scholarly journals On the importance of heat and mass transfer coupling during characterization of hygroscopic insulation materials

Author(s):  
Patrick Perre ◽  
Arnaud Challansonnex

The present work is focused on mass transfer characterization of hygroscopic materials used for insulation, such as Low Density Fibreboards. Due to their particular morphology, these panels present a very high mass diffusivity in the connected gaseous phase and a very low thermal conductivity. This combination of properties exacerbates the coupling between heat and mass transfer in transient state. Based on experimental data obtained with an original set-up and relevant simulations performed using a comprehensive physical formulation, a throughout vision of this question is proposed in the present study. In particular, we emphasize on: - The impressive change in core temperature in terms of magnitude and duration, - The great impact of the internal temperature gradient, which slows down mass diffusion, - The dramatic error on mass diffusivity value if the coupling is ignored. Keywords: experiment; identification; modelling; RH at back-face; transient state

2014 ◽  
Vol 989-994 ◽  
pp. 3100-3104
Author(s):  
Rui Hang Zhang ◽  
Zi Ye Wang ◽  
Run Ping Niu

TA mathematical model describing heat and mass transfer performance of packed-type parallel flow dehumidifier was set up. The numerical solution of differential equations was derived. Taking the heat and mass transfer coefficients obtained by experiments as the input parameters of the model, the impact of solution inlet parameters on outlet parameter of air was described. The simulation results indicated that the mathematical model could be used to predict the performance of liquid dehumidification. The results showed that the mathematical model can be of great value in the design and improvement of dehumidifier.


Author(s):  
ByungJun Kim ◽  
SangSeok Yu ◽  
YoungDuk Lee ◽  
KookYoung Ahn

In this paper, a technique of the humidity measurement is developed to identify the performance of membrane humidifier. The technique is designed to measure the performance of membrane humidifier during steady state and transient state. In particular, the measurement technique is very useful to understand dynamic behavior of humidifier because the response of commercial humidity sensor is too slow to capture the transient response of mass and heat transfer through the membrane. Accordingly, the heat and mass transfer characteristics of membrane humidifier are figured out with the experimental analysis. The parameters used in experiment are dry air pressure, humid air temperature and dry air flow rate.


2020 ◽  
Vol 154 ◽  
pp. 309-316
Author(s):  
Rebecca Chamberlain ◽  
Jonas Schlauersbach ◽  
Matthias Erber

Fuel ◽  
2015 ◽  
Vol 145 ◽  
pp. 136-142 ◽  
Author(s):  
Wei Zhou ◽  
Qinghui Wang ◽  
Qingfu Qiu ◽  
Yong Tang ◽  
Jiawei Tu ◽  
...  

2002 ◽  
Vol 53 (2) ◽  
pp. 161-176 ◽  
Author(s):  
Olivier Vitrac ◽  
Dominique Dufour ◽  
Gilles Trystram ◽  
Anne-Lucie Raoult-Wack

TecnoLógicas ◽  
2020 ◽  
Vol 23 (49) ◽  
pp. 53-70
Author(s):  
David Gamboa ◽  
Bernardo Herrera

A heat pipe can be considered a highly effective thermal conduction device, which is especially desirable in heat transfer operations in order to ensure high energy efficiency. However, the operation of heat pipes comprises different heat and mass transfer phenomena, such phase change, heat conduction and convection, solid-liquid and vapor-liquid surface interactions, surface vaporization, and nucleate boiling. Therefore, modelling heat pipes is a highly complex task that demands detailed knowledge of the physical phenomena involved and choosing suitable theoretical models to obtain a good representation of the real nature of the heat and mass transfer processes. In this study, some models and parameters available in the commercial CFD software ANSYS Fluent for turbulence, density, phase change, and phase interfaces were examined to determine their influence on the prediction of the heat and mass transfer in a two-phased closed thermosyphon (TPCT). The numerical results show that using a turbulence viscous model is not necessary and that a variable density model improves the temperature distribution inside the TPCT. Furthermore, using high mass and energy transfer coefficients during condensation makes the vapor remain close to the saturation temperature. Finally, a sharp interphase model is strongly recommended for this type of process.


2009 ◽  
Vol 12 (8) ◽  
pp. 67-80
Author(s):  
Dung Tan Nguyen ◽  
Dung Van Trinh ◽  
Bao Duc Tran

When applied technology Freeze - Drying in preserving foods had economy value, it seems that establishment and solution mathematical model heat and mass transfer at the same time in conditional processing freeze - drying is very important problem. From that point it is basis of science to determine regime technology Freeze - Drying. In this article, we will publish result research to set up and solve mathematical model heat and mass transfer at the same time of cylinder form in conditional freeze - drying. Result research will apply for preserving fishery foods crustacean group (PENAEUS MONODON, PENAEUS MERGUIENSIS, PENAEUS VANNAMEI) has economy value.


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