• 한국농공학회지
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• 제16권4호
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• pp.3545-3554
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• 1974

The objective of this study was to investigate the characteristics of the evaporation rate, the plastic shrinkage and the compressive strength of concrete exposed to a rapid evaporation environment immediately after casting. Drying of concrete were conducted under a controlled chamber in which the temperature was mainfoimed at 30 ${\pm}$1$^{\circ}C$, the relative humidity 22 ${\pm}$1 percent, and the wind velocity 7 ${\pm}$1 m/sec. The compressive strength of concrete was tested after 28 days of standard curing. The results obtained are as follows: 1. The evaporation rate was the highest at the very beginning, was decreased as the drying progresses, and was kept almost constant after 6 hours. 2. The shrinkage of concrete was changed in three different rates for the concrete mixture having its slump vallue between 3.0cm and 7.5cm. 3. The plastic shrinkage was ended within 5 or 6 hours after casting, regardless of the water cement ratio. 4. The shrinkage was increased within the limit of slump values between 3.0cm and 7.5cm as the water-cement ratio was increased. 5. The evaporation was kept on even after the plastic shrinkage was ended. 6. Within the limit of good workability (slump value between 4.5cm and 7.5cm), the compressive strength of concrete was increased when the shrinkage rate was slow but it was decreased when the rate was rapid 7. From the result of this study it is recommended that (1) the water-cement ratio should be less as long as the workability of concrete is allowable; (2) the evaporation should be prevented at least for 4 hours after casting concrete.

• 한국세라믹학회지
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• 제53권6호
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• pp.597-603
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• 2016

Tantalum carbide, which is one of the ultra-high temperature ceramics, was deposited on graphite by low pressure chemical vapor deposition from a $TaCl_5-C_3H_6-Ar-H_2$ mixture. To maintain a constant $TaCl_5/C_3H_6$ ratio during the deposition process, $TaCl_5$ powders were continuously fed into the sublimation chamber using a screw-driven feeder. Sublimation behavior of $TaCl_5$ powder was measured by thermogravimetric analysis. TaC coatings have various phases such as $Ta+{\alpha}-Ta_2C$, ${\alpha}-Ta_2C+TaC_{1-x}$, and $TaC_{1-x}$ depending on the powder feeding methods, the $C_3H_6/TaCl_5$ ratio, and the deposition temperatures. Near-stoichiometric TaC was obtained by optimizing the deposition parameters. Phase compositions were analyzed by XRD, XPS, and Raman analysis.

• 한국산학기술학회논문지
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• 제17권6호
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• pp.199-206
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• 2016

본 연구는 다양한 세균에 오염된 신발을 효과적으로 살균하고 탈취할 수 있는 신발장을 설계하기 위한 최적의 조건을 확립하고자하는 목적으로 실시하였다. 신발장의 제작과 평가는 2014년 10월부터 2015년 9월까지 1년에 걸쳐 진행하였다. 항균성능의 평가는 JIS Z 2801:2010 규격에 따라 대장균과 황색포도상구균 균주에 대하여 실시하였고, 탈취효율은 한국공기청정협회 실내공기청정기 규격인 SPS-KACA002-132:2006 규격에 따라 실시하였다. 대장균과 황색포도상구균 균주에 대한 UV 조사시간에 대한 항균성능을 시험한 결과에서 30초 후에 99.9% 이상의 세균감소율을 보였고, 시험가스에 대한 평균 탈취효율은 42.5%를 보였다. UV램프로 5분의 점등과 25분의 소등을 반복하여 작동을 할 경우에 신발 내부와 신발장 내부 온도는 약 $40^{\circ}C$ 와 $25^{\circ}C$ 이하로 유지되었다. 신발장의 작동시간에 따른 온도 변화를 측정한 결과는 UV램프를 점등과 소등을 반복적으로 작동시켜 신발 내부의 온도를 적절하게 유지할 수 있었다. 결과적으로 실제 신발장 내부의 용적은 시험연구원의 챔버 용적보다 매우 작은 용적을 가지고 있기 때문에 시험결과의 값을 상대적으로 보정하게 되면 실제 탈취효율은 측정값보다 매우 클 것으로 판단이 된다. 또한 신발의 내부에서 악취를 유발하는 원인균인 박테리아를 반복적으로 살균하기 때문에 신발 내의 실제 탈취의 효과는 더욱 증가될 것이다. 추가 연구로 일정한 신발장 내부의 온도편차를 찾아야 할 것이다.

