• 한국수처리학회지
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• 제26권6호
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• pp.53-59
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• 2018

Water pollution is drastically increasing day by day, because of the enhancement in use of livestock, urban sewage detergents and fertilizers. Moreover increase in concentration of phosphorous and nitrogen contained in sewage, leads to green tide problem in the rivers and causes marine pollution. For this problem to solve, several technologies are being researched and developed. Among them, this experiment is a study on Bench-scale STP based on internationally certified sewage treatment equipment by MEPC. 227(64) of IMO. The purpose of this study is to compare the biological treatment efficiency of phosphorus of Bench-scale STP. The ratio of C : N : P was set to 10 : 5 : 3 and 10 : 3 : 1 as the operating conditions. And the operation cycle was set to anoxic(mixed) 70 min - aeration 50 min (70-50), anoxic(mixed) 90 min - aeration 60 min (90-60). As a result, the phosphorous treatment efficiency was 88% at average, and the treatment efficiency was steady at 90-60 better than 70-50. The efficiency of the bench-scale STP has been verified through this experiment and additional experiments are required to derive the optimal operating conditions.

• 한국환경보건학회지
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• 제21권1호
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• pp.86-92
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• 1995

This study was performed to evaluate the effect of temperature on operating parameters for reactor in pig wastewater treatment using sequencing batch reactor method which is one of the biological treatment methods. Study was accomplished by experimental apparatus of bench scale, and the degradation rate coefficient and temperature correction factor were derived. The followings are the conclusions that were derived from this study. 1. In the characteristics of pig wastewater, concentrations of TKN and T-P were very high as 590 mg/l and 40 mg/l, respectively. 2. Removal efficiency of BOD and $COD_{Mn}$ as organic compound indicators were the highest mark as 97% at 25$\circ$C. 3. When temperature was incresed from 10$\circ$C to 25$\circ$C, removal efficiencies of TKN and T-P were proportionally increased. Especially, the former was greatly effected by temperature of reactor. 4. In experiment of bench scale, the degradation rate coefficients were increased as temperature increased, but decreased at the temperature range of 25~35$\circ$C. Temperature adjustment coefficients for $COD_{Mn}$, BOD, TKN and T-P were 1.1460, 1.1356, 1.1140 and 1.0565, respectively.

• 한국환경농학회지
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• 제20권4호
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• pp.225-231
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• 2001

퇴비화시 생물학적 활성을 증대하고 악취발생을 최소화 할 수 있는 적절한 공기주입율을 구명하고자 밀폐형 bench-scale reartor 퇴비화 시스템을 이용하여 시험을 수행한 결과는 다음과 같았다. 1) 공기주입율이 증가할수록 생물학적 활성은 증대하여 0.6 L/min/kg dry-solids 처리가 가장 높았고, 퇴비화 35일째의 퇴적물 품질도 가장 양호하였다. 2) 암모니아 평균 배출농도는 0.6 < 0.1 < 0.4 < 0.2 L/min/kg dry-solids 처리 순으로 낮았으며, 0.6 L/min/kg dry-solids 처리시 암모니아 배출농도는 0.2 L/min/kg dry-solids 처리에 비해 약 40% 수준에 불과하였다. 3) 계분톱밥 퇴비화시 주요 악취원인 황화합물 가스는 공기주입율이 낮을수록 배출농도가 높고 배출기간도 길어지는 경향이었으나, 0.6 L/min/㎏ dry-solids 처리에서는 전혀 검출되지 않았다. 4) 계분톱밥 퇴적물의 초기 수분함량을 60%로 조절하고 0.6 L/min/kg dry-solids의 공기주입율로 퇴비화할 경우 생물학적 활성증대로 인한 양질의 퇴비생산과 황화합물 및 암모니아에 대한 악취발생을 최소화 할 수 있을 것으로 기대되었다.

