Thermodynamics: Third World Bacteriological Test

AI Thread Summary
The discussion focuses on a low-cost incubator designed for bacteriological testing in developing nations, which maintains a temperature of 37°C using phase-change materials. The calculations for the required mass of the waxy material to sustain this temperature are explored, with a derived mass of approximately 0.96 kg. The conversation also addresses why the mass of the samples and insulation are not included in the calculations, emphasizing that the samples should be in thermal equilibrium and that the insulation's specific heat is relatively low. Participants confirm the accuracy of the calculations and clarify the reasoning behind the exclusions. The design aims to provide a practical solution for consistent bacteriological testing in areas with unreliable electricity.
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Homework Statement


For bacteriological testing of water supplies and in medical clinics, samples must routinely be incubated for 24 h at 37°C. A standard constant temperature bath with electric heating and thermostatic control is not suitable in developing nations without continuously operating electric power lines. Peace Corps volunteer and MIT engineer Amy Smith invented a low cost, low maintenance incubator to fill the need. The device consists of a foam-insulated box containing several packets of a waxy material that melts at 37°C, interspersed among tubes, dishes, or bottles containing the test samples and growth medium (food for bacteria). Outside the box, the waxy material is first melted by a stove or solar energy collector. Then it is put into the box to keep the test samples warm as it solidifies. The heat of fusion of the phase-change material is 205 kJ/kg. Model the insulation as a panel with surface area 0.490 m2, thickness 4.50 cm, and conductivity 0.0120 W/m·°C. Assume the exterior temperature is 23°C for 12.0 h and 16°C for 12.0 h. (a) What mass of the waxy material is required to conduct the bacteriological test? (b) Why are the mass of the samples and the mass of the insulation not factored into the calculations?

Homework Equations


P = \dfrac{kA \left( T_h - T_c \right)}{L}
Q = L_f \Delta m

The Attempt at a Solution


So I figure that in the 24 hours, the amount of heat (assuming there is enough) that will transfer through the "panel" (escaping from inside the container) will be equal to the rate of heat transfer x time:
Q = \left( \dfrac{kA \left( 37-23^{\circ}C \right) }{L} + \dfrac{kA \left( 37-16 ^{\circ} \right) }{L} \right) \cdot \left( 3600 \dfrac{s}{h} \cdot 12 \right) = L_f \Delta m
And solving for m:
m = \left( 3600 \dfrac{s}{h} \cdot 12 \right) kA \dfrac{74-23-16^{\circ}C}{L \cdot L_f}
Where:
L = .0450 m
Lf = 205 kJ/kg = 2.05e5 J/kg
k = .0120 W/m2
A= .490 m2

I get m = 0.96 kg

There is no solution to this problem in my book and my professor (bless his heart?) posted solutions to an old edition. So... does this look right? Also, I can't figure out a good answer to part (b) other than, if the samples are in thermal equilibrium at the beginning of the 24 hours, as long as the rate of energy is steady state the temperature will not change and the bacteria will be sufficiently warmed.
 
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Bennigan88 said:
Q = \left( \dfrac{kA \left( 37-23^{\circ}C \right) }{L} + \dfrac{kA \left( 37-16 ^{\circ} \right) }{L} \right) \cdot \left( 3600 \dfrac{s}{h} \cdot 24 \right) = L-f \Delta m
I guess that should read LfΔm.
There are two 12 hour periods, but you have a time factor of 24 hours for each rate.
Other than that, looks fine.
I can't find the question for part (b).
 
Ah, I overlooked that. Thank you, and yes it was supposed to be L_f! Part (b) is why the mass of the sample and the mass of the insulation are not factored into the calculations.
 
Bennigan88 said:
Part (b) is why the mass of the sample and the mass of the insulation are not factored into the calculations.
What you answered (in particular, if the samples are already below temperature presumably they're spoilt), plus, the insulation will have relatively low specific heat.
 
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