• 한국산업보건학회지
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• 제6권1호
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• pp.125-137
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• 1996

This study was designed to investigate effects of relative humidity on the breakthrough of charcoal tubes at a fixed vapor concentration and sampling time during mixed organic vapor sampling. A vapor generator was used to generate three different concentrations of mixed organic vapor and a stainless steel chamber was fabricated and utilized to maintain three different percentages of relative humidity while maintaining a constant temperature. The results were as follows; 1. At high relative humidity, breakthrough of mixed organic vapor occurred quickly at low vapor concentration than at high vapor concentration because of the reduced adsorption volume of charcoal tube due to humidity. 2. Breakthrough by competitive adsorption of vapors onto charcoal tube was observed at first from n-hexane having the lowest boiling point and highest vapor pressure among the three organic vapors investigated, followed by TCE. No breakthrough was observed from toluene under all experimental conditions. 3. For n-hexane, breakthrough was observed after 2 hours of sampling and breakthrough rates were increased as relative humidity increased. For TCE, breakthrough was found after 3 hours of sampling and breakthrough rates by sampling time were increased as vapor concentration increased. 4. The adsorbed amount of mixed organic vapor at breakthrough was shown to have statistically significant correlations with sampling time, relative humidity, and vapor concentration in descending order of correlation. Relative humidity and sampling time for n-hexane and sampling time and concentration for TCE were both statistically significantly correlated. 5. Relative humidity was found to affect the amount of breakthrough of mixed organic vapor and n-hexane. Among three percentages of relative humidity investigated, the amount of breakthrough at 85 % relative humidity was significantly larger than those of at lower percentages of relative humidity. No statistically significant difference was found between 25 % and 55 % relative humidity. 6. The results of multiple regression analysis between breakthrough and relative humidity, vapor concentrations showed that the coefficient of determination of mixed organic vapor was 0.263 and those of n-hexane and TCE were 0.275 and 0.189, respectively. 7. Flow rates of sampling pumps used were found to be affected by relative humidity present. At 25 %, 55 %, and 85 % relative humidity, the relative errors of sampling pump were 1.4 %, 13.4 %, and 18.6 %, respectively. In conclusion, the results of this study showed that high relative humidity could reduce the adsorption volume of charcoal tubes and subsequently increase breakthrough rates. Therefore, to prevent breakthrough when sampling mixed organic vapors, it is suggested that either sampling volume be reduced on the flow rate be lowered so as to minimize breakthrough of the most volatile organic vapor in the mixture. In addition, since the flow rates of a sampling pump can be adversely affected by high relative humidity, it is recommended to use a constant flow mode pump when sampling in the highly humid environment.

• 지질공학
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• 제14권4호
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• pp.401-416
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• 2004

이 연구에서는 물과 산성용액을 이용한 동결${\cdot}$융해실험을 통하여 강원도 횡성군에서 채취된 셰일의 물리적 특성변화를 측정하였다. 실험에 적용된 동결${\cdot}$융해 온도 범위는 $-20{\pm}2^{\circ}C\~15{\pm}2^{\circ}C$ 이고 시료는 12시간 동안 동결한 후 물속에서 8시간 동안 융해시켰다. 이 후 시료를 진공 챔버에서 4시간동안 수침하여 완전히 포화시켰으며, 이러한 일련의 과정을 1 cycle로 설정하였다. 본 연구에서는 매 5 cycle마다 시료의 흡수율, 탄성파 속도, 쇼어 경도, 슬래이크 내구성시험, 일축압축시험 등을 실시하였다. 동결${\cdot}$융해 실험의 반복횟수가 증가될수록 시료의 물성은 변화하였다. 일축압축강도는 물을 이용한 실험에서는 매cycle마다 0.40MPa정도 감소하였고 산성용액을 이용한 실험에서는 0.48Mra정도 감소하였으며, 탄성계수 역시 물에서 0.21Gpa, 산성용액에서 0.30GPa 감소하였다. 흡수율의 경우는 물에서 $0.29\%$, 산성용액에서 $0.37\%$ 증가되었다. 이러한 결과는 산성용액에서의 풍화속도가 물에서의 풍화속도보다 빠름을 지시한다. 그러나 탄성파속도, 쇼어경도와 슬레이크 내구성 시험에서는 물과 산성용액에 따른 차이가 거의 나타나지 않았다. 동결${\cdot}$융해 실험 결과와 연구지 역의 동절기 기간의 기온분포를 고려해 볼 때 실제 1년이 동결-응해 실험 약 $6\~12\;cycle$에 해당될 것으로 추정된다.