• 대한기계학회논문집B
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• 제25권10호
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• pp.1373-1383
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• 2001

The desulfurization characteristics of anthracite in a bench scale pressurized fluidized bed combustor are investigated. The coal used in the experiment is domestic anthracite from Kangwon Taeback area. The desulphurization experiment is performed with limestone from Chungbuk Danyang. The pressure of the combustor is maintained at 6 atm, and the combustion temperatures are 850, 900, and 950$\^{C}$. The superficial gas velocities are 0.9, 1.1, and 1.3 m/s. The excess air ratio is varied from 5 to 35%. The Ca/S mole ratios are 0.5, 1.5, 2.5 and 4.5 mole. All experiments are executed at 2m bed height. Consequently, SO$_2$ concentration in the flue gas is increased with incresing bed temperature and superficial gas velocity. However SO$_2$ concentration is decreased with incresing excess air ratio and Ca/S mole ratio.

• 한국환경농학회지
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• 제17권3호
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• pp.260-267
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• 1998

밀폐형 bench-scale reactor(242 l)에 thermocouples, oxygen sensor 및 datalogger 등을 연결하여 우분과 볏짚 혼합물의 퇴비화 촉진 및 양질의 퇴비생산을 위한 기초자료를 얻고자 공기주입량(0.09, 0.18, 0.90, 1.79 l $min^{-1}kg$ dry $solids^{-1}$)에 따른 생물학적 활성 변수들의 일시적이고 공간적인 변화를 모니터링한 결과는 다음과 같았다. 공기주입량이 높을수록 퇴비화 초기 및 뒤집기 이후 단계 모두 부숙온도의 증가 및 감속속도가 빨랐고 퇴적물과 배출공기의 온도차이는 적었으며, 모든 처리에서 퇴적물의 경우 $50{\sim}53^{\circ}C$에서 약 5시간 동안, 배출공기는 $45^{\circ}C$에서 약 $5{\sim}15$시간 동안 온도정지기를 보인 후 다시 증가하는 경향을 보였다. 최대온도는 퇴비화 초기단계에서는 공기주입량이 많을수록 감소하였지만 뒤집기 이후 단계에서는 1.79 l $min^{-1}kg^{-1}$처리를 제외하고는 그 반대 경향이었으며, 퇴적물의 최고온도 도달시간은 초기 및 뒤집기 이후 단계 모두 공기주입량이 적을수록 늦었다. $45^{\circ}C$이상의 고온 유지시간은 공기주입량이 증가할수록 급격히 감소하였고, 퇴비화 초기단계에 있어서 0.09 및 0.18 l $min^{-1}kg^{-1}$ 처리는 $65^{\circ}C$ 이상, 0.90 l $kg^{-1}$는 $55{\sim}64.9^{\circ}C$, 1.79 l $min^{-1}kg^{-1}$는 $45{\sim}54.9^{\circ}C$의 유지시간이 가장 길었다. 배출공기의 최저 산소농도 및 최대 산소비율은 공기주입량이 많을수록 높아지는 경향이었으나 그 수준에 도달하는 시간은 일정한 경향이 없었다.

• 한국환경과학회지
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• 제18권7호
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• pp.709-714
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• 2009

Catalytic activities of $V_2O_5/TiO_2$ catalyst were investigated under reaction conditions such as reaction temperature, catalyst size, inlet concentration and space velocity. A 1,2-dichlorobenzene(1,2-DCB) concentrations were measured in front and after of the heated $V_2O_5/TiO_2$ catalyst bed, and conversion efficiency of 1,2-DCB was determined from it's concentration difference. The conversion of 1,2-DCB using a pellet type catalyst in the bench-scale reactor was lower than that with the powder type used in the micro flow-scale reactor. However, when the pellet size was halved, the conversion was similar to that with the powder type catalyst. The highest conversion was shown with an inlet concentration of 100 ppmv, but when the concentration was higher or lower than 100 ppmv, the conversion was found to decrease. Complete conversion was obtained when the GHSV was maintained at below 10,000 $h^{-1}$, even at the relatively low temperature of $250^{\circ}C$. Water vapor inhibited the conversion of 1,2-DCB, which was suspected to be due to the competitive adsorption between the reactant and water for active sites.

