The objective of this study is to develope natural and economical Naengmyun broth using stock prepared with chicken heads. Proper mixing ratio of chicken head stock and chicken breast broth was determined through the sensory evaluation. In order to find out the attributes of chicken head-chicken breast broth(CH-CB broth), chicken breast broth and beef brisket(BB) broth were mixed to the chicken head stock and compared the preference and chemical elements between the broths were compared. The appropriate mixing ratio for reinforcing the meat broth and savory flavor, of was determined to 3:7(w:w). The comparison of CH-CB broth's and CH-BB broth's elements showed that the amount of crude protein and ash was the same and, in the case of crude lipid, CH-BB broth had 0.01% more than CH-CB broth. In the case of the total amount of free amino acids, CH-CB broth had 1.6 times more than CH-BB broth. A survey with 50 consumers showed that was prefered between CH-CB broth and CH-BB broth. CH-CB broth with significance.

2013년 UNEP(United Nations Environment Programme)에서 미나마타 협약이 채택되어 수은의 전생애(Life-cycle) 관리를 요구하는 등, 수은(Mercury)은 장거리이동 및 생태계 축적 등으로 인해 인간의 건강 및 환경에 악영향을 끼칠 수 있기 때문에 국제적으로 우선순위 관리대상 물질로 관리되고 있다. 이러한 국제적인 움직임에 대응하기 위해 국내에서도 “국가 화학물질 기본계획”, “수은 폐기물의 환경 친화적 관리를 위한 기술 지침서” 및 “수은관리 종합대책” 등 다양한 제도 및 처리 방안을 준비하고 있다. 따라서 이러한 국내･외 수은 협약 및 정책에 대응하기 위해서는 국내 폐기물의 수은 배출실태 조사가 필요한 실정이다. 따라서 본 연구에서는 국내 수은 함유 폐기물의 배출시설 중 문헌조사와 국립환경과학원과 협의하여 수은 배출량이 많을 것으로 예상되는 산업폐기물 소각시설과 의료폐기물 소각시설을 선정하여 수은 물질흐름을 조사하였다. 본 연구에서는 2014년 대전광역시 소재의 산업폐기물소각시설(A시설)과 경상북도 경산시 소재의 의료폐기물소각시설(B시설)을 대상으로 수은의 물질흐름을 분석하고자 하였다. 본 연구에서는 산업폐기물 소각시설(A시설)과 의료폐기물 소각시설(B시설)의 공정도를 중심으로 연속3일 샘플링을 실시하였다. 따라서 물질흐름분석의 경계는 소각시설 공정도로 설정하여 연구를 진행하였다. 수집된 조사 데이터와 샘플링 데이터를 토대로 STAN 2.5 소프트웨어를 이용하여 물질흐름을 분석하였다. 본 연구 결과, 산업폐기물소각시설(A시설)의 수은처리량은 40.48±14.77 g/day으로 분석되었으며, 수은배출량 중 대기로 배출되는 양이 가장 많았으며 바닥재, 폐수처리슬러지로 많이 배출되는 것으로 분석되었다. 의료폐기물 소각시설(B시설)의 수은처리량은 DSI/FF/Scrubber기준(0.178)으로 54.16±8.59 g/day, DSI/Carbon Injection/FF(4.87)기준으로 124.54±37.46 g/day 으로 분석되었으며, 수은의 상당량이 내부에 축적되지 않고 대기 중 배출, 폐수 그리고 비산재로 많이 배출되는 것으로 분석되었다.

수은은 인체의 신경계뿐만 아니라 인체 내 다른 여러 부정적인 영향을 준다. 수은의 위해성이 알려짐에 따라 최근에는 국제적인 움직임으로 UNEP(United Nations Environment Programme)에서 수은협약(Minamata Convention on Mercury)이 채택되었다. 이 협약의 목적은 수은 및 수은화합물의 인위적 배출로부터 공중보건 및 환경을 보호하는 것이다. 주요 협약 내용을 살펴보면 수은 및 수은화합물의 생산부터 폐기까지의 전과정을 관리하고, 수은제품을 단계적 금지, 배출원 파악 및 배출량 저감 등 다양한 내용을 담고 있다. 국내에서는 국제 사회의 요구에 따라 환경부와 국립환경과학원을 중심으로 하여 수은 유통 기초조사 및 수은 함유 폐기물 배출 실태조사 등이 이루어지고 있다. 다만 아직까지 폐기물처리시설 내에서 수은의 거동특성에 대해 연구자료는 해외에 비해 다소 부족한 실정으로, 이에 대해 좀 더 자세히 살펴볼 필요가 있다. 따라서 본 연구에서는 수은함유 폐기물 처리시설 내 수은의 물질흐름분석을 통해 시설 내 수은의 거동특성을 자세히 살펴보고자 한다. 본 연구에서는 문헌조사를 통해 수은 배출이 많을 것으로 판단되는 시설을 선정하여 현장조사를 실시하였다. 현장조사를 통해 확보된 데이터와 시설 내 수은의 샘플링을 통해 수은의 물질흐름 데이터를 분석하였다. 물질흐름분석은 Stan 2.5 Software를 통해 실시하였다. 연구결과, 하/폐수처리시설에서는 수은의 상당량이 슬러지형태로 배출되는 것을 확인할 수 있었다. 또한 소각시설에서는 수은의 상당량이 비산재 형태로 배출되어 시설의 후단집진설비에 의해 폐기물로 배출되었다.