• 한국대기환경학회지
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• 제24권1호
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• pp.91-99
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• 2008

A multilayer tower-type photoreactor, in which $TiO_2$-coated glass-tubes were installed, was used to measure the vapor-phase BTEX removal efficiencies by ozone oxidation ($O_3$/UV), photocatalytic oxidation ($TiO_2$/UV) and the combination of ozone and photocatalytic oxidation ($O_3/TiO_2$/UV) process, respectively. The experiments were conducted under various relative humidities, temperatures, ozone concentrations, gas flow rates and BTEX concentrations. As a result, the BTEX removal efficiency and the oxidation rate by $O_3/TiO_2$/UV system were highest, compared to $O_3$/UV and $TiO_2$/UV system. The $O_3/TiO_2$/UV system accelerated the low oxidation rate of low-concentration organic compounds and removed organic compounds to a large extent in a fixed volume of reactor in a short time. Therefore, $O_3/TiO_2$/UV system as a superimposed oxidation technology was developed to efficiently and economically treat refractory VOCs. Also, this study demonstrated feasibility of a technology to scale up a photoreactor from lab-scale to pilot-scale, which uses (i) a separated light-source chamber and a light distribution system, (ii) catalyst fixing to glass-tube media, and (iii) unit connection in series and/or parallel. The experimental results from $O_3/TiO_2$/UV system showed that (i) the highest BTEX removal efficiencies were obtained under relative humidity ranging from 50 to 55% and temperature ranging from 40 to $50^{\circ}C$, and (ii) the removal efficiencies linearly increased with ozone dosage and decreased with gas flow rate. When applying Langmuir-Hinshelwood model to $TiO_2$/UV and $O_3/TiO_2$/UV system, reaction rate constant for $O_3/TiO_2$/UV system was larger than that for $TiO_2$/UV system, however, it was found that adsorption constant for $O_3/TiO_2$/UV system was smaller than that for $TiO_2$/UV system due to competitive adsorption between organics and ozone.

• 한국식품과학회지
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• 제10권4호
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• pp.398-403
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• 1978

고체입자를 열매체로 유동화시킨 유동층내에서 오징어를 고정시켜 건조시킬 때 유동화입자, grid로 부터의 오징어 고정위치, 온도가 오징어의 건조속도와 품질에 미치는 영향을 검토하였으며 또한 감율건조기간중 수분의 이동 메카니즘을 추론하였다. 1) 유동화입자로는 식염이 가장 바람직했고 풍속 3.8 m/sec에서 최적 유동화상태를 얻었다. 2) 유동층내에서의 균일온도 분포는 grid로 부터 4 cm 이상거리에서 얻었으며 따라서 오징어의 고정위치는 이 거리 이상에서 바람직한 것으로 관찰되었다. 3) 풍속 3.8m/sec, grid로부터 4 cm 이상되는 오징어의 고정위치에서 건조속도에 대한 최적온도는 $35^{\circ}C$에서 얻었으며 이 조건에서 초기수분 80.8%로 부터 최종수분 $18{\sim}22%$까지 건조하는 데 소요되는 시간은 8.5시 간 이었다. 4) 건조자료는 측정된 수분함량범위에서 비정상상태의 확산방정식 $ln{\frac{(W-We}{(Wc-We)}=-m{\theta}$의 경험식에 따랐으며 m의 값은 $0.32hr^{-1}$로 계산되었다. 또 이들 결과는 감율 건조기간중 수분의 이동이 액체확산에 의한 것임을 시사했다. 5) 오징어의 건조는 초기 짧은 시간 동안만 항율건조되고 그 이후는 감율건조에 의해 지배되는 것으로 나타났으며 동일온도에서 동일잔존수분까지 건조시키는 데 소요되는 유동층건조에 대한 통기 열풍건조의 건조시간비율은 1 : 1.4였다. 6) 유동충건조된 오징어 제품은 시판 천일건조 오징어 제품과 비교하여 품질상 유의차가 없었다.

