Thermodynamics: An Engineering Approach 8th Edition

Published by McGraw-Hill Education
ISBN 10: 0-07339-817-9
ISBN 13: 978-0-07339-817-4

Chapter 10 - Vapor and Combined Power Cycles - Problems - Page 600: 10-90

Answer

$\eta_{\text {th }}=48.6\%$ $\dot{W}_{\mathrm{net}}=19,428\text{ kJ/s}$ $\dot{m}_{\text {cool }} =194.6\text{ kg/s}$

Work Step by Step

(a) From the steam tables (Tables A-4, A-5, and A-6), $$ \begin{aligned} & h_1=h_{f @ 7.5 \mathrm{kPa}}=168.75 \mathrm{~kJ} / \mathrm{kg} \\ & v_1=v_{f @ 7.5 \mathrm{kPa}}=0.001008 \mathrm{~m}^3 / \mathrm{kg} \\ & T_1=T_{\text {sat } @ 7.5 \mathrm{kPa}}=40.29^{\circ} \mathrm{C} \\ & w_{\mathrm{p}, \text { in }}=v_1\left(P_2-P_1\right) \\ & =\left(0.001008 \mathrm{~m}^3 / \mathrm{kg}\right)(6000-7.5 \mathrm{kPa})\left(\frac{1 \mathrm{~kJ}}{1 \mathrm{kPa} \cdot \mathrm{m}^3}\right) \\ & =6.04 \mathrm{~kJ} / \mathrm{kg} \\ & h_2=h_1+w_{\mathrm{p}, \mathrm{in}}=168.75+6.04=174.79 \mathrm{~kJ} / \mathrm{kg} \\ & h_4=h_{g @ 7.5 \mathrm{kPa}}=2574.0 \mathrm{~kJ} / \mathrm{kg} \\ & s_4=s_{g @ 7.5 \mathrm{kPa}}=8.2501 \mathrm{~kJ} / \mathrm{kg} \\ & \left.\begin{array}{l} P_3=6 \mathrm{MPa} \\ s_3=s_4 \end{array}\right\} \begin{array}{l} h_3=4852.2 \mathrm{~kJ} / \mathrm{kg} \\ T_3=1089.2^{\circ} \mathrm{C} \end{array} \\ & \end{aligned} $$ (b) $$ \begin{aligned} q_{\text {in }} & =h_3-h_2=4852.2-174.79=4677.4 \mathrm{~kJ} / \mathrm{kg} \\ q_{\text {out }} & =h_4-h_1=2574.0-168.75=2405.3 \mathrm{~kJ} / \mathrm{kg} \\ w_{\text {net }} & =q_{\text {in }}-q_{\text {out }}=4677.4-2405.3=2272.1 \mathrm{~kJ} / \mathrm{kg} \end{aligned} $$ and $$ \eta_{\text {th }}=\frac{w_{\text {net }}}{q_{\text {in }}}=\frac{2272.1 \mathrm{~kJ} / \mathrm{kg}}{4677.4 \mathrm{~kJ} / \mathrm{kg}}=48.6 \% $$ Thus, $$ \dot{W}_{\mathrm{net}}=\eta_{\mathrm{th}} \dot{Q}_{\text {in }}=(0.4857)(40,000 \mathrm{~kJ} / \mathrm{s})=19,428 \mathrm{~kJ} / \mathrm{s} $$ (c) The mass flow rate of the cooling water will be minimum when it is heated to the temperature of the steam in the condenser, which is $40.29^{\circ} \mathrm{C}$, $$ \begin{aligned} \dot{Q}_{\text {out }} & =\dot{Q}_{\text {in }}-\dot{W}_{\text {net }}=40,000-19,428=20,572 \mathrm{~kJ} / \mathrm{s} \\ \dot{m}_{\text {cool }} & =\frac{\dot{Q}_{\text {out }}}{c \Delta T}=\frac{20,572 \mathrm{~kJ} / \mathrm{s}}{\left(4.18 \mathrm{~kJ} / \mathrm{kg} \cdot{ }^{\circ} \mathrm{C}\right)\left(40.29-15^{\circ} \mathrm{C}\right)}=194.6 \mathrm{~kg} / \mathrm{s} \end{aligned} $$
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