• Journal of the korean academy of Pediatric Dentistry
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• v.26 no.2
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• pp.350-364
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• 1999

The distribution of mast cells and nerves were investigated in the submandibular and sublingual glands of postnatal rats, using morphometric, histochemical and immunohistochemical techniques. Mast cells were observed in the submandibular and sublingual glands of postnatal development. Number of mast cells gradually increased in both glands following development. At birth, mast cells were relatively fewer in submandibular gland than those in sublingual gland, and they were mainly distributed in parenchymal tissues. At $2{\sim}4$ weeks, most of the mast cells were observed in the connective tissues, surrounding neurovascular elements, but some mast cells were closely related with the acini of submandibular gland. PGP 9.5 immunoreactive nerve fibers were found in the submandibular and sublingual glands of all developmental age. The nerve fibers were showed in varicose shape, and mainly located in adjacent area of ducts and vascular components of both glands. The number of nerve fibers were increased rapidly until 8 weeks, but they were not increased any more until 24 weeks. Therefore, it is suggested that mast cells and nerve fibers related with each other, and that their interactions may play roles not only in maturation of secretory units but also growth and differentiation of the tubular structures of the rat submandibular and sublingual glands during postnatal development.

• Journal of Bio-Environment Control
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• v.11 no.1
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• pp.5-11
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• 2002

In this study, new development of natural ventilation window was accomplished to control environment of greenhouse with no use of farced ventilation during hot season. The ventilation effect of developed ventilation window was investigated in experimental greenhouse which was designed using side wall panel and folding type panel fur natural ventilation. Folding panel type ventilation window was designed to open upper part of the side wall and top of the roof using two hinges which are located bottom of the side wall and the roof panel to grab one side of each panels and guide the other side along with the guidance rail. Developed ventilation window has top ventilation part with maximum moving distance X=ι (1-cos$\theta$)=848.5 mm and side ventilation part with maximum moving distance Y=ι/2 $\times$sin$\theta$=1,184.4 mm at 45$^{\circ}$ of theoretical opening angle. It took 4.5 minutes to open roof vent fully and temperature at 1.2 and 0.8 m height decreased after 1 minute from starting opening and became equilibrium state maintaining 3-4$^{\circ}C$ difference after 2 minutes from complete opening. Air exchange rate was 15.2~39.3 h$^{-1}$ which was more than 10~15 h$^{-1}$ of continuous type and Venlo type greenhouse. The descent effect of temperature by ventilation windows was two times higher than Venlo type greenhouse.

• Korean Chemical Engineering Research
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• v.53 no.6
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• pp.783-791
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• 2015

A fluidized-bed reactor with an inside diameter of 0.1 m and a height of 1.2 m was used to study the effect of steam and catalyst additions to air-blown biomass gasification on the production of producer gas. The equipment consisted of a fluidized bed reactor, a fuel supply system, a cyclone, a condenser, two receivers, steam generator and gas analyzer. Silica sand with a mean particle diameter of $380{\mu}m$ was used as a bed material and calcined dolomite ($356{\mu}m$), which is effective in tar reduction and producer gas purification, was used as the catalyst. Both of Korea wood pellet (KWP) and a pellet form of EFB (empty fruit bunch) which is the byproduct of Southeast Asia palm oil extraction were examined as biomass feeds. In all the experiments, the feeding rates were 50 g/min for EFB and 38 g/min for KWP, respectively at the reaction temperature of $800^{\circ}C$ and an ER (equivalence ratio) of 0.25. The mixing ratio (0~100 wt%) of catalyst was applied to the bed material. Air or an air-steam mixture was used as the injection gas. The SBR (steam to biomass ratio) was 0.3. The composition, tar content, and lower heating value of the generated producer gas were measured. The addition of calcined dolomite decreased tar content in the producer gas with maximum reduction of 67.3 wt%. The addition of calcined dolomite in the air gasification reduced lower heating value of the producer gas. However The addition of calcined dolomite in the air-steam gasification slightly increased its lower heating value.