• 한국수산과학회지
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• 제14권4호
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• pp.189-193
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• 1981

등온흡습곡선측정시의 건제품이 주어진 대상습도에서 평형에 이르는 시간을 단축시키기 위하여 조절기류를 이용하는 장치를 만들고, 이를 이용하여 $25^{\circ}C$에서 말쥐치 건제품의 등온흡습곡선을 측정하였다. 1. 조절기류를 이용함으로써 주어진 수분활성에서보다 높은 수분활성에 이르는 시간을 평균 45 시간으로 단축시킬 수 있었다. 2. 단분자의 수분함양은 고형물 1kg당 0.092kg이었으며, 건조말쥐치의 제품에 대하여 $8.42\%$였다. Symbols used in the text A : surface, $m^2$ $a_w$: water activity $A_s$ : specific surface, $m^2/kg$ dry matter C : constant related to the heat of adsorption $K_g$ : gas film coefficient of mass transfer, $kg water/hr{\cdot}Pa{\cdot}m^2$ n : number of molecular layers $n_s$ : moisture content, kg water /kg dry matter $n_{sa}$ : mean moisture content, kg water/kg dry matter $n_{se}$ : equilibrium moisture content, kg water/kg dry matter $n_{sm}$ : moisture content for monolayer, kg water/kg dry matter $P_g$ : saturated vapor pressure at wet-bulb temperature, Pa $P_a$ : partial vapor pressure of water in air, Pa $R_d$ : resistance factor against diffusion, $m^2{\cdot}hr/kg$ dry matter $R_s$ : resistance factor against drying, $m^2{\cdot}hr/kg$ dry matter R.H. : relative humidity, $\%$ $\varphi$ : R.H./100

• 광물과산업
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• 제26권
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• pp.1-12
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• 2013

In this study, an accelerated carbonation process was applied to stabilize hazardous heavy metals of industrial solid waste incineration (ISWI) bottom ash and fly ash, and to reduce $CO_2$ emissions. The most commonly used method to stabilize heavy metals is accelerated carbonation using a high water-to-solid ratio including oxidation and carbonation reactions as well as neutralization of the pH, dissolution, and precipitation and sorption. This process has been recognized as having a significant effect on the leaching of heavy metals in alkaline materials such as ISWI ash. The accelerated carbonation process with $CO_2$ absorption was investigated to confirm the leaching behavior of heavy metals contained in ISWI ash including fly and bottom ash. Only the temperature of the chamber at atmospheric pressure was varied and the $CO_2$ concentration was kept constant at 99% while the water-to-solid ratio (L/S) was set at 0.3 and $3.0dm^3/kg$. In the result, the concentration of leached heavy metals and pH value decreased with increasing carbonation reaction time whereas the bottom ash showed no effect. The mechanism of heavy metal-stabilization is supported by two findings during the carbonation reaction. First, the carbonation reaction is sufficient to decrease the pH and to form an insoluble heavy metal-material that contributes to a reduction of the leaching. Second, the adsorbent compound in the bottom ash controls the leaching of heavy metals; the calcite formed by the carbonation reaction has high affinity of heavy metals. In addition, approximately 5 kg/ton and 27 kg/ton $CO_2$ were sequestrated in ISWI bottom ash and fly ash after the carbonation reaction, respectively.

• 대한환경공학회지
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• 제34권12호
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• pp.787-791
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• 2012

실험실 규모의 음향정재파 장치를 이용하여 수체에 포함된 입자의 분리특성을 알아보았다. 음향정재파는 음파 또는 초음파와 유사한 파장으로 반사벽에 의해 발생된 파가 돌아오면서 일정한 파장을 형성한다. 이때 수중에 분산되어 있던 미세한 입자들은 음압이 0인 파장의 절점(node) 부분에 모이게 된다. 주파수 28.0 kHz와 1.0 MHz의 음향정재파 트랜스듀서를 이용하였고, 수체에 포함된 입자는 평균 입경 $6.8{\mu}m$의 카올린과 $100.5{\mu}m$의 레드머드를 사용하였다. 수체 내에 음향정재파가 형성되면 발생된 파장에 의한 음압으로 수온이 $0.15{\sim}0.20^{\circ}C/min $ 정도 상승된다. 카올린과 레드머드의 초기 농도는 0.1, 0.2, 0.3, 0.4, 0.5 g/L로 동일하게 제조하였다. 1.0 MHz의 주파수에서 5분경과 후 음향정재파가 가장 뚜렷하게 형성되었을 때의 반응조내의 탁도 제거율은 카올린은 18.2%~56.2%로, 입경이 큰 레드머드는 23.0%~53.6%의 분리효율을 나타내었다. 28.0 kHz 주파수에서는 입자분리가 이루어지지 않았다.