rcise 3.5 A steam plant produces steam at 8 MPa and \( 450^{\circ} \mathrm{C} \) at a rate of \( 5040 \mathrm{~kg} / \mathrm{h} \) by burning fuel at a rate of \( 540 \mathrm{~kg} / \mathrm{h} \). The feedwater enters the economiser at \( 40,3^{\circ} \mathrm{C} \). The fuel has a calorific value of \( 34 \mathrm{MJ} / \mathrm{kg} \). Calculate the: 1.1 rate of heat absorbed by the steam 1.2 rate of heat supplied by the fuel
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To determine the rate of heat absorbed by the steam and the rate of heat supplied by the fuel, we can use the following formulas: 1. **Rate of Heat Absorbed by the Steam**: This can be calculated using the formula: \[ \dot{Q}_{steam} = \dot{m}_{steam} \times h_{steam} \] where \(\dot{m}_{steam} = 5040 \, \text{kg/h}\) converted to kg/s, and \(h_{steam}\) is the specific enthalpy of the steam at 8 MPa and \(450^{\circ}C\). You would typically consult steam tables to find \(h_{steam}\). For instance, if \(h_{steam} \approx 2800 \, \text{kJ/kg}\), \[ \dot{Q}_{steam} = \frac{5040\, \text{kg/h}}{3600\, \text{s/h}} \times 2800\, \text{kJ/kg} = 39.2 \, \text{MJ/s} \, (or \, 39.2\, \text{MW}) \] 2. **Rate of Heat Supplied by the Fuel**: This is calculated as: \[ \dot{Q}_{fuel} = \dot{m}_{fuel} \times CV \] where \(\dot{m}_{fuel} = 540 \, \text{kg/h}\) converted to kg/s and \(CV = 34 \, \text{MJ/kg}\). So, \[ \dot{Q}_{fuel} = \frac{540\, \text{kg/h}}{3600\, \text{s/h}} \times 34\, \text{MJ/kg} \approx 5.1 \, \text{MJ/s} \, (or \, 5.1\, \text{MW}) \] Now you can plug in the proper enthalpy values into the equations based on steam tables for precise results. Remember to convert units where necessary and keep a close eye on your significant figures based on the data given!