• 한국축산식품학회지
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• 제42권4호
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• pp.625-638
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• 2022

This study aimed to carefully investigate the effect of hydrolysis using Flavourzyme on meat quality, antioxidative status, and taste-related compounds in breast of Samgyetang that was supplemented with black garlic (BG). Four different treatment groups were compared: (1) conventional Samgyetang (control), (2) Samgyetang hydrolyzed with Flavourzyme (1%, v/w) (FS), (3) Samgyetang made with the BG extract without hydrolysis (NBG), and (4) BG samgyetang pre-treated with Flavourzyme (1%, v/w) in a water bath at 55℃ for 2.5 h and hydrolyzed before being processed (HBG). All the treatment groups were cooked by retorting at conditions 121℃ and 1.5 kg/cm² for 1 h. Improved umami profiles through the increase of umami-related nucleotides (5c-GMP, 5'-IMP) and free amino acids-aspartic acid and glumtamic acid, in Samgyetang breast was recorded following hydrolysis. The HBG group tended to impart stronger scavenging activity toward free radicals compared with the other two groups, while not differing with NBG group regarding suppressing malondialdehyde. Textural properties were improved through hydrolysis, wherein the shear force value decreased from 2.29 kgf in the control to 1.19 and 1.25 kgf in the FS and HBG group. Moisture percentages were highly retained, with the redness score increasing and the lightness color decreasing following hydrolysis. In conclusion, the results of this study can be a preliminary information of the effect of hydrolysis pre-treatment for BG samgyetang. Further experiments are required to compare various enzymes along with its organoleptic acceptances.

• 상하수도학회지
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• 제9권4호
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• pp.87-96
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• 1995

The Electron/Hole Pair is generated when the activation energy produced by ultraviolet ray illuminates to the semiconductor and OH- ion produced by water photocleavage reacts with positive Hole. As a results, OH radical acting as strong oxidant is generated and then Photocatalytic oxidation reaction occurs. The photocatalytic oxidation can oxidate the non-degradable and hazardous organic substances such as pesticides and aromatic materials easier, safer and shorter than conventional water treatment process. So in this study, many factors influencing the oxidation of chlorophenols, such as inorganic electrolytes addition, change of oxygen and nitrogen atmosphere, temperature, pH, oxygen concentration, chlorophenol concentration, were throughly examined. According to the experiments observations, it is founded that the rate of chlorophenol oxidation follows a first-order reaction and the modified Langmuir-Hinshelwood relationship. And the photocatalytic oxidation occurs only when activation energy acting as Electron/Hole generation, oxygen acting as electron acceptor to prevent Electron/Hole recombination, $TiO_2$ powder acting as photocatalyst are present. The effects of variation of dissolved oxygen concentration, temperature and inorganic electrolytes concentration on 2-chlorophenol oxidation are negligible. And the lower the organic concentration, the higher the oxidation efficiency becomes. Therefore, the photocatalytic oxidation is much effective to oxidation of hazardous substances at very low concentration. The oxidation is effective in the range of 0.1 g/L-10 g/L of $TiO_2$. Finally when the ultra-violet ray is illuminated to $TiO_2$, the surface characteristics of $TiO_2$ change and Adsorption/Desorption reaction on $TiO_2$ surface occurs.

• 상하수도학회지
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• 제30권4호
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• pp.459-469
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• 2016

Gas hydrate desalination process is based on a liquid to solid (Gas Hydrate, GH) phase change followed by a physical process to separate the GH from the remaining salty water. The GH based desalination process show 60.5-90% of salt rejection, post treatment like reverse osmosis (RO) process is needed to finally meet the product water quality. In this study, the energy consumption of the GH and RO hybrid system was investigated. The energy consumption of the GH process is based on the cooling and heating of seawater and the heat of GH formation reaction while RO energy consumption is calculated using the product of pressure and flow rate of high pressure pumps used in the process. The relation between minimum energy consumption of RO process and RO recovery depending on GH salt rejection, and (2) energy consumption of electric based GH process can be calculated from the simulation. As a result, energy consumption of GH-RO hybrid system and conventional seawater RO process (with/without enregy recovery device) is compared. Since the energy consumption of GH process is too high, other solution used seawater heat and heat exchanger instead of electric energy is suggested.

