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Modern Engineering Thermodynamics

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158 CHAPTER 5: First Law Closed System Applications<br />

EXAMPLE 5.7 (Continued )<br />

The unknowns are, after 5 seconds have passed, (a) T 2 =?and(b)<br />

U 2 − U 1 = ? The system is closed, and the material is the helium gas<br />

in the sphere.<br />

The basic equations here are the closed system energy balance (EB)<br />

T ∞ = 15.0°C<br />

0.100 m diameter<br />

System boundary<br />

1Q 2 − 1 W 2 = U 2 − U 1 + KE 2 − KE 1 + PE 2 − PE 1<br />

Helium<br />

Neglect<br />

and neglecting _ KE and _ PE, the closed system energy rate balance (ERB) is<br />

h = 3.50 W/(m 2 .K)<br />

_Q − _W = _U<br />

The auxiliary equations needed here are<br />

FIGURE 5.7<br />

Example 5.7.<br />

1. The mechanical work mode 1 W 2 = _W = 0 (a rigid hollow sphere).<br />

2. The convective heat transfer mode _Q = −hAðT s − T ∞ Þ (the negative sign is necessary here because the helium loses heat).<br />

3. Assuming the helium to be an ideal gas, the internal energy can be represented as du = c v ðdTÞ and _U = m _u = mc v<br />

_T s :<br />

Putting these results into the energy rate balance equation gives (assuming T ∞ = constant)<br />

or<br />

_T s = dT s<br />

dt<br />

_Q = −hAðT s − T ∞ Þ = _U = mc v<br />

_T s<br />

= dðT s − T ∞ Þ<br />

dt<br />

= − hA<br />

mc v<br />

ðT s − T ∞ Þ<br />

This is a first-order ordinary differential equation with the initial condition T s = T 1 when t = 0. Its solution is<br />

<br />

T s = ðT 1 − T ∞ Þ exp − hAt<br />

<br />

+ T ∞<br />

mc v<br />

where T 2 = T s at t = 5.00 s. The remaining part of the solution is given by the energy balance equation as<br />

The auxiliary equations and calculations are<br />

U 2 − U 1 = mc v ðT 2 − T 1 Þ<br />

h = 3:50: W/ðm 2 ⋅KÞ<br />

T ∞ = 15:0°F<br />

V = π 6 ðDÞ3 = π 6 ð0:100 mÞ3 = 5:24 × 10 − 4 m 3<br />

A = πD 2 = πð0:100 mÞ 2 = 0:0314 m 2 ðthe surface area of a sphereÞ<br />

c v = 3:123 kJ/ðkg⋅KÞ ðfrom Table C:13bÞ<br />

and from the ideal gas equation of state for helium, m = PV/RT, Table C.13b gives R = 2:077 kJ/ðkg⋅KÞ. Then,<br />

and at t = 5.00 s,<br />

m =<br />

ð140: kN/m 2 Þð5:24 × 10 − 4 m 3 Þ<br />

½2:077 kJ/ðkg⋅KÞŠ½ð200: + 273:15ÞKŠ = 7:46 × 10−5 kg<br />

hA ½3:50 W/ðm 2 ⋅KÞŠð0:0314 m 2 Þ<br />

=<br />

mc v ð7:46 × 10 − 5 = 0:472 s−1<br />

kgÞ½3:123 kJ/ðkg⋅KÞŠ<br />

T 2 = ðT 1 − T ∞ Þ expð− hAt/mc v Þ + T ∞<br />

= ½ð200: − 15:0Þ°CŠ exp½ −ð0:472 s − 1 Þð5:00 sÞŠ + 15:0°C<br />

= 32:5°C<br />

Then,<br />

U 2 − U 1 = mc v ðT 2 − T 1 Þ<br />

= ð7:46 × 10 − 5 kgÞ½3:123 kJ/ðkg⋅KÞŠ½ð32:5 − 200:Þ KŠ<br />

= −0:039 kJ

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