• The Korean Journal of Physiology and Pharmacology
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• 제7권6호
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• pp.357-362
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• 2003

Carbon monoxide (CO) is low molecular weight oxide gas that is endogenously produced under physiological conditions and interacts with another gas, nitric oxide (NO), to act as a gastrointestinal messenger. The aim of this study was to determine the effects of exogenous CO on L-type calcium channel currents of human jejunal circular smooth muscle cells. Cells were voltage clamped with 10 mM barium ($Ba^{2+}$) as the charge carrier, and CO was directly applied into the bath to avoid perfusion induced effects on the recorded currents. 0.2% CO was increased barium current ($I_{Ba}$) by $15{\pm}2$% ($mean{\pm}S.E.$, p<0.01, n=11) in the cells. To determine if the effects of CO on barium current were mediated through the cGMP pathway, cells were pretreated with 1-H-[1,2,4]oxadiazolo[4,3,-a]quinoxalin-1-one (ODQ, $10{mu}M$), a soluble guanylyl cyclase inhibitor, and exogenous CO (0.2%) had no effect on barium currents in the presence of ODQ ($2{\pm}1$% increase, n=6, p>0.05). CO mediates inhibitory neurotransmission through the nitric oxide pathway. Therefore, to determine if the effects of CO on L-calcium channels were also mediated through NO, cells were incubated with $N^G-nitro-L-arginine$ (L-NNA, 1 mM), a nitric oxide synthase inhibitor. After L-NNA pretreatment, 0.2 % CO did not increase barium current ($4{\pm}2$% increase, n=6, p>0.05). NO donor, SNAP ($20{\mu}M$) increased barium current by $13{\pm}2$% (n=6, p<0.05) in human jejunal smooth muscle cells. These data suggest that CO activates L-type calcium channels through NO/cGMP dependant mechanism.

• 한국가구학회지
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• 제14권1호
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• pp.1-9
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• 2003

This research was carried out for packing materials and building materials to examine thylene gas adsorption and effect of keeping fruit fresh of wet formed charcoal-fiber mposite made from defibrated fiber of Pinus densiflora Sieb. et Zucc. and white charcoal from uercus variabilis Bl.(wood fiber: charcoal=8:2, 6:4, 4:6, 2:8), with/without phenol formaldehyde resin(PF, Non volatile content:$52\%$, resin content $1,3,5\%$). The results are summarized as follows: 1. The higher the charcoal content, the more the ethylene gas adsorption. At the same mixing ratio of fiber to charcoal, $\#100-200$ of charcoal particle size gave the better reslts than $\#60-100$. 2. Adding PF into the charcoal fiber composite decreased the capacity of ethylene gas adsorption but there was no significant difference until $5\%$ adding amount of PF. 3. For keeping fruit fresh for a long time, Charcoal fiber composite was $66\%$ longer than control. The higher the white charcoal content, the longer fresh time.

• The Korean Journal of Physiology
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• 제6권1호
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• pp.1-9
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• 1972

In order to observe a possible effect of CO intoxication on the activities of surfactant, the rabbit war exposed either to 0.1, 0.2 and 0.4% CO gas for two to six hours or 0. 1% CO gas for two hours daily for 1, 3 and 5 days, and the lung extract was prepared. The tension-area diagram of the lung extract was recorded automatically using the modified Langmuir-wilhelmy balance with a synchronized recording system, and the results were compared with control (i. e. : non-CO gas exposed normal rabbits). The results obtained are summarized as follows: 1. The maximal and minimal surface tensions, width of the tension-area diagram at the surface area of 40% in lung extract, and stability index of the normal rabbit lung extracts were $31.6{\pm}3.11\;dynes/cm,\;8.2{\pm}0.56\;dynes/cm,\;21.4{\pm}4.40dynes/cm\;and\;1.12{\pm}0.22$, respectively. 2. The activities of surfactant in the CO gas exposed group did not show any significant change from the control. 3. The above results suggest that CO gas produced no noticeable effect on the surfactant system of the lung.

