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Thermal_Power_Plant_2 Prepared by: NMG

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## Thermal_Power_Plant_2 Prepared by: NMG

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**We consider power cycles where the working fluid undergoes a**phase change. The best example of this cycle is the steam power cycle where water (steam) is the working fluid. Carnot Vapor Cycle**The heat engine may be composed of the following components.**The working fluid, steam (water), undergoes a thermodynamic cycle from 1-2-3-4-1. The cycle is shown on the following T-s diagram.**The thermal efficiency of this cycle is given as**• Note the effect of TH and TL on th, Carnot. • The larger the TH the larger the th, Carnot • The smaller the TL the larger the th, Carnot Nimymech\CarnotCycle\shell.swf**To increase the thermal efficiency in any power cycle, we**try to increase the maximum temperature at which heat is added. • Reasons why the Carnot cycle is not used: • Pumping process 1-2 requires the pumping of a mixture of saturated liquid and saturated vapor at state 1 and the delivery of a saturated liquid at state 2. • To superheat the steam to take advantage of a higher temperature, elaborate controls are required to keep TH constant while the steam expands and does work. • To resolve the difficulties associated with the Carnot cycle, the Rankine cycle was devised.**RANKINE CYCLE: THE IDEAL CYCLE**FOR VAPOR POWER CYCLES The simple ideal Rankine cycle.**Energy Analysis of the Ideal Rankine Cycle**Steady-flow energy equation The efficiency of power plants in the U.S. is often expressed in terms of heat rate, which is the amount of heat supplied, in Btu’s, to generate 1 kWh of electricity. The thermal efficiency can be interpreted as the ratio of the area enclosed by the cycle on a T-s diagram to the area under the heat-addition process. nimymech\steamPowerPlant.swf**To increase system efficiency**• Lower condenser pressure Must have at least 10°C DT between condenser and cooling water or air temperature for effective heat transfer Watch quality at exit to prevent turbine problems (shouldn’t go less than about 88%) • Superheat the steam more Tmax ~ 620° due to metallurgical considerations • Increase boiler pressure (with same Tmax) Pmax ~ 30 Mpa 4. Reheat of steam 5. Regeneration**HOW CAN WE INCREASE THE EFFICIENCY OF THE RANKINE CYCLE?**The basic idea behind all the modifications to increase the thermal efficiency of a power cycle is the same: Increase the average temperature at which heat is transferred to the working fluid in the boiler, or decrease the average temperature at which heat is rejected from the working fluid in the condenser. Lowering the Condenser Pressure (Lowers Tlow,avg) To take advantage of the increased efficiencies at low pressures, the condensers of steam power plants usually operate well below the atmospheric pressure. There is a lower limit to this pressure depending on the temperature of the cooling medium Side effect: Lowering the condenser pressure increases the moisture content of the steam at the final stages of the turbine. The effect of lowering the condenser pressure on the ideal Rankine cycle.**Effect of Lowering Condenser Pressure on the Ideal Rankine**cycle**Superheating the Steam to High Temperatures (Increases**Thigh,avg) Both the net work and heat input increase as a result of superheating the steam to a higher temperature. The overall effect is an increase in thermal efficiency since the average temperature at which heat is added increases. Superheating to higher temperatures decreases the moisture content of the steam at the turbine exit, which is desirable. The temperature is limited by metallurgical considerations. Presently the highest steam temperature allowed at the turbine inlet is about 620°C. The effect of superheating the steam to higher temperatures on the ideal Rankine cycle.**Increasing the Boiler Pressure (Increases Thigh,avg)**Today many modern steam power plants operate at supercritical pressures (P > 22.06 MPa) and have thermal efficiencies of about 40% for fossil-fuel plants and 34% for nuclear plants. A supercritical Rankine cycle. For a fixed turbine inlet temperature, the cycle shifts to the left and the moisture content of steam at the turbine exit increases. This side effect can be corrected by reheating the steam. The effect of increasing the boiler pressure on the ideal Rankine cycle.**Effect of Increasing Boiler Pressure on the Ideal Rankine**cycle**Reheat Cycle**• Allows us to increase boiler pressure without problems of low quality at turbine exit**Rankine Cycle with Reheat**Component Process First Law Result Boiler Const. Pqin = (h3 - h2) + (h5 - h4) Turbine Isentropic wout = (h3 - h4) + (h5 - h6) Condenser Const. Pqout = (h6 - h1) Pump Isentropic win = (h2 - h1) = v1(P2 - P1) The thermal efficiency is given by Nimymech\RankineCycleReheating\Source\shell.swf Nimymech\Animation\ReheatCycle.swf**THE IDEAL REHEAT RANKINE CYCLE**How can we take advantage of the increased efficiencies at higher boiler pressures without facing the problem of excessive moisture at the final stages of the turbine? 1. Superheat the steam to very high temperatures. It is limited metallurgically. 2. Expand the steam in the turbine in two stages, and reheat it in between (reheat) The ideal reheat Rankine cycle.**Regeneration**• Preheats steam entering boiler using a feedwater heater, improving efficiency • Also deaerates the fluid and reduