• International Journal of Air-Conditioning and Refrigeration
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• 제13권4호
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• pp.167-174
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• 2005

The evaporation heat transfer coefficient of $CO_2$ (R-744) in a horizontal tube was investigated experimentally. The experiments were conducted without oil in a closed refrigerant loop which was driven by a magnetic gear pump. The main components of the refrigerant loop are a receiver, a variable-speed pump, a mass flow meter, a pre-heater and evaporator (test section). The test section consists of a smooth horizontal stainless steel tube of 7.75 mm inner diameter. The experiments were conducted at mass flux of 200 to $500kg/m^2s$, saturation temperature of $-5^{\circ}C\;to\;5^{\circ}C$, and heat flux of 10 to $40kW/m^2$. The test results showed the evaporation heat transfer of $CO_2$ has greater effect on nucleate boiling than convective boiling. The evaporation heat transfer coefficient of $CO_2$ is highly dependent on the vapor quality, heat flux and saturation temperature. The evaporation heat transfer coefficient of $CO_2$ is very larger than that of R-22 and R-134a. In comparison with test results and existing correlations, the best fit of the present experimental data is obtained with the correlation of Jung et al. But the existing correlations failed to predict the evaporation heat transfer coefficient of $CO_2$. Therefore, it is necessary to develop reliable and accurate predictions determining the evaporation heat transfer coefficient of $CO_2$ in a horizontal tube.

• 한국터널지하공간학회 논문집
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• 제24권1호
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• pp.39-55
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• 2022

본 연구는 경주 중·저준위 지하 처분환경에서의 사일로 콘크리트의 음향방출(AE) 신호 감쇠계수(α)를 결정하기 위해 신호감쇠 실험을 수행하였다. 활용된 시료들은 경주 중·저준위 처분장 사일로에 사용된 콘크리트 배합비로 제작하였으며 28일간 수중 양생 후 처분환경에 맞도록 온도 및 포화유무에 따라 추가적으로 노출시켰다. 처분조건 별 각 3개씩의 공시체에 대하여 신호전달거리에 따른 AE 신호를 측정한 결과, 초기구간에서는 포화콘크리트의 AE 진폭과 절대에너지가 건조콘크리트의 경우보다 더 높게 나타났지만, α는 포화콘크리트의 경우가 더 높게 산정되었다. 또한, 포화유무와 상관없이 온도가 증가함에 따라 α는 감소하는 경향을 보였다. α는 온도조건보다는 포화유무에 따른 영향이 큰 것으로 분석되었으며, 이는 콘크리트 처분구조물의 감쇠신호 측정 시 포화여부를 고려한 판단이 중요하다는 것을 의미한다. 처분환경에서의 콘크리트 α는 균열이 발생한 위치에서의 실제 AE 특성 파라미터 값을 추정함으로써 경주 중·저준위 처분환경에서 사일로 콘크리트의 건전성을 예측하고 센서의 최적 배치를 결정하는 데 도움이 될 것으로 기대한다.

• 한국자기학회지
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• 제2권3호
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• pp.211-215
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• 1992

The temperature-dependent saturation magnetization curves of amorphous $Fe_{80-x}Co_xB_{20}$ (8 ${\le}$ x ${\le}$ 40, the step of x is 8) alloys were measured using a vibrating sample magnetometer from 77 K up to 1000 K. Curie temperature and the Bloch coefficient were estimated from the saturation magnetization curves. The low temperature dependence of magnetization is in good agreement with Bloch relation, $M_s(T)$=$M_s(O)$ (1-$BT^{3/2}$ - ${\cdots}.$). The spin wave stiffness constant, tne range of the exchange interaction, and the probable atomic spin were calculated from the saturation magnetization values.

• Journal of Advanced Marine Engineering and Technology
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• 제29권3호
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• pp.297-305
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• 2005

The evaporation heat transfer coefficient of $CO_2$ (R-744) in a horizontal tube was investigated experimentally. The experiments were conducted without oil in a closed refrigerant loop which was driven by a magnetic gear pump. The main components of the refrigerant loop are a receiver. a variable-speed pump. a mass flow meter. a pre-heater and evaporator (test section). The test section consists of a smooth. horizontal stainless steel tube of 7.75 mm inner diameter. The experiments were conducted at mass flux of 200 to $500\;kg/m^{2}s$. saturation temperature of $-5^{\circ}C\;to\;5^{\circ}C$. and heat flux of 10 to $40\;kW/m^2$. The test results showed the evaporation heat transfer of $CO_2$ has greatly effect on more nucleate boiling than convective boiling. The evaporation heat transfer coefficients of $CO_2$ are highly dependent on the vapor quality. heat flux and saturation temperature. The evaporation heat transfer coefficient of $CO_2$ is very larger than that of R-22 and R-134a. In making a comparison between test results and existing correlations. the present experimental data are the best fit for the correlation of Jung et al. But it was failed to predict the evaporation heat transfer coefficient of $CO_2$ using by the existing correlation. Therefore. it is necessary to develop reliable and accurate predictions determining the evaporation heat transfer coefficient of $CO_2$ in a horizontal tube.

• KIEE International Transactions on Electrophysics and Applications
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• 제4C권4호
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• pp.185-189
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• 2004

The temporal variation of a secondary electron emission coefficient (${\gamma}$ coefficient) of hydrogenated amorphous silicon (a-Si:H) was investigated in a dc silane plasma. Estimated ${\gamma}$ coefficients have a value of 2.73 ${\times}$ 10$^{-2}$ on the pure aluminum electrode and 1.5 ${\times}$ 10$^{-3}$ after 2 hours deposition of -Si:H thin films on a cathode. It showed an abrupt decrease for about 30 minutes before saturation. The variation of the ${\gamma}$ coefficient was estimated as a function of the thin film thickness, and the film thickness was about 80 nm after 30 minutes deposition time. These results are compared with the results of a computer simulation for ion penetration into a cathode.