• 한국수소및신에너지학회논문집
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• 제33권4호
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• pp.383-390
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• 2022

Appropriate explosion proof electrical equipment should be installed in hazardous areas. In areas where hydrogen is handled, explosion proof electrical equipment adjacent to the hydrogen handing facility must be reviewed for selection of gas group IIC (or IIB+H₂) equipment. When selecting explosion proof electrical equipment for the flammable substance handling facility in areas where hydrogen and flammable substance are handled, the method to avoid gas group IIC (or IIB+H₂) equipment has been suggested by using the operating pressure of the hydrogen handling facility. When the operating pressure of the outdoor hydrogen handling facility is 1.065 MPa or less, it has been confirmed that there is no need to install gas group IIC (or IIB+H₂) equipment for the flammable substance handling facility adjacent to the hydrogen handling facility. And the method of selecting explosion proof electrical equipment for the flammable substance handling facility has been suggested as a flowchart, so it will be able to be utilized when selecting appropriate explosion proof electrical equipment.

• 한국연소학회:학술대회논문집
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• 대한연소학회 2003년도 제27회 KOSCO SYMPOSIUM 논문집
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• pp.89-94
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• 2003

For the development of high efficiency and low emission combustion systems, high temperature air combustion technology has been tested by utilizing preheated air over 1100 K and exhaust gas recirculation. In this system, combustion air is diluted with large amount of exhaust gases ($N_2$, $CO_2$), such that the oxygen concentration is relatively low in the reaction zone, leading to low flame temperature. Since, the temperature fluctuations and sound emissions form the flame are small and flame luminosity is low, the combustion mode is expected to be flameless or mild combustion. Experiment was performed to investigate the turbulent flame structure and $NO_X$ emission characteristics in the high temperature air combustion focused on coflowing jet diffusion flames which has a fundamental structure of many practical combustion systems. The effect of turbulence has also been evaluated by installing perforated plate in the oxidizer inlet nozzle. LPG was used as a fuel. Results showed that even though $NO_X$ emission is sensitive to the combustion air temperature, the present high temperature air combustion system produce low $NO_X$ emission because it is operated in low oxygen concentration condition in excess of dilution.

• 한국가금학회지
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• 제28권1호
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• pp.49-54
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• 2001

Two experiments were conducted to investigate the influence of dietary supplemental Enviro on noxious gas of environmental controlled poultry house and performance of broiler chicks. Diets contained 21.5, 19.00 CP and 3,100, 3,200 kcal/kg ME, respectively for starting and finishing period. Enviro were supplemented with 0, 0.2, 0.4, 0.6 and 0, 0.1, 0.2, 0.3% in Expt. 1 and 2, respectively. $CO_{2}$ and ammonia gas were periodically detected for finsihing period in Expt. 1. Weight gain, feed intake and feed conversion(FC) were measured for five weeks in Expt. 2. ND antibody titer were also measured after primary and booster vaccination at two and three weeks old. Blood cholesterol and nutrients digestibility were In Expt. 1, ammonia and $CO_{2}$ gas of chicks fed 0.2% Enviro showed 32.8ppm and 1,719ppm in poultry house and significantly decrease compared to that of control(P〈0.05). $CO_{2}$ gas was 1,814ppm in 0.4% Enviro treatments and also significantly lower than control(P〈0.05), but tended to be increased compared to that of 0.2% Enviro treatments, In Expt. 2, weight gain of chicks fed 0.1 and 0.2% Enviro was significantly increased for starting period(P〈0.05), but was not statistically different for finishing period. Feed intake was no significantly different of all treatments. Chicks showed lower FC in 0.3% Enviro treatment for starting period(P〈0.05) than others, but was not for finishing period. ND AB titer of chicks fed Enviro was prone to be higher than control, but was not significantly different. Total blood cholesterol was not significantly different of all treatments, but tended to be high in 0.1 and 0.2% Enviro treatments. HDL of chicks fed those levels showed significantly higher than control(P〈0.05), whereas LDL was tended to be decreased in those treatments. The digestibilites of crude protein and fiber were improved in 0.1 and 0.2% Enviro treatments relative to those of control, but was not statistically different. However, crude ash digestibility was significantly improved in 0.1 and 0.2% Enviro treatments(P〈0.05). Chicks also showed AMEn in 0.1, 0.2% Enviro treatments, but was no significance. The results of these experiments indicated that 0.1% Enviro supplement would be maximize the performance of broiler chicks.