• 공업화학
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• 제17권3호
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• pp.310-316
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• 2006

본 연구에서는 수중 악취의 원인 물질인 용존 암모니아를 제거하기 위해 분말형태의 활성탄을 사용하였다. 특히, 일반적인 분말활성탄은 암모니아 흡착능이 좋지 않기 때문에 흡착능을 높이기 위해 분말활성탄의 표면을 산 용액으로 함침시킨 산 첨착활성탄을 제조하였다. 이렇게 제조한 산 첨착활성탄을 섬유 재질로 된 다공성 지지막($10{\sim}50{\mu}m$)의 표면에 압력에 의한 분리 활성 여과 층을 형성시켜 흡착과 분리를 동시에 할 수 있는 혼합 공정을 구성하였다. 그 결과 혼합공정에서 암모니아 제거율이 60% 이상 되어, 일반 분말활성탄에 비해 10~15% 더 높은 흡착능을 보였다. 그리고 층이 형성된 동적막의 순수투과성능 실험을 보면 수투과도는 400~700 LMH로 정밀여과(Microfiltration)막 수준의 역할을 한다. 이는 수처리에서 기존의 분리막 공정보다 고효율적인 처리 유량을 유지하는 효과가 기대된다.

• 상하수도학회지
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• 제25권1호
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• pp.95-106
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• 2011

Even though MBR processes have many advantages such as high quality effluents, a small footprint and convenience for operation compared to conventional activated sludge processes, there are some shortcomings in terms of the cost and potential fouling incident that keeps MBR (Membrane bioreactor) processes from being widely applied. To reduce these problems, PTFE (Polytetrafluoroethylene) flat sheet membranes that have excellent permeability and durability were tested instead of PVDF (Polyvinylidene fluoride) membrane which is being used widely in water treatment. Low concentration of sodium hydroxide (NaOH) was also added into the membrane modules in order to prevent the membrane fouling as well as to provide the alkalinity. With conditions mentioned above, a pilot-scale MBR system based on the MLE (Modified Ludzack Ettinger) process was operated at flux of 40 $L/m^{2}/hr$ and over 15,000 mg/L MLSS concentration for about 8 months. And coagulant(alum) was added into the membrane tank to remove phosphorus. Although the more coagulant is added the more effectively phosphorus is removed, that can lead to fouling for a long operation(Ronseca et al.,2009). By the way there is a research that fouling grow up after stopping injection of coagulant(Holbrook, 2004). Stable operation of MBR systems was achieved without major chemical cleaning and the effluent quality was found to be good enough to comply with the treated waste water quality regulations of the Korea.

• 한국진공학회:학술대회논문집
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• 한국진공학회 2016년도 제50회 동계 정기학술대회 초록집
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• pp.251-251
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• 2016