In this study, ibuprofen(IBP) degradation by the photochemical (UV/S2O8 2-) and sonochemical (US/S2O8 2-) processes was examined under various parameters, such as UV (10~40±5 W/L) and US (50~90±5 W/L) power density, optimum dosage of persulfate ion (S2O8 2-), temperature (20~60℃) and anions effect (Cl-, HCO3 -, CO3 2-). The pseudo‐first‐order degradation rate constants were in the order of 10-1 to 10-5 min-1 depending on each processes. The synergistic effect of IBP degradation in UV/S2O8 2- and US/S2O8 2- processes could investigated, due to the generation of SO4 - radical. This result can confirm from the produced H2O2 and SO4 2- concentration in each processes. IBP degradation rate affected by the S2O8 2- dosage, temperature, power and anion existence parameters. In particular, IBP degradation rate increased with the increase of the temperature (60℃) and applied power density (UV:40±5 W/L, US:90±5 W/L). On the other hand, anions effect on the IBP degradation was negative, due to the anion play as a the scavenger of radical.

Diethyl phthalate (DEP) is widely spread in the natural environment as an endocrine disruption chemicals (EDs). Therefore, in this study, ultrasound (US) and ultraviolet (UVC), including various applied power density (10-40 W/L), UV wavelengths (365 nm, 254 nm and 185 nm) and frequencies (283 kHz, 935 kHz) were applied to a DEP contaminated solution. The pseudo-first order degradation rate constants were in the order of 10-1 to 10-4 min-1 depending on the processes. Photolytic and sonophotolytic DEP degradation rate also were high at shortest UV wavelength (VUV) due to the higher energy of photons, higher molar absorption coefficient of DEP and increased hydroxyl radical generation from homolysis of water. Sonolytic DEP degradation rate increased with increase of applied input power and the dominant reaction mechanism of DEP in sonolysis was estimated as hydroxyl radical reaction by the addition of t-BuOH, which is a common hydroxyl radical scavenger. Moreover, synergistic effect of were also observed for sonophotolytic degradation with various UV irradiation.

In this study, Ibuprofen (IBP) degradation by the photo catalytic process was investigated under various parameters, such as UV intensity, optimum dosage of TiO2, alkalinity, temperature and pH of bulk solution. The pseudo-first order degradation rate constants were in the order of 10-1 to 10-4 min-1 depending on each condition. The Photocatalytic IBP degradation rate increased with an increase in the applied UV power. At high UV intensity a high rate of tri-iodide (I3 -) ion formation was also observed. Moreover, in order to avoid the use of an excess catalyst, the optimum dosage of catalyst under the various UV intensities (30 and 40 W/L) was examined and ranged from approximately 0.1 gL-1. The photo catalytic IBP degradation rate was changed depending on the alkalinity and temperature and pH in the aqueous solution. This study demonstrated the potential of photo catalytic IBP degradation under different conditions.

Diethyl phthalate (DEP) and nonylphenol (NP) are widely spread in the natural environment as an endocrine disruption chemicals (EDs). Therefore, in this study, ultrasound (US) and ultraviolet (UVC), including TiO2, as advanced oxidation processes (AOPs) were applied to a DEP and NP contaminated solution. When only the application of US, the optimum frequency for significant DEP degradation and a high rate of hydrogen peroxide (H2O2) formation was 283 kHz. We know that the main mechanism of DEP degradation is radical reaction and, NP can be affected by both of radical reaction and pyrolysis through only US (sonolysis) process and combined US+UVC (sonophotolysis) process. At combined AOPs (sonophotolysis/sonophotocatalysis) such as US+UVC and US+UVC+TiO2, significant degradation of DEP and NP were observed. Enhancement effect of sonophotolysis and sonophotocatalysis system of DEP and NP were 1.68/1.38 and 0.99/1.17, respectively. From these results, combined sonophotocatalytic process could be more efficient system to obtain a significant DEP and NP degradation.

Sediments of Little Scioto (LS) River in Ohio was contaminated by poor disposal of creosote from Baker Wood Creosoting Facility. Among the primary compounds of creosote, Polycyclic Aromatic Hydrocarbons (PAHs) are the most common ingredient. PAHs are known for toxic, carcinogenic and mutagenic compounds. There are many difficulties to remove the PAHs in nature environment because their characteristics are having a less water-solubility, volatile and low mobility properties as increasing the molecular weight. The generation of hydroxyl radicals (ㆍOH) and hydrogen peroxide (H2O2) forms as well as high temperature (5000 K) and pressure (1000 atm) by a physico-chemical effects of ultrasound during a cavitation collapse can promote the degradation and desorption of PAHs in sediment And it can also produces shock wave and microjets which are able to change the size and surface of particle in solid-liquid system as one of physical effects. Therefore, we explored to understand the role of particle size, the effect of elimination for PAHs concentration by ultrasound and optimize the conditions for ultrasonic treatment. The condition of various size of particles ( > 150㎛, < 150㎛) and solid-liquid ratio (12.5g/L, 25g/L) for the treatment was considered and ultrasonic power (430 W/L) with liquid – hexane extraction and microwave extraction method were applied after ultrasound treatment.