• Elastomers and Composites
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• v.10 no.2
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• pp.136-156
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• 1975

고무는 불량열전도체(不良熱傳導體)이며 두께가 두꺼우면 내부(內部)가 적정온도수준(適正溫度水準)에 이르기 전까지 가황시간(加黃時間)이 길어진다. 가황온도(加黃溫度)가 상승(上昇)할수록 가황물(加黃物)의 물성(物性)은 열화(劣化)되는 경향(傾向이) 있다. 천연(天然)고무든지 합성(合成)고무든지 간(間)에 과가황(過加黃)에 대(對)한 저항성(抵抗性)이 나쁘므로 특(特)히 고온가황(高溫加黃)에 대(對)해 민감(敏感)하다. 이것은 고온(高溫)에서 단시간(短時間) 가황(加黃)일수록 가속(加速)된다. 평탄가황배합물(平坦加黃配合物)의 경우에서 보더라도 내부(內部)가 적절(適切)히 가황(加黃)되기도 전(前)에 외부(外部)는 과가황(過加黃)이 되는 수가 있다. 근래(近來) 발간(發刊)된 문헌(文獻)에서도 이러한 내용(內容)이 잘 설명(說明)이 되어 있는데 다른 각도(角度)에서 고찰(考察)해 볼것 같으면 정체시간(停滯時間)이 비교적(比較的) 길지 않는 한(限) 가황시간(加黃時間)은 정체시간(停滯時間)과 sheet 가황시간(加黃時間)과의 합(合)이라고 말할 수 있겠다. 예(例)를 들어 설명(說明)하자면 $130^{\circ}C(266^{\circ}F)$에서 정체시간(停滯時間)이 10분(分)이고 sheet 가황시간(加黃時間)이 20분(分)인 제품(製品)은 이 온도(溫度)에서 30분간(分間) 가황(加黃)해야 된다는 것이다. 온도계수(溫度係數)를 2라고 가정(假定)할 경우 $140^{\circ}C(284^{\circ}F)$에서의 가황시간(加黃時間)은 $30\times\frac{1}{2}=15$분(分)이 아니라 $20\times\frac{1}{2}+10=20$분(分)이 된다. 크기가 큰 제품(製品)은 보통(普通) 다음에 있는 여러 방법(方法)들 가운데 한 가지 또는 여러가지를 조합(組合)하여 가황(加黃)시킨다. a) 크기가 작은 것에 대한 것 보다 낮은 온도(溫度)에서 가황(加黃)한다. b) 침투가황-제품(浸透加黃-製品)을 가압하(加壓下)에 두고서 외부가황(外部加黃)은 단속(斷續)시키고 열(熱)이 중심(中心)으로 침투(浸透)하게 한다. c) 단계가황(段階加黃)-처음에는 저온(低溫)에서 시작(始作)하여 일정간격(一定間隔)을 두고 점차(漸次) 온도(溫度)를 상승(上昇)시켜 최종적(最終的)으로 가황온도(加黃溫度)까지 올린다. d) 가능(可能)하다면 metal base나 금형(金型)에서 고무를 증기가황(蒸氣加黃)시킬 경우에 있어서 속이 빈 축(軸)을 사용하여 내부(內部)로 부터 가열(加熱)하면 가황시간(加黃時間)이 단축(短縮)된다. e) 냉각중(冷却中)의 후가황(後加黃)-이것은 가열장치(加熱裝置)에서 끄집어낸 후 제품(製品)의 외부(外部)를 냉각(冷却)시키는 방법(方法)이다. 가열(加熱)된 제품(製品)이 쌓여 있거나 적절(適切)하게 냉각(冷却)되지 않을 때 가황(加黃)이 추가적(追加的)으로 되거나 과가황(過加黃)이 될 우려가 있는 제조공정(製造工程)에서는 흔히들 이 방법(方法)을 무시(無視)하고 있다. 여기서 강조(强調)해 두어야 할 것은 항상 제품(製品)의 외부(外部)를 완전(完全)히 가황(加黃)시킬 필요(必要)는 없다는 것이다. 다공성(多孔性)이나 기포생성(氣泡生成)을 조장(助長)하는 불량가황상태(不良加黃狀態)와 표면(表面)에서의 과가황상태간(過加黃狀態間)의 균형(均衡)을 취(取)해 줘야 하는데 물론(勿論) 이때는 가황시간(加黃時間)을 단축(短縮)시켜야 한다는 경제적(經濟的)인 측면(側面)도 아울러 고려(考慮)해야 한다. 이것은 고무기술자(技術者)가 당면(當面)해야할 과제(課題)에 속(屬)하며 바람직 한것은 본장(本章)의 내용(內容)이 여러 상황하(狀況下)에서 당면(當面)한 문제(問題)에 대(對)해 어떻게 대처(對處)해 야 할지를 모르는 여러 기술자(技術者)들에게 도움이 되었으면 하는 것이다.

