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Modern Engineering Thermodynamics

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372 CHAPTER 11: More Thermodynamic Relations<br />

EXAMPLE 11.7 (Continued )<br />

From Table C.13a in Thermodynamic Tables to accompany <strong>Modern</strong> <strong>Engineering</strong> <strong>Thermodynamics</strong>, we find R = 85.78 ft·lbf/(lbm·R) =<br />

0.1102 Btu/(lbm·R). Then, at 212.0°F,<br />

h fg ð212:0°FÞ = ½6289:78 R + ð1,827,997:8R 2 Þ/461:2 ð + 212:0RÞŠ<br />

× ½0:1102 Btu/ ðlbm ⋅ RÞŠ = 992:37 Btu/lbm<br />

Table C.1a gives h fg ð212:0°FÞ = 970:4 Btu/lbm: Thus, the value obtained from Rankine’s equation is in error by only +2.26%.<br />

Exercises<br />

19. Determine p sat from the Rankine equation given in Example 11.7 when T sat =212.0°F and compare it with the value of T sat<br />

given in Table C.1a at 212.0°F. Answer: (p sat ) calc = 14.73 psia, and from Table C.1a, p sat (212.0°F) = 14.696 psia.<br />

20. Using the relations given in Example 11.7, find the value of T sat for water when h fg = 1037 Btu/lbm and compare your<br />

result with the value given in Table C.1a. Answer: (T sat ) calc = 124.6°F, and from Table C.1a, T sat = 100.0°F.<br />

21. Determine h fg in Example 11.7 if the temperature is increased from 212.0°F to 500.0°F and compare your result with the<br />

value given in Table C.1a. Answer: (h fg ) calc = 902.7 Btu/lbm, and from Table C.1a, h fg (500.0°F) = 714.8 Btu/lbm.<br />

11.6 DETERMINING u, h, AND s FROM p, v, AND T<br />

We are now ready to combine the previous results to produce u, h, ands relations from p, v, andT data. For a<br />

simple substance, any two independent intensive properties fix its thermodynamic state. Consider the specific<br />

internal energy described by a function of temperature and specific volume. We can write this as u = u(T, v).<br />

Differentiating this function, we get<br />

From Eq. (11.1), we can write<br />

<br />

du =<br />

∂u<br />

∂T<br />

<br />

∂u<br />

∂v T<br />

and using the Maxwell Eq. (11.15), this becomes<br />

<br />

∂u<br />

∂v T<br />

<br />

dT +<br />

v<br />

∂u<br />

∂v<br />

<br />

dv<br />

T<br />

<br />

= T ∂s <br />

− p<br />

∂v T<br />

<br />

= T ∂p <br />

− p<br />

∂T<br />

v<br />

In Chapter 3, we introduce the constant volume specific heat c v as<br />

<br />

c v =<br />

∂u <br />

∂T v<br />

(3.15)<br />

and our equation for the total differential du then becomes<br />

<br />

du = c v dT + T<br />

∂p <br />

− p dv (11.19)<br />

∂T<br />

v<br />

Therefore, the change in specific internal energy for any simple substance can be determined by integrating<br />

Eq. (11.19):<br />

Z T2<br />

Z v2<br />

<br />

u 2 − u 1 = c v dT + T ∂p <br />

− p dv (11.20)<br />

T 1 v 1<br />

∂T<br />

Here, we achieved what we set out to do. Equation (11.20) has u cast completely in terms of the measurable<br />

quantities p, v, T, and c v .<br />

Similarly, we can consider the specific enthalpy to be given by a continuous function of temperature and pressure,<br />

h = h(T, p). Then, its total differential is<br />

<br />

dh =<br />

∂h <br />

dT +<br />

∂h<br />

<br />

dp<br />

∂T p ∂p<br />

T<br />

In Chapter 3, we introduce the constant pressure specific heat c p as<br />

<br />

c p =<br />

∂h <br />

(3.19)<br />

∂T p<br />

v

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