Research on convective condensation heat transfer for a gas mixture in a vertical tube

2004 ◽  
Vol 33 (4) ◽  
pp. 219-228 ◽  
Author(s):  
Li Jia ◽  
Xiaofeng Peng
Author(s):  
Masahiro Kawakubo ◽  
Hiroshige Kikura ◽  
Masanori Aritomi ◽  
Toshihiro Komeno

2018 ◽  
Vol 10 (04) ◽  
pp. 25-34 ◽  
Author(s):  
Shengjun Zhang ◽  
Xu Cheng ◽  
Feng Shen

2005 ◽  
Vol 2005 (0) ◽  
pp. 39-40
Author(s):  
Koichi HIRATA ◽  
Masahiro KAWAKUBO ◽  
Hiroshige KIKURA ◽  
Masanori ARITOMI ◽  
Toshihiro KOMENO

2013 ◽  
Vol 325-326 ◽  
pp. 346-352
Author(s):  
Jing Lan Dong ◽  
Wei Ping Yan ◽  
Xue Hong He

For the convective condensation heat transfer of flue gas with a few water vapors produced by pressurized oxy-coal combustion in vertical tube, investigation and calculation were carried out by theoretical analyzing method. Heat transfer mathematical model was set up by modified film model and Nusselt's condensation theory. Calculations were performed for condensation heat transfer at different wall temperatures, Reynolds numbers and water vapor fractions. Results show that with the increase of wall temperature, the condensation rate of flue gas, heat flux and condensation film thickness decrease. And with the increase of Reynolds number of the mixture gas, the condensation rate of flue gas and heat flux increase too, while the condensation film thickness decrease. With the decrease of water vapor fraction, the condensation rate of flue gas and heat flux decrease too, while the decrease of condensation film thickness is not obvious.


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