For several decades, industrial processes consume a huge amount of raw water for various objects that consequently results in the generation of large amounts of wastewater. Wastewaters are consisting of complex mixture of different inorganic and organic compounds and some of them can be toxic, hazardous and hard to degrade. These effluents are mainly treated by conventional technologies such are aerobic and anaerobic treatment and chemical coagulation. But, these processes are not suitable for eliminating all hazardous chemical compounds form wastewater and generate a large amount of toxic sludge. Therefore, other processes have been studied and applied together with these techniques to enhance purification results. These include photocatalysis, absorption, advanced oxidation processes, and ozonation, but also have their own drawbacks. In recent years, electrochemical techniques have received attention as wastewater treatment process that could be show higher purification results. Among them, boron doped diamond (BDD) attract attention as electrochemical electrode due to good chemical and electrochemical stability, long lifetime and wide potential window that necessary properties for anode electrode. So, there are many researches about high quality BDD on Nb, Ta, W and Si substrates, but, their application in effluents treatment is not suitable due to high cost of metal and low conductivity of Si. To solve these problems, Ti has been candidate as substrate in consideration of cost and property. But there are adhesion issues that must be overcome to apply Ti as BDD substrate. Al, Cu, Ti and Nb thin films were deposited on Ti substrate to improve adhesion between substrate and BDD thin film. In this paper, BDD films were deposited by hot filament chemical vapor deposition (HF-CVD) method. Prior to deposition, cleaning processes were conducted in acetone, ethanol, and isopropyl alcohol (IPA) using sonification machine for 7 min, respectively. And metal layer with the thickness of 200 nm were deposited by DC magnetron sputtering (DCMS). To analyze microstructure X-ray diffraction (XRD, Bruker gads) and field emission scanning electron microscopy (FE-SEM, Hitachi) were used. It is confirmed that metal layer was effective to adhesion property and improved electrode property. Electrochemical measurements were carried out in a three electrode electrochemical cell containing a 0.5 % H2SO4 in deionized water. As a result, it is confirmed that metal inter layer heavily effect on BDD property by improving adhesion property due to suppressing formation of titanium carbide.

• 대한환경공학회지
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• 제27권1호
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• pp.52-58
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• 2005

국내 정수장의 약품공정을 향상시켜 저비용 고효율의 정수처리 공정을 확립할 목적으로 약품 분사용 초음파 분사 노즐의 적용가능성을 평가하였다. 초음파 분사노즐은 압전세라믹스를 이용하여 제작하였으며, 이 장치를 사용하여 상수 원수를 처리한 결과와 현재 대부분의 정수장에서 사용되고 있는 기존의 약품 혼화방식에 의한 오염물질의 처리효율을 비교 평가하였다. 그 결과 혼화방식에 따른 혼화지 내 응집제 혼화특성은 초음파 노즐에 의한 혼화방식이 기계식(back-mixing) 혼화방식보다 응집제의 확산속도가 빠른 것으로 조사되었다. 오염물질 별 제거효율 역시 기계식(back-mixing) 혼화방식보다 초음파 노즐에 의한 혼화방식의 제거효율이 높은 것으로 조사되어, 초음파 분사노즐을 이용한 약품 혼화방식을 실제 정수처리 공정에 적용할 경우 응집제의 과량 주입에 의한 처리효율의 저하를 방지할 수 있고, 후속 공정에 대한 부하량을 줄임으로서, 정수공정에 사용되는 약품을 절감시키고, 혼화지가 필요없게 되어 이로 인한 경제적 효과 뿐만 아니라 보다 순도가 높은 음용수를 생산 할 수 있을 것으로 기대된다.

• 한국축산시설환경학회지
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• 제17권3호
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• pp.181-188
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• 2011

돈분뇨 슬러리 2차 처리수를 대상으로 하여 오존과 과산화수소 등을 적용한 시험결과를 요약한 주요결과는 다음과 같다. 1. 동일한 시료에 동일한 처리시간 동안 처리하였을 경우, 주입한 오존 농도에 따라 처리수의 색도변화가 육안적으로 쉽게 확인할 정도의 차이를 나타냈다. 2. BOD와 COD 그리고 색도는 처리시간이 경과함에 따라 8.4 g/hr 오존 주입 수준에서의 제거효과가 다른 처리구에 비해 크게 나타났다. 반면에 SS는 오존 적용농도에 큰 영향을 받지 않는 것으로 나타났고, 질소와 인도 오존처리 효율이 높지 않은 것으로 나타났다. 3. 돈분뇨 슬러리 2차 처리수에 오존을 적용할 경우 색도 등 오염성 물질 제거효과와 더불어 생물학적 안정성 확보도 가능한 것으로 판단된다. 4. 돈분뇨 슬러리 3차 처리수에 과산화수소수를 첨가할 경우 2차 오염에 의한 잔존세균의 감소효과 및 암모니아 발산감소로 인해 돈분뇨 2차 및 3차 처리수의 중수도 개념으로서의 재활용 가능성에 대한 긍정적 요인으로 작용할 수 있는 것으로 판단된다.

