support was developed for the removal of odor emitted from barbecuing restaurants. Its ozone oxidation at room temperature was tested using acetaldehyde (CH3CHO), the most dominant compound in the barbecuing odor, and the ozonation efficiency under wet conditions was also studied. The manganese catalyst was made with the honeycomb-type ceramic support, and an acid pretreatment was applied to increase its specific surface area, resulting in an increase of the degree of dispersion of manganese oxide. The acetaldehyde removal efficiency using the manganese catalyst on the acidpretreated support (Mn/APS) increased by 49%, and the ozone decomposition rate and the CO2 conversion rate also increased by 41% and 27%, respectively. The catalyst without surface pretreatment (Mn/S) showed a low efficiency for the acetaldehyde ozonation, and other organic compounds such as acetic acid (CH3COOH) and nonanal (CH3(CH3)7CHO) were found as oxidation by-products. In comparison, CO2 was the most dominant product by the ozonation of acetaldehyde using the Mn/APS. When the relative humidity was increased to 50% in the influent gas stream, the acetaldehyde removal efficiency using the Mn/APS decreased, but only the production rates of CO2 and acetic acid were changed. As a result, the manganese oxide catalyst on the surface of the acid-pretreated honeycomb support manifested high acetaldehyde ozonation even at humid and room temperature conditions.

This study focused on natural organic matter and trihalomethane removal by ozonation with various ferrous concentration in surface water. Ozonation is more affected by injection concentration than reaction time. dissolved organic carbon removal rates in ozonation increased with the increase in ferrous concentration. The highest removal was obtained at 6 mg/L of ferrous concentration. When 1 mg/L of ferrous was added with 2 mg/L of ozone concentration, it was found to be a rapid decrease in specific ultraviolet absorbance at the beginning of the reaction because ferrous acts as a catalyst for producing hydroxyl radical in ozonation. As ozone concentration increased, trihalomethane formation potential decreased. When 2 mg/L of ozone was injected, trihalomethane formation potential was shown to decrease and then increase again with the increase in ferrous concentration.

Climate change is believed to increase the amount of dissolved organic matter in surface water, as a result of the release of bulk organic matter, which make difficult to achieve a high quality of drinking water via conventional water treatment techniques. Therefore, the natural water treatment techniques, such as managed aquifer recharge (MAR), can be proposed as a alternative method to improve water quality greatly. Removal of bulk organic matter using managed aquifer recharge system is mainly achieved by biodegradation. Biodegradable dissolved organic carbon (BDOC) and assimilable organic carbon (AOC) can be used as water quality indicators for biological stability of drinking water. In this study, we compared the change of BDOC and AOC with respect to pretreatment methods (i.e., ozone or peroxone). The oxidative pretreatment can transform the recalcitrant organic matter into readily biodegradable one (i.e., BDOC and AOC). We also investigated the differences of organic matter characteristics between BDOC and AOC. We observed the decreases in dissolved organic carbon (DOC) and the tryptophan-like fluorescence intensities. Liquid chromatographic - organic carbon detection (LC-OCD) analysis also showed the reduction of the low molecular weight (LMW) fraction (15% removed, less than 500 Da), which is known to be easily biodegradable, and the biopolymers, high molecular weight fractions (66%). Therefore, BDOC consists of a broad range of organic matter characteristics with respect to molecular weight. In AOC, low molecular weight organic matter and biopolymers fraction was reduced by 11 and 6%, respectively. It confirmed that biodegradation by microorganisms as the main removal mechanism in AOC, while BDOC has biodegradation by microorganism as well as the sorption effects from the sand. O3 and O3 + H2O2 were compared with respect to biological stability and dissolved organic matter characteristics. BDOC and AOC were determined to be about 1.9 times for O3 and about 1.4 times for O3 + H2O2. It was confirmed that O3 enhanced the biodegradability by increasing LMW dissolved organic matter.

