• 설비공학논문집
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• 제21권3호
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• pp.167-175
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• 2009

In this study, condensation heat transfer coefficients(HTCs) of R22, R123, R134a and R245fa are measured on both 26fpi low fin and Turbo-C tubes. All data are taken at the vapor temperature of $39^{\circ}C$ with a wall subcooling of $3{\sim}8^{\circ}C$. Test results show that HTCs of the newly developed low vapor pressure alternative refrigerant, R245fa, are $7.8{\sim}9.2%$ and $10.3{\sim}18.6%$ higher than those of R123 for 26fpi low fin tube and Turbo-C tube respectively. For all refrigerants tested, HTCs of Turbo-C enhanced tube are higher than those of 26fpi low fin tube. For the low fin tube, Beatty and Katz's prediction equation yielded 20% deviation for all fluids. The heat transfer enhancement ratio of R245fa on the Turbo-C tube is $5.9{\sim}6.4$ while that of R123 is $5.7{\sim}5.9$. From the view point of environmental safety and condensation heat transfer, R245fa is a long term candidate to replace R123 currently used in centrifugal chillers.

• 대한기계학회논문집B
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• 제39권7호
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• pp.591-598
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• 2015

본 연구에서는 핀 핏치와 핀 높이가 다른 7종류의 낮은 핀관에 대하여 LiBr 농도 0%.~50%, 열유속 $20kW/m^2{\sim}40kW/m^2$, 포화압력 7.38kPa~101.3kPa에서 풀 비등 실험을 수행하였다. 실험 범위에서 최적 낮은 핀관 형상은 핀 핏치 26fpi, 핀 높이 1.8mm로 나타났다. 핀 핏치가 너무 넓으면 전열 면적이 감소하고 핀 핏치가 너무 좁으면 기포의 성장 및 이탈이 원활하지 못하게 되어 최적 핀 핏치가 존재한다. 포화압력이 낮아질수록, LiBr 농도가 증가할수록 열전달계수는 감소하였다. 이는 포화압력이 낮아질수록 기포의 이탈직경은 증가하고 이탈 빈도는 감소하기 때문이다. 또한 LiBr 농도가 증가하면 포화온도는 증가하고 물질확산율은 감소하는데 이에 따라 기포의 성장속도가 감소하고 따라서 열전달계수가 감소하게 된다. 낮은 핀관의 열전달계수는 모든 포화압력과 농도에서 평활관의 열전달계수보다 크게 나타났다. 본 실험자료를 기반으로 상관식을 제시하였다.

• 설비공학논문집
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• 제23권3호
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• pp.208-215
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• 2011

In this work, pool boiling heat transfer coefficients(HTCs) of R22, R123, R134a, and R245fa are measured on both horizontal plain and 26 fpi low fin tubes. The pool boiling temperature is maintained at $7^{\circ}C$ and heat flux is varied from 80 $kW/m^2$ to 10 $kW/m^2$ with an interval of 10 $kW/m^2$. Wall temperatures are measured directly by thermocouples inserted through holes of 0.5 mm diameter. Test results show that HTCs of high vapor pressure refrigerants are usually higher than those of low pressure fluids in both plain and low fin tubes. On a plain tube, HTCs of R245fa are 23.3% higher than those of R123 while on a 26 fpi low fin tube, HTCs of R245fa are 46.3% higher than those of R123. The fin effect is more prominent with low vapor pressure refrigerants than with high vapor pressure ones due to a sweeping effect.

• 설비공학논문집
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• 제13권8호
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• pp.710-719
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• 2001

Pool boiling heat transfer coefficients (HTCs) of HCFC123, HFC134a, HCFC22, HFC407C, HFC410A and HFC32 wre measured on a horizontal smooth tube, 26 fpi low fin tube, Turbo-B and Thermoexcel-E enhanced tubes. AN experimental apparatus was designed such that all tubes heated by cartridge heaters could be installed at the same time to save the refrigerant. Data were taken in the pool of $7^{\circ}C$ with the heat flux decreasing from 80 kW/$m^2\;to\;5kW/m^2$. Test results showed that HTCs of pure refrigerants and those of a azeotrope were greatly influenced by reduced pressure. HTCs of HFC407C were 21~25% lower than those of HCFC22 due to mass transfer resistance. For all refrigerants, enhanced tubes with sub-surface and sub-tunnels showed the largest heat transfer enhancement. Especially the largest heat enhancement was obtained for HCFC123 whose reduced pressure is the lowest among al the refrigerants tested. This indicates that either Turbo-B or Thermoexcel-E enhanced tube would be the best choice when used with a low vapor pressure refrigerant.