• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2006년도 동계학술발표대회 논문집
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• pp.35-35
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• 2006

• 설비공학논문집
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• 제25권2호
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• pp.101-108
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• 2013

This paper is presented an experimental study of flow boiling heat transfer characteristics of ammonia, and is focused on pressure gradient and heat transfer coefficient of the refrigerant flow inside horizontal small tube with inner diameter of 3.0 mm and length of 2000 mm. The direct heating method is applied for supplying heat to the refrigerant, where the test tube is uniformly heated by electric current. The local heat transfer coefficients were obtained over a heat flux range of 20 to $80kW/m^2$, a mass flux range of 50 to $500kg/m^2s$, a saturation temperature range of 0 to $10^{\circ}C$, and quality up to 1.0. The pressure drops increase with increasing mass flux and heat flux, and with decreasing saturation temperature. The heat transfer coefficients increase with increasing mass flux and saturation temperature in middle and high quality region. And the local heat transfer coefficient increase with increasing heat flux in low quality region. The heat transfer coefficient of the experimental result was compared with six existing heat transfer coefficient correlation. A new boiling heat transfer coefficient correlation based on the superposition model for ammonia in small tubes is developed average deviation of -0.17% and mean deviation of 10.85%.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2008년도 하계학술발표대회 논문집
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• pp.154-159
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• 2008

Two-phase flow boiling heat transfer of R-410A in horizontal small tubes was reported in the present experimental study. The local heat transfer coefficients were obtained over a heat flux range of 5 to 40 kW/$m^2$, a mass flux range of 170 to 600 kg/$m^2s$, a saturation temperature range of 3 to $10^{\circ}C$, and quality up to 1.0. The test section was made of stainless steel tubes with inner diameters of 0.5 and 3.0 mm, and lengths of 330 and 3000 mm, respectively. The section was heated uniformly by applying a direct electric current to the tubes. The effects on heat transfer of mass flux, heat flux, inner tube diameter, and saturation temperature were presented. The experimental heat transfer coefficient is compared with six existing heat transfer coefficient correlations. A new boiling heat transfer coefficient correlation based on the superposition model for R-410A in small tubes was developed with mean deviation of 10.13%.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2008년도 동계학술발표대회 논문집
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• pp.262-268
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• 2008

The present paper dealt with flow heat transfer characteristics of R-410A vaporization in horizontal smooth microchannel. The test sections were made of stainless steel tube with inner diameters of 300 mm and length of 300 mm. The refrigerant was supplied with mass flux range of 260-600 kg/$m^2s$ and applied under operating heat flux range of 5-20 kW/$m^2$ using a direct electric current heating method. The in let saturation temperature was set at $10^{\circ}C$ and vapor quality up to 1.0. The influences of mass flux, heat flux and inner tube diameter on local heat transfer coefficients were presented. Comparison with existing heat transfer coefficient correlations was performed. An improved heat transfer coefficient correlation for refrigerant vaporization in microchannel based on superposition model was developed with a mean deviation of 14.01%.

• 대한기계학회논문집B
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• 제27권2호
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• pp.163-172
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• 2003

Boiling heat transfer coefficients and pressure drops for R-22 and R-407C were measured in horizontal micro-channels. The test section is stainless steel tube, inner tube diameters are 1.8mm and 2.8mm, and the respective lengths are 1500mm and 3000mm. The range of mass flux is 300-600kg/$m^2$s and heat flux is 5-15kW/$m^2$. In this results, pressure drop increased linearly for both R-22 and R-407C with increased mass flux, but the increase of heat flux did not affect the pressure. In addition, the pressure drop was fairly increased in the high quality region rather than low quality region. In the range of low quality, the mass flux had a small affect on the heat transfer coefficients, however, in high quality region, the heat transfer coefficients increased even more with increasing mass flux. Under the low quality region and low mass flux, the heat transfer coefficients increased with increasing heat flux densities. The effects of inner tube diameter were clearly observed. Namely, the measured pressure drop inside inner tube diameter 1.8 mm is higher than 2.8 mm with increasing the mass flux and heat flux. Also, the measured local heat transfer coefficient inside inner tube diameter 1.8 mm is higher than 2.8 mm in the range of high qualities. The experimental data for R-407C compared with proposed correlation using pure refrigerant. The experimental data for R-407C was more decreased than the proposed correlation for pure refrigerant up to 50% or more.