본 연구는 넙치 양식장 시설 내로 유입되는 병원 미생물을 효과적으로 관리하기 위한 오존 처리 기준을 마련하고자 수행되었다. 유수식 환경에서 오존 주입량을 0.3∼3.0 mg O3 L-1의 범위로 주입하면서 3분의 반응시간을 가진 후 ORP 320~410 mV에서 TRO가 0.01±0.01 mg L-1가 검출되었으며, 600 mV와 700 mV에서 0.07±0.02 mg L-1와 0.16±0.03 mg L-1가 검출되었다. 오존 처리에 따라 총세균수는 80.6~97.9%의 제거율을 나타내어 오존 처리를 통한 미생물 제거효과는 분명하게 나타났다. 230 g 넙치를 8.0 kg m-2 밀도로 사육한 300~400 mV 실험구에서는 총세균수는 가장 낮은 값을 보였다. 특히 400~500 mV에서 Vibrio spp.와 그램음성균은 거의 검출되지 않았다. 일간사료섭취율은 300~500 mV에서 0.7% 이상을 나타내어 대조구인 자연해수보다 감소하지 않아 부작용이 적은 것으로 나타났다. 넙치 양식장으로 유입되는 병원 미생물은 유입수의 ORP 400 mV 수준에서 효율적으로 제거되는 것으로 조사되었다.

Water and wastewater treatment has always been a challenging task due to the continuous increase in amount and the change in characteristics of the poorly biodegradable and highly colored organic matters, as well as harmful micro-organisms. Advanced techniques are therefore required to successfully remove these pollutants from water before reuse or discharge to receiving water bodies. Application of ozone, which is a powerful oxidant and disinfectant, alone or as part of advanced oxidation process depends on the complex kinetic reactions and the mass transfer of ozone involved. Micro- and nano bubbling considerably improves gas dissolution compared to conventional bubbles and hence mass transfer. It can also intensify generation of hydroxyl radical due to collapse of the bubbles, which in turn facilitates oxidation reaction under both alkaline as well as acidic conditions. This review gives the overview of application of micro- and nano bubble ozonation for purification of water and wastewater. The drawbacks of previously considered techniques and the application of the hydrodynamic ozonation to synthetic aqueous solutions and various industrial wastewaters are systematically reviewed.

Optimal processes to remove chromaticity at E water treatment plant(WTP) mainly caused by algae of E lake in Jeju island were investigated based on lab-tests of chlorine and ozone oxidation. 42.9% of chromaticity of filtered water was removed by chlorine oxidation under pH 7.0∼8.0, dose of 1.0 mg/L with contact time of 30∼60 min. On the other hand, chromaticity removal was 71.4% when post-ozone dose of 0.9∼1.9 mg/L and pH 9.0, while it was increased to 86.7% under post-ozone dose of 3.1∼7.3 mg/L and pH 9.0. However, there was no significant chromaticity removal efficiency increase when ozone doses were higher than 5.0 mg/L regardless of feeding point(i.e., pre-ozonation and post-ozonation) and pHs(i.e., 7.0 and 9.0.) under the experimental conditions. Based on the results, chlorine oxidation using existing chlorination facilities at the WTP is recommended for lower chromaticity while ozone oxidation is recommended for higher chromaticity by installing new ozone feeding facilities.

본 연구는 플라즈마-촉매 및 오존 처리공정을 이용하여‘홍로’사과 저장과정에서 발생되는 에틸렌 을 제거하고자 하였다.‘홍로’사과는 저장온도가 증가할수록 호흡속도가 빨라져 산소농도는 급격히 감소하고 이산화탄소와 에틸렌 농도는 증가하였다. 특히, 저장온도 20℃에서 90시간 저장 후 산소가 모두 소모되었으며, 이산화탄소 농도는 약 20%로 증가하였다. 플라즈마-촉매와 오존 처리는 에틸렌 제거에 효과적인 것으로 나타났으나, 오존 처리의 경우 사과표면에 반점이 생기는 문제가 발생하였 다.‘홍로’사과의 품질 분석결과 가용성 고형분과 산도는 무 처리군에서 다소 높게 나타났으며, 경도 는 플라즈마-촉매 처리군와 오존 처리군에서 다소 높게 분석되었다. 하지만 유의적 차이는 나타내지 않았다.

