Question 12.24: A steam power plant of 110 MW capacity is equipped with rege...
A steam power plant of 110 MW capacity is equipped with regenerative as well as reheat arrangement. The steam is supplied at 80 bar and 55°C of superheat. The steam is extracted at 7 bar for feed heating and remaining steam is reheated to 350°C, and then expanded to 0.4 bar in the L.P. stage.Assume indirect type of feed heaters. Determine :
(i) The ratio of steam bled to steam generated,
(ii) The boiler generating capacity in tonnes of steam/hour, and
(iii) Thermal efficiency of the cycle.
Assume no losses and ideal processes of expansion.
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The schematic arrangement of the plant is shown in Fig. 12.39 (a) and the processes are represented on h-s chart in Fig. 12.39 (b).
Given : Capacity of plant = 110 MW ;
\left.t_1=350^{\circ} C \text { i.e., } t_s \text { at } 80 \text { bar } \simeq 295^{\circ} C +55^{\circ} C =350^{\circ} C \right) p_2=p_3=7 \text { bar } ; t_3=350^{\circ} C ; p_4=0.4\text { bar }• Locate point 1 corresponding to the condition p_1=80 bar and t_1=350^{\circ} C, on the h-s chart.
• Locate point 2 by drawing vertical line through point 1 till it cuts the 7 bar pressure line.
• Locate point 3 as the cross point of 7 bar and 350°C temperature line.
• Locate point 4 by drawing vertical line through the point 3 till it cuts the 0.4 bar pressure line.
From h-s chart, we find :
h_1=2985 kJ/kg ; h_2=2520 kJ/kg ;
h_3=3170 kJ/kg ; h_4=2555 kJ/kg.
Also, from steam tables, we have :
h_{f 2} (at 7 bar) = 697.1 kJ/kg ; h_{f 4} (at 0.4 bar) = 317.7 kJ/kg.
(i) The ratio of steam bled to steam generated :
Consider energy/heat balance of feed heater :
Heat lost by m kg of steam = Heat gained by (1 – m) kg of condensed steam
m\left(h_2-h_{f 2}\right)=(1-m)\left(h_{f 2}-h_{f 4}\right)m(2520 – 697.1) = (1 – m) (697.1 – 317.7)
1822.9 m = (1 – m) × 379.4
∴ m = 0.172 kg
i.e. Amount of steam bled per kg of steam supplied to the turbine =
0.172 kg
∴ \frac{\text { Steam generated }}{\text { Steam bled }}=\frac{1}{0.172}=5.814.
(ii) The boiler generating capacity :
If m_s is the mass of steam supplied to the power plant per second, then the work developed is given by :
m_s\left(h_1-h_2\right)+m_s(1-m)\left(h_3-h_4\right)=110 \times 10^3or, m_s(2985-2520)+m_s(1-0.172)(3170-2555)=110 \times 10^3
or, m_s(465+509.22)=110 \times 10^3
∴ m_s=112.91 kg/s or 406.48 tonnes/hour
(iii) Thermal efficiency of the cycle, \eta_{\text {thermal }} :
\eta_{\text {thermal }}=\frac{\text { Output } / kg \text { of steam }}{\text { Input } / kg \text { of steam }}=\frac{\left(h_1-h_2\right)+(1-m)\left(h_3-h_4\right)}{\left(h_1-h_{f_2}\right)+(1-m)\left(h_3-h_2\right)}= \frac{(2985-2520)+(1-0.172)(3170-2555)}{(2985-697.1)+(1-0.172)(3170-2520)}
= \frac{974.22}{2826.1}=0.3447 or 34.47%.