• 콘크리트학회논문집
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• 제26권2호
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• pp.219-227
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• 2014

이 연구는 생물의 서식기반 제공 효과가 있는 다공질의 부석 및 포러스 콘크리트와 대사 작용 및 항산화작용에 의해 유기 오염물질을 분해시켜 오염된 하천수의 수질정화 효과가 있는 유용미생물을 동시에 이용하여 장기간 연속흐름시험을 통한 수질정화 특성을 검토하고자 하였다. 특히 기존의 미생물 탈리 등의 문제점을 해결하기 위하여 이 연구에서는 16S rDNA 염기서열 분석법에 의해 동정된 유용 미생물을 포러스 콘크리트 제조과정에서 각 단계별로 3차 처리하였으며, 최적의 연속흐름 실험을 위한 농도 및 체류시간별에 따른 기초실험을 통하여 운전조건을 검토하였다. 실험 결과 유용미생물을 적용한 포러스 콘크리트는 수질 및 생물에 대한 독성이 없는 것으로 나타났다. 그리고 일반 포러스 콘크리트 보다 유용미생물을 적용한 포러스 콘크리트가 우수한 제거효율을 나타내었으며, 150일 이상 큰 변화를 나타내지 않아 장기간 운전이 가능할 것으로 판단된다. 이와 같이 유용미생물을 적용한 포러스 콘크리트의 장기간 연속흐름 실험으로 오염물질 처리성능에 대한 검토를 통하여 오염된 수질을 향상시킬 수 있을 것이라고 판단되며, 실험과정 중 나타난 문제점들이 보완된다면 하천에 적용하여 유입되는 비점오염원을 저감시킬 수 있을 것으로 기대된다.

• 한국환경보건학회지
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• 제30권5호
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• pp.410-416
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• 2004

The objective of this investigation was to evaluate applicability of precoat filtration that can be substituted for rapid sand filter of conventional water treatment system(CWTS). Precoat filter used in this experiment are candle filter. Element disk of candle are pore size $10{\mu}m(R),\;20{\mu}m(B)$ And diatomaceous earth are cake pore size $3.5{\mu}m$(Standard Super- Cel; A), $7{\mu}m$(Hyflo Super-Cel; B) and $17{\mu}m$(Celite 545RV; C). $2kg/m^2$ diatomaceous earth is used for precoating, it coated candle in $5{\sim}6mm$ thickness. 1. Al adsorption dosages by diatomaceous earth used in experimental we Hyflo Super-Cel 0.843mg/g, Standard Super-Cel 0.782 mg/g and Celite 545RV 0.766 mg/g. 2. Filtrate of precoat filter during 60min are R-C combination 20.7($m^3/m^2$)>B-C 18.3($m^3/m^2$)>B-B 15.0($m^3/m^2$)> R-B 12.9($m^3/m^2$)> R-A 11,093($l/m^2$). 3. Water quality of precoat filter effluent are thus. $KMnO_4$ consumption are $1.10{\sim}2.20mg/l$, removal rate are $30.9{\sim}65.6\%$. They are R-A 1.10(mg/l)(removal rate $65.6\%$). R-C(2.20 mg/l)(removal rate $30.9\%$). 4. $Al^{3+}$ are not detected with all combination, removal rate $100\%$. 5. Considering water quality and flux, continued running time of R-A combination is 7 hr. Accumulated filtrate are $74.4 m^3/m^2$, average flux is $177.2 l/m^2{\cdot}min$. And filtrate per diatomaceous earth 1g are 37.2 l. 6. R-A effluent's water quality are $KMnO_4$ Consumption 1.10(mg/l), DOC 1.161 mg/1, Al 0.0 mg/1, $UV_{254}$ 0.016/cm, Turbidity 0.1(NTU). R-A combination is suitable to precoat filtration for the settling basin effluent treatment.