• 설비공학논문집
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• 제21권12호
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• pp.663-670
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• 2009

Two-phase flow boiling heat transfer of R-410A in horizontal small tubes was reported in the present experimental study. The local heat transfer coefficients were obtained over a heat flux range of 5 to 40 kW/$m^2$ a mass flux range of 170 to 600 kg/$m^2s$, a saturation temperature range of 3 to $10^{\circ}C$, and quality up to 1.0. The test section was made of stainless steel tubes with inner diameters of 0.5 and 3.0 mm, and lengths of 330 and 3000 mm, respectively. The test section was heated uniformly by applying a direct electric current to the tubes. The effects on heat transfer of mass flux, heat flux, inner tube diameter, and saturation temperature were presented. The experimental heat transfer coefficients are compared with six existing heat transfer coefficient correlations. A new boiling heat transfer coefficients correlation based on the superposition model for R-410A in small tubes was developed with mean deviation of 10.13%.

• 설비공학논문집
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• 제18권11호
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• pp.906-914
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• 2006

The present paper dealt with an experimental study of boiling heat transfer characteristics of R-290. Pressure gradient and heat transfer coefficient of the refrigerant flow inside horizontal smooth minichannel were obtained with inner tube diameter of 3.0 mm and length of 2,000 mm. The direct electric heating method was applied for supplying a heat to the refrigerant uniformly. The experiments were conducted with R-290 purity of 99.99%, at saturation temperature of 0 to $10^{\circ}C$, a mass flux range of $50{\sim}250kg/m^2s$, and a heat flux range of $5{\sim}20kW/m^2$. The heat transfer coefficients of R-290 increased with increasing mass flux and saturation temperature, wherein the effect of mass flux was higher than that of the saturation temperature. Heat flux has a low effect on the increasing of heat transfer coefficient. The heat transfer coefficient was compared with six existing heat transfer coefficient correlations. The Zhang et al.'s correlation (2004) gave the best prediction of heat transfer coefficient. A new correlation to predict the two-phase flow heat transfer coefficient was developed based on the Chen correlation. The new correlation predicted the experimental data well with a mean deviation of 11.78% and average deviation of -0.07%.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2006년도 하계학술발표대회 논문집
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• pp.68-73
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• 2006

The present paper deals with an experimental study of boiling heat transfer characteristics of R-290, and is focused on pressure gradient and heat transfer coefficient of the refrigerant flow inside horizontal smooth minichannel with inner diameter of 3.0 mm and length of 2000 mm. The direct heating method applied for supplying heat to the refrigerant where the test tube was uniformly heated by electric current which was applied to the tube wall. The experiments were conducted with R-290 with purity of 99.99% at saturation temperature of 0 to $10^{\circ}C$. The range of mass flux is $50{\sim}250kg/m^2s$ and heat flux is $5{\sim}20kW/m^2$. The heat transfer coefficients of R-290 increases with increasing mass flux and saturation temperature, wherein the effect of mass flux is higher than that of the saturation temperature, whereas the heat flux has a low effect on increasing heat transfer coefficient. The significant effect of mass flux on heat transfer coefficient is shown at high quality, the effect of heat flux on heat transfer coefficient at low quality shows a domination of nucleate boiling contribution. The heat transfer coefficient of the experimental result was compared with six existing heat transfer coefficient correlation. Zang et al.'s correlation(2004) gave the best prediction of heat transfer coefficient.