• Journal of Power Electronics
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• 제14권6호
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• pp.1243-1253
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• 2014

The phase inductance of a switch reluctance motor (SRM) is significantly nonlinear. With different saturation conditions, the phase inductance shape is clearly changed. This study focuses on the relationship between coefficient and current in an inductance model with ignored harmonics above the order of 3. A position estimation method based on the variable coefficient inductance model is proposed in this paper. A four-quadrant sensorless control system of the SRM drive is constructed based on the relationship between variable coefficient inductance and rotor position. The proposed algorithms are implemented in an experimental SRM test setup. Experimental results show that the proposed method estimates position accurately in operating two/four-quadrants. The entire system also has good static and dynamic performance.

• 한국산학기술학회논문지
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• 제16권5호
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• pp.3006-3013
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• 2015

원관 열교환기보다 납작관 열교환기를 사용하면 전열성능을 한층 향상시킬 수 있다. 납작관 열교환기를 적절히 설계하기 위해서는 관 내측 열전달계수를 알아야 한다. 본 실험에서는 수력직경 1.41mm인 알루미늄 납작관 내 R-410A 대류 비등 열전달계수를 구하였다. 실험범위는 질량유속 $200{\sim}600kg/m^2s$, 열유속 $5{\sim}15kg/m^2$, 포화온도 $5{\sim}15^{\circ}C$이다. 실험 결과 열전달계수는 임계 건도를 기점으로 감소함을 보였다. 임계 건도는 열유속이 증가할수록 감소하고, 질량유속이 감소할수록 감소하였다. 이는 높은 열유속 또는 낮은 질량유속에서 대류의 영향이 작게 되고 따라서 조기에 dryout이 발생되기 때문에 나타나는 현상으로 판단된다. 열전달계수는 질량유속이 증가할수록 증가하였다. 그러나 낮은 건도에서는 질량유속의 영향은 미미하였다. 열전달계수는 포화온도가 증가할수록 증가하였다. 하지만 이런 경향은 열유속이 작아지면 감소하였다. Shah와 Kaew-On et al. 상관식은 본 실험자료를 적절히 예측하였다.

• 한국축산시설환경학회지
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• 제7권3호
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• pp.177-182
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• 2001

본 연구는 가축분뇨의 오염물질의 농도와 영상처리를 통해 얻어 낸 영상정보값과의 상관관계를 구하기 위해 수행하였다. CCD-카메라와 개인용 컴퓨터를 사용하여 축 분뇨의 영상을 받은 후 각 활성 영역에서의 영상정보와 공정시험 법으로 구한 오염물질과의 관계를 회귀분석법을 이용하여 다음과 같은 결론을 얻을 수 있었다. 1. 영상정보 R값은 CDD값과 결정계수가 0.9213으로 가장 높았으며, G값은 BOD값과 결정계수가 0.9019로 가장 높게 나타났으며, B값의 경우 오염물질 농도와의 상관관계는 매우 적은 것을 알 수 있었다. 2. H값은 BOD와의 결정계수($R^2$)가 0.9496으로 매우 높게 나타났다. 이는 BOD추정에 이용가능할 것으로 판단되었다. 3. BOD농도 추종을 위해서 G값,GRAY, H값, S값, 1값 등이 결정계수가 0.8이상을 나타냈으며, 그 중 H값이 가장 높은 결정계수를 나타냈으며, 이러한 정보를 이용하여 농도 추정이 가능할 것으로 판단되었다. 4. COD농도 추정을 위해서 R값, GRAY값, S값이 0.8이상의 결정계수를 나타냈으며, 그 중에서 R값과의 관계가 가장 높게 나타났으며, 이를 이용하여 간접적으로 농도 추정이 가능할 것으로 판단되었다. 5. SS농도와 영상정보값과 결정계수가 모두 0.8이하로 나타났으며, $NH_4$-N와 $NO_3$-N의 농도와 영상정보와의 결정계수는 모두 0.2이하로 매우 낮게 나타났으며, 가시광선영역의 CCD-카메라를 이용한 농도추정은 불가능할 것으로 판단되었다.

• 한국자기학회:학술대회 개요집
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• 한국자기학회 2003년도 somma/kms meeting
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• pp.117-117
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• 2003

• Journal of Mechanical Science and Technology
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• 제18권12호
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• pp.2284-2293
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• 2004

The evaporation heat transfer coefficient h$\_$r/ and frictional pressure drop Δp$\_$f/ of refrigerant R-134a flowing in the oblong shell and plate heat exchanger were investigated experimentally in this study. Four vertical counterflow channels were formed in the oblong shell and plate heat exchanger by four plates of geometry with a corrugated sinusoid shape of a 45 chevron angle. Upflow of refrigerant R-134a boils in two channels receiving heat from downflow of hot water in other channels. The effects of the refrigerant mass flux, average heat flux, refrigerant saturation temperature and vapor quality of R-134a were explored in detail. Similar to the case of a plate heat exchanger, even at a very low Reynolds number, the flow in the oblong shell and plate heat exchanger remains turbulent. The results indicate that the evaporation heat transfer coefficient h$\_$r/ and pressure drop Δp$\_$f/ increase with the vapor quality. A rise in the refrigerant mass flux causes an increase in the h$\_$r/ and Δp$\_$f/. But the effect of the average heat flux does not show significant effect on the h$\_$r/ and Δp$\_$f/. Finally, at a higher saturation temperature, both the h$\_$r/ and Δp$\_$f/ are found to be lower. The empirical correlations are also provided for the measured heat transfer coefficient and pressure drop in terms of the Nusselt number and friction factor.