• Journal of Bio-Environment Control
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• v.11 no.4
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• pp.151-156
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• 2002

Root zone cooling, such as soil or nutrient solution cooling, is less expensive than air cooling in the whole greenhouse and is effective in promoting root activity, improving water absorption rate, decreasing plant temperature, and reducing high temperature stress. The heat transfer of a soil cooling system in a plastic greenhouse was analyzed to estimate cooling loads. The thermal conductivity of soil, calculated by measured heat fluxes in the soil, showed the positive correlation with the soil water content. It ranged from 0.83 to 0.96 W.m$^{[-10]}$ .$^{\circ}C$$^{[-10]}$ at 19 to 36％ of soil water contents. As the indoor solar radiation increased, the temperature difference between soil surface and indoor air linearly increased. At 300 to 800 W.m$^{-2}$ of indoor solar radiations, the soil surface temperature rose from 3.5 to 7.$0^{\circ}C$ in bare ground and 1.0 to 2.5$^{\circ}C$ under the canopy. Cooling loads in the root zone soil were estimated with solar radiation, soil water content, and temperature difference between air and soil. At 300 to 600 W.m$^{-2}$ of indoor solar radiations and 20 to 40％ of soil water contents,46 to 59 W.m$^{-2}$ of soil cooling loads are required to maintain the temperature difference of 1$0^{\circ}C$ between indoor air and root zone soil.

• Journal of Korean Society of Environmental Engineers
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• v.34 no.7
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• pp.459-466
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• 2012

In order to improved treatment performance of dielectric barrier discharge (DBD) plasma, plasm + UV process and gas-liquid mixing method has been investigated. This study investigated the degradation of N, N-Dimethyl-4-nitrosoaniline (RNO, indicator of the generation of OH radical). The basic DBD plasma reactor of this study consisted of a plasma reactor (consist of quartz dielectric tube, titanium discharge (inner) and ground (outer) electrode), air and power supply system. Improvement of plasma reactor was done by the combined basic plasma reactor with the UV process, adapt of gas-liquid mixer. The effect of UV power of plasma + UV process (0~10 W), gas-liquid mixing existence and type of mixer, air flow rate (1~6 L/min), range of diffuser pore size (16~$160{\mu}m$), water circulation rate (2.8~9.4 L/min) and UV power of improved plasma + UV process (0~10 W) were evaluated. The experimental results showed that RNO degradation of optimum plasma + UV process was 7.36% higher than that of the basic plasma reactor. It was observed that the RNO decomposition of gas-liquid mixing method was higher than that of the plasma + UV process. Performance for RNO degradation with gas-liquid mixing method lie in: gas-liquid mixing type > pump type > basic reactor. RNO degradation of improved reactor which is adapted gas-liquid mixer of diffuser type showed increase of 17.42% removal efficiency. The optimum air flow rate, range of diffuser pore size and water circulation rate for the RNO degradation at improved reactor system were 4 L/min, 40~$100{\mu}m$ and 6.9 L/min, respectively. Synergistic effect of gas-liquid mixing plasma + UV process was found to be insignificant.