- #1
Ying_Thes
- 9
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Hi all, I am not sure if the is the right place to post the question being new to the forum, but I am looking for some help with a heat transfer experiment that I ran for my honours thesis.
Essentially the aim is to determine if warmed saline fluid bags taped to 3 different types of tree barks will cool at the same rate. We had 4 fluid bags in total all starting at the same temperature, 3 of which were taped to a rough, smooth and paper bark tree respectively and the 4th was hung in the shade and had no contact to any surfaces.
I initially thought that I would just measure the rate of heat loss per area using the following:
Heat loss C/sec/cm2 = {[k * (Ti - Tf)] / As} / t
Where k = Thermal conductivity of tree bark or air
Ti = initial temperature
Tf = final temperature
As = Surface area exposed to either wood or air
t = time
Then I read up more and decided that a time constant formula should be used instead. The problem I have is that I am not sure which formula/equation/law to use and what else I should include to compare between the cooling rates of the 4 bags. After reading multiple journals and texts, there was still no solution to this so I thought of posting it on the forum, the major issue is how do I incorporate both convective cooling by air and conductive cooling by heat loss to the cooler tree trunks into the a thermal time constant formula?
I tried using the Logarithmic Method on this webpage : http://www.facstaff.bucknell.edu/mastascu/eLessonsHTML/SysDyn/SysDyn3TCBasic.htm#Measuring to generate a slope and get an equation for the slope (using the trendline in excel), and for one of the bags it was "y = -0.0156x + 7.4019", which didn't make any sense to me, because time constant would be -0.0156?
I also read up on lumped system analysis but it just made me very confused. Then there was interface boundary conditions where 2 materials of different thermal conductivities are in imperfect thermal contact and share a common boundary which I am not sure what to use that for.
Things to note:
Thanks so much~
Essentially the aim is to determine if warmed saline fluid bags taped to 3 different types of tree barks will cool at the same rate. We had 4 fluid bags in total all starting at the same temperature, 3 of which were taped to a rough, smooth and paper bark tree respectively and the 4th was hung in the shade and had no contact to any surfaces.
I initially thought that I would just measure the rate of heat loss per area using the following:
Heat loss C/sec/cm2 = {[k * (Ti - Tf)] / As} / t
Where k = Thermal conductivity of tree bark or air
Ti = initial temperature
Tf = final temperature
As = Surface area exposed to either wood or air
t = time
Then I read up more and decided that a time constant formula should be used instead. The problem I have is that I am not sure which formula/equation/law to use and what else I should include to compare between the cooling rates of the 4 bags. After reading multiple journals and texts, there was still no solution to this so I thought of posting it on the forum, the major issue is how do I incorporate both convective cooling by air and conductive cooling by heat loss to the cooler tree trunks into the a thermal time constant formula?
I tried using the Logarithmic Method on this webpage : http://www.facstaff.bucknell.edu/mastascu/eLessonsHTML/SysDyn/SysDyn3TCBasic.htm#Measuring to generate a slope and get an equation for the slope (using the trendline in excel), and for one of the bags it was "y = -0.0156x + 7.4019", which didn't make any sense to me, because time constant would be -0.0156?
I also read up on lumped system analysis but it just made me very confused. Then there was interface boundary conditions where 2 materials of different thermal conductivities are in imperfect thermal contact and share a common boundary which I am not sure what to use that for.
Things to note:
- We only measured the surface temperatures of the bags and the tree trunks above and below where the bags were sitting. The data seems to indicate that the two surfaces (bag and tree trunk) never came to equilibrium after 2 hours of data recording.
- The ambient temperature and humidity fluctuates as it was not in an environmentally controlled room, but wind speed was not an issue as there was not much wind around. As all the bags were in shaded areas, I don't think radiation is of much concern.
- Each fluid bag seemed to have a temperature gradient within it, with the top of the bags warmer than the bottom despite us having mixed the fluid withing the bags prior to taping them onto the trees to ensure a uniform temperature throughout.
- All tree trunks were cooler than the saline bags and the ambient temperature was also consistently cooler than the bags.
Thanks so much~