본 연구는 오존수 침수처리가 소와 돼지 부산물의 미생물학적 안전성 및 품질특성에 미치는 영향에 대해 알아보고자 실시하였다. 미생물학적 안전성 및 품질평가를 위하여 총균 및 대장균수, 육색, 가열감량, 지방산패도를 측정하였으며, 처리구 설정은 처리하지 않은 대조구(Control)와 일반수돗물(10℃)로30분간 침수처리한 처리구 1(T1), 오존수(1.0ppm, 10℃)에 10분간 침수처리한 처리구 2(T2), 오존수에 20분간 침수처리한 처리구 3(T3) 및 오존수에 30분간 침수처리한 처리구 4(T4)로 분류하였다. 소 및 돼지의 간, 소창의 가열감량은 모든 처리구에서 유의적인 차이가 없었으며(p>0.05), 간보다는 소창에서 높은 가열감량을 보였다. 육색은 소의 간과 소창에서는 오존수 20 또는 30분 침수 처리시 황색도 값을 감소시키나, 명도 및 적색도 값에서 유의적인 차이가 나타나지 않았다(p>0.05). 지방산패도 측정 결과, 돼지 소창의 경우 일반수돗물 및 오존수 침지 처리시 대조구에 비해 낮은 지방산패도 값을 나타내었으며 오존수 침지 처리시 유의적으로 낮게 나타났다(p<0.05). 소 간의 경우 대조구에 비해 모든 처리구에서 유의적으로 높은 지방산패도 값을 보였으며 일반수돗물로 침지한 T1에 비해 오존수 침지시 낮은 지방산패도 값을 나타내었다. 총균 및 대장균수는 저장기간이 증가할수록 모든 처리구에서 유의적으로 증가하며(p<0.05), 대조구 및 T1에 비해 오존수 침지처리구에서 유의적으로 낮은 총균 및 대장균수를 나타내었다(p<0.05). 이상의 결과를 통해 오존수 침지처리는 축육부산물의 품질특성 저하 없이 미생물로부터 안전성 확보가 가능할 것으로 판단된다.

The aim of this study was to evaluate the chemical quenching system for residual ozone and to determine the operating condition for the quenching system. Hydrogen peroxide (H₂O₂) and sodium thiosulfate (Na₂S₂O₃) were investigated as quenching reagents for ozone removal, and the tendency of each chemical was notably different. In the case of H₂O₂, the degradation rate of ozone was increased as the concentration of H₂O₂ increase, and temperature and pH value have a significant effect on the degradation rate of ozone. On the other hand, the degradation rate of ozone was not affected by the concentration of Na₂S₂O₃, temperature and pH value, due to the high reactivity between the S₂O₃²- and ozone. This study evaluates the decomposition mechanism of ozone by H₂O₂ and Na₂S₂O₃ with consideration for the water quality and reaction time. Furthermore, the removal test for the quenching reagents, which can be remained after reaction with ozone, was conducted by GAC process.

The ozonation process has been widely used for drinking water disinfection around the world. Recently, the pressurized ozone contactor, in which the side stream typed ozone injection method is installed, has been applied to water treatment system. In this study, numerical calculations were conducted to compare prototype and screw-type ozone contactors based on hydraulic effectiveness in more details. The prototype ozone contactor was already installed and operated in domestic water treatment plant, and the screw-type is the suggested one for improving ozone contact efficiency installing the screw plate to the prototype. Screw turn numbers of screw plate were changed as 3, 5, 7 and 9, respectively for numerical simulation. The CT(concentration of disinfectant in mg/L times time in minutes) value was considered as one of the options for evaluating disinfection ability. From the results, it could be concluded that the performance of the screw-type is higher than that of the protype contactor by controlling the variable T as the tracer time. Also, Morill index of the screw-type(turn numbers = 5 ) appeared to be lower than the other.