
Boil, Expand, Condense, Repeat: The Rankine Cycle in Action Part 1 and Part 2

\(a\)
\(b\)
\(c\)
\(d\)


\(a\)
\(b\)
\(c\)
\(d\)
\[\eta=1-\frac{T_\mathrm{cold}}{T_\mathrm{hot}}=1-\frac{373.15}{473.15}=0.2113\]
\[-W_\mathrm{net}=410.0\ \mathrm{kJ/kg}\]
\[Q_\mathrm{hot}=1939.8\ \mathrm{kJ/kg}\]
\[Q_\mathrm{cold}=-1529.8\ \mathrm{kJ/kg}\]
What are the engineering problems with the Steam Carnot cycle?



The process from b to c is now
isobaric instead of isothermal.
Pump from a
to b now only
compresses
liquid.
\(\Delta H_\mathrm{pump}=W_{s}=V\Delta P\)
A steam power plant operates with steam entering the turbine at 80 bar and 500\(^{\circ}\)C. The condenser operates at 44\(^{\circ}\)C.
Data needed from the steam tables:
@ 44\(^{\circ}\)C and 0.091118 bar: \(\hat{H}_{l}\), \(\hat{H}_{v}\), \(\hat{S}_{l}\), \(\hat{S}_{v}\), \(\hat{V}_{l}\)
@ 500\(^{\circ}\)C and 80 bar: \(\hat{H},\hat{S}\)
At 44\(^{\circ}\)C and 0.091118 bar
\(\hat{V_{l}}=0.0010095\mathrm{\frac{m^{3}}{kg}}\) \(\quad\) \(\hat{H}_{l}=184.26\mathrm{\frac{kJ}{kg}}\) \(\quad\) \(\hat{H}_{v}=2580.7\mathrm{\frac{kJ}{kg}}\)
\(\hspace{20cm}\) \(\hat{S}_{l}=0.62547\mathrm{\frac{kJ}{kg~K}}\) \(\quad\) \(\hat{S}_{v}=8.1816\mathrm{\frac{kJ}{kg~K}}\)
At 500\(^{\circ}\)C and 80 bar
\(\hat{H}=3399.4\mathrm{\frac{kJ}{kg}}\)
\(\hat{S}=6.7264\mathrm{\frac{kJ}{kg~K}}\)
\[\frac{\dot{W_{s}}}{\dot{m}}=\Delta\hat{H}=\hat{V}\Delta P\]
\[=0.0010095\mathrm{\frac{m^{3}}{kg}}(8000\mathrm{~kPa}-9.1118\mathrm{~kPa})=8.067\mathrm{\frac{kJ}{kg}}\]
\[\hat{H}_\mathbf{b}=\hat{H}_\mathbf{a}+\Delta\hat{H}=184.26\mathrm{\frac{kJ}{kg}}+8.067\mathrm{\frac{kJ}{kg}}=192.3\mathrm{\frac{kJ}{kg}}\]
\[\Delta\hat{H}=\frac{\dot{Q}}{\dot{m}}=\hat{H}_\mathbf{c}-\hat{H}_\mathbf{b}=3399.4\mathrm{\frac{kJ}{kg}}-192.3\mathrm{\frac{kJ}{kg}}=3207.1\mathrm{\frac{kJ}{kg}}\]
\[\frac{\dot{W_{s}}}{\dot{m}}=\Delta\hat{H}\]
\[\Delta\hat{S}=0\Rightarrow\hat{S}_\mathbf{c}=\hat{S}_\mathbf{d}\]
\[6.7264=x(8.1816)+(1-x)(0.62547) \quad x=\frac{6.10093}{7.5561}=0.8074\]
\[\hat{H}_\mathbf{d}=x\hat{H}_{v}+(1-x)\hat{H}_{l}\]
\[=0.8074(2580.7\mathrm{\frac{kJ}{kg}})+(1-0.8074)(184.26\mathrm{\frac{kJ}{kg}})=2119.2\mathrm{\frac{kJ}{kg}}\]
\[\Delta\hat{H}=2119.2\mathrm{\frac{kJ}{kg}}-3399.4\mathrm{\frac{kJ}{kg}}=-1280.2\mathrm{\frac{kJ}{kg}}\]
\[\eta=\frac{-W_\mathrm{net}}{Q_\mathrm{hot}}=\frac{1280.2\mathrm{\frac{kJ}{kg}}-8.067\mathrm{\frac{kJ}{kg}}}{3207.1\mathrm{\frac{kJ}{kg}}}=0.3967=39.7\%\]
\[-\dot{W}_\mathrm{net}=80,000\mathrm{\frac{kJ}{s}}=-\dot{m}W_\mathrm{net}\]
\[\dot{m}=\frac{-\dot{W}_\mathrm{net}}{-W_\mathrm{net}}=\frac{80,000\mathrm{\frac{kJ}{s}}}{1280.2\mathrm{\frac{kJ}{kg}}-8.067\mathrm{\frac{kJ}{kg}}}=62.88\mathrm{\frac{kg}{s}}\]
Thanks for watching!
The previous video in the series is in the link in the upper left. The next video in the series is in the upper right. To learn more about Chemical and Thermal Processes, visit the website linked in the description.
The DOFPro Team