• 한국가스학회지
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• 제17권4호
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• pp.51-57
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• 2013

천연가스 액화 공정은 상온의 천연가스를 상압 $-160^{\circ}C$ 이하로 냉각해서 액화시키는 공정으로, 안정된 LNG 생산을 위해서는 최적의 제어 전략이 필요하다. 제어 전략을 수립할 때 가장 중요한 작업 중 하나가 공정의 분석인데, 조절 변수의 변화에 따른 제어 변수의 변화를 파악하는 것이다. 본 논문에서는 C3MR(Propane Pre-cooled Mixed Refrigerant) 공정으로 BSU(Bench Scale Unit)를 제작하여 천연가스 액화 공정을 실험하였다. 각 조절변수의 조작에 따른 유량의 변화가 공정에 미치는 영향을 알아보기 위해서 냉매의 유량변화에 따른 냉매 온도 변화 및 천연가스의 온도 변화를 분석하였고, 천연가스 자체의 유량 변화에 따른 냉매의 온도 변화를 분석함으로써 3개의 조절 변수와 공정의 제어변수들과의 관계를 알아보았다. 각 제어변수들은 독립적인 요소들이 아닌 서로 연관되어 유기적인 움직임을 보였으나, 특정 조절 변수의 변화에 따라 큰 반응을 보이는 제어 변수를 확인 할 수 있었다.

• Environmental Engineering Research
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• 제21권3호
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• pp.297-303
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• 2016

Global warming due to greenhouse gases is an issue of great concern today. Fossil fuel power plants, especially coal-fired thermal power plants, are a major source of carbon dioxide emission. In this work, carbon capture and utilization using sodium hydroxide was studied experimentally. Application for flue gas of a coal-fired power plant is considered. Carbon dioxide, reacting with an aqueous solution of sodium hydroxide, could be converted to sodium bicarbonate ($NaHCO_3$). A bench-scale unit of a reactor system was designed for this experiment. The capture scale of the reactor system was 2 kg of carbon dioxide per day. The detailed operational condition could be determined. The purity of produced sodium bicarbonate was above 97% and the absorption rate of $CO_2$ was above 95% through the experiment using this reactor system. The results obtained in this experiment contain useful information for the construction and operation of a commercial-scale plant. Through this experiment, the possibility of carbon capture for coal power plants using sodium hydroxide could be confirmed.

• 한국환경과학회지
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• 제27권1호
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• pp.39-45
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• 2018

In this study, the International Maritime Organization (IMO)'s guideline MEPC. 277 (64) was developed and evaluated for the removal efficiency of T-N in a SBR and MBR combined process. This combined process of resized equipment based on large capacity water treatment device for a protection of marine aquatic life. In this experiment, T-N concentration of influent and effluent was measured through with the artificial wastewater. The SBR reactor operation time was varied according to the C : N : P ratios so that different conditions for mixing and aeration period in mins (90 : 60, 80 : 40, 70 : 50) and two C: N: P ratios (10 : 5 : 3, 10 : 3 : 1) were used. During experiment in the reactor's aeration and anoxic tank DO concentrations were 3 mg/L and 0.2 mg/L respectively. Furthermore, in the reactor MLSS concentration was 2000 mg/L and flowrate was 2 L/hr. Experiment results showed that C : N : P, 10 : 3 : 1 ratio with 90 mins mixing and 60 mins aeration maximized removal efficiency at 97.3% T-N as compared to other conditions. The application of the SBR and MBR combined process showed efficient results.

• 한국환경과학회지
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• 제6권2호
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• pp.133-139
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• 1997

말로네이트 제조 공정에서 발생되는 폐액으로부터 용매추출법을 적용하여 코발트 회수 연구를 하였다 용매 추출에서의 주요 변수는 용매의 선택, pH, 코발트 농도, 역추출 온도 등이며 이러한 변수들의 영향을 조사하였다. 용매로써 DEHPA와 PC88A가 사용되었으며 이들 용매의 평형추출 곡선을 구하였다. 공장설계 조건을 찾기 위하여 Mccabe-Tiele 선도를 작성하였고, 연속 공정인 믹서-세틀러 장치를 가동하였다. 본 연구 결과 폐액 중에서 코발트는 99.9% 이상 회수되었고, 회수된 황산코발트의 순도는 99.9% 이상이었다.