• 대한소아치과학회지
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• 제46권1호
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• pp.76-84
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• 2019

이 연구의 목적은 3종의 수복재료와 3종의 tricalcium-silicate 기반 치수복조제의 미세누출을 평가하고, 이들 치수복조제와 상아질 사이의 전단결합강도를 비교하는 것이다. 수복재료로는 복합레진(CR), 레진강화형 글래스아이오노머 시멘트(RMGI), 그리고 전통적인 글래스아이오노머 시멘트(GIC)를, 치수복조제로는 TheraCal $LC^{(R)}$(TLC), $Biodentine^{(R)}$ (BD), 그리고 $ProRoot^{(R)}$ white MTA (WMTA)을 사용했다. 소의 절치에 5급와동을 형성하여 이를 적용하는 치수복조제와 수복재료에 따라 9개의 그룹으로 분류하고 0.5% fuchsin 용액을 이용한 염색침투법을 시행했다. 각 표본을 절단하고 입체현미경으로 관찰해 미세누출 정도를 평가했다. 아크릴 레진에 소 절치의 임상적 치관을 매몰한 후 수평으로 절단해 준비한 표본을 임의로 3그룹으로 나누었다. 표본의 상아질에 그룹별로 TLC, BD, 그리고 WMTA 블록을 적용한 후 universal testing machine을 이용해 전단결합강도를 측정했다. 미세누출은 TLC + GIC, TLC + RMGI, TLC + CR, 그리고 BD + GIC 그룹에서 가장 적었고, WMTA + RMGI와 WMTA + CR 그룹에서 가장 많았다. 전단결합강도는 WMTA 그룹에서 다른 그룹보다 통계적으로 유의하게 낮은 것으로 나타났다.

• Applied Microscopy
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• 제29권3호
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• pp.383-403
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• 1999

흰쥐 성체 전뇌 기저부의 수직 및 수평 대각 Broca대에서 각 형별 ChAT 면역반응 신경세포의 조직학적 및 미세구조적 특징을 면역조직화학 및 전자현미경을 이용한 면역세포화학적 방법으로 조사하였다. ChAT 면역반응 신경세포에서 광학현미경적 면역반응은 세포체의 세포질과 신경돌기에서 확인되었다. 아울러 미세구조적 관찰로 ChAT 면역반응은 핵외막, 조면소포체의 막, 자유리보좀 그리고 polysomes에서 나타났다. 수직 및 수평 대각 Broca대에서 ChAT 면역반응 신경세포는 세포의 모양과 세포체의 장 단축의 비에 따라 원형, 난형, 세장형, 방추형, 삼각형 그리고 다각형으로 분류되었다. 이 각각의 세포형들을 전자현미경을 이용하여 미세구조적으로 관찰한 결과, 세포체의 크기, 세포질에 대한 핵의 상대적 크기, 세포소기관의 종류 및 분포양상, 신경연접의 수 및 종류 등의 기준에 따라 면역반응 신경세포들은 아유형 I, II로 분류되었다. 그러나, 방추형 및 삼각형 면역반응 신경세포에서는 아유형 I만이 관찰되었다. 아유형 I 면역반응 신경세포는 핵막함입을 보이는 작은 핵과 풍부한 세포질을 포함하였다. 이들 면역반응 세포질은 평행한 긴 수조들로 규칙적인 층판을 이룬 잘 발달된 rER를 함유하였다. 1, 2개의 층판체와 nematosome들이 세포질에서 관찰되었다. 축삭-세포체 신경연접은 주로 대칭형이었으며, 축삭-수상돌기 신경연접은 대다수 비대칭형이었다. 아유형 II 면역반응 신경세포는 비교적 깊은 핵막함입을 보이는 큰 핵과 빈약한 세포질을 포함하였다. rER는 발달이 미약하였다. 축삭-세포체 신경연접은 대칭형과 비대칭형이 같은 비율로 나타났고, 축삭-수상 돌기 신경 연접은 주로 비대칭형이었다. 이상과 같은 미세구조적 관찰에서 ChAT 면역반응 신경세포가 방추형과 삼각형을 제외한 모든 세포형에서 아유형 I, II로 분류되는 것은 투사영역의 원근에 의한 세포 대사활성의 차이에 기인한 것으로 생각된다.