• 한국진공학회지
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• 제7권2호
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• pp.82-87
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• 1998

$O_2$기체에 $NH_3/O_2$기체를 첨가하여 실리콘 표면에 산화막을 형성하는 $NH_3/O_2$산화법 에 의한 산화공정시 반응석영관 외부에 방출하는 기체는 $N_2,O_2$및 $H_2O$이며 극소량의 $CO_2$, NO 및 $NO_2$가 검출되었다. 두 종류의 산화제($O_2$ 및 $H_2O$)가 산화에 기여하며 성장률은 $NH_3$및 $O_2$ 의 부분압과 온도에 의해 결정되며, 그 기울기는 건식 및 습식 산화법의 중간에 평행 하게 위치함을 확인하였다. Auger Electron Spectroscopy(AES) 측정결과 $NH_3/O_2$ 산화막은 정확한 $SiO_2$의 화학량론을 가지며 $SiO_2/Si$계면에 발생하는 결합을 억제하며 고정전하의 발 생을 최소화함을 알 수 있었다. $NH_3/O_2$ 산화막(470$\AA$)의 항복전압을 57.5Volt이며, C-V특성 곡선을 축정한 결과 플랫밴드 전압은 0.29Volt이며 곡선의 형태는 이상곡선과 일치하였다.

• 한국환경과학회지
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• 제21권1호
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• pp.113-123
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• 2012

A unit emission reduction of nitrous oxide ($N_2O$) from anthropogenic sources is equivalent to a 310-unit $CO_2$ emission reduction because the $N_2O$ has the global warming potential (GWP) of 310. This greatly promoted very active development and commercialization of catalysts to control $N_2O$ emissions from large-scale stationary sources, representatively nitric acid production plants, and numerous catalytic systems have been proposed for the $N_2O$ reduction to date and here designated to Options A to C with respect to in-duct-application scenarios. Whether or not these Options are suitable for $N_2O$ emissions control in nitric acid industries is primarily determined by positions of them being operated in nitric acid plants, which is mainly due to the difference in gas temperatures, compositions and pressures. The Option A being installed in the $NH_3$ oxidation reactor requires catalysts that have very strong thermal stability and high selectivity, while the Option B technologies are operated between the $NO_2$ absorption column and the gas expander and catalysts with medium thermal stability, good water tolerance and strong hydrothermal stability are applicable for this option. Catalysts for the Option C, that is positioned after the gas expander thereby having the lowest gas temperatures and pressure, should possess high de$N_2O$ performance and excellent water tolerance under such conditions. Consequently, each de$N_2O$ technology has different opportunities in nitric acid production plants and the best solution needs to be chosen considering the process requirements.

• 센서학회지
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• 제20권5호
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• pp.317-321
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• 2011

A Micro platform for micro gas sensor consisted of micro heater, insulator, and sensing electrode on 2 ${\mu}m$ thick $SiN_x$ membrane. Three types of micro platforms were designed and fabricated with membrane sizes. Total size of micro platform was 2.6 mm by 2.6 mm. Measured power consumptions were 28 mW, 28 mW, and 32.5 mW for Type 1, Type 2, and Type 3. At this moment, temperatures of membranes on the platforms were $295^{\circ}C$, $297^{\circ}C$, and $296^{\circ}C$, respectively. Fabricated micro platform considered appropriate to apply for low power consumption micro gas sensor. Micro gas sensors were prepared by the sequence that $SnO_2$ nanopowder pastes were dropped on membrane of Type 1 platforms, dried in oven, heat-treated with micro heaters in platforms. One of the micro gas sensors was tested for gas response to 1157 ppm, 578 ppm, and 231 ppm of methane and 1.68 ppm, 0.84 ppm, and 0.42 ppm of $NO_2$.

• 센서학회지
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• 제24권1호
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• pp.29-34
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• 2015

This study aimed to evaluate the characterization of a metal oxide semiconductor and electrochemical gas sensor array for measuring wastewater odor. The sensitivity of all gas sensors observed in sampling method by stripping was 6.7 to 20.6 times higher than that by no stripping, except sensor D (electrochemical gas sensor). The average reduction ratio of sensor signal as a function of initial dilution rate of wastewater was in the order of food plant > food waste reutilization facility > plating plant. The sensitivity of gas sensors was dependent on both the type of wastewater and the dilution rate. The sensor signals observed by the gas sensor array were correlated with the dilution factor (OU) calculated by the air dilution sensory test with several wastewater ($r^2=0.920{\sim}0.997$), except the sensor signals of sensor D measured in the plating plant wastewater. It seems likely that the gas sensor array plays a role in the evaluation of odor in wastewater and is useful tool for on-site odor monitoring in the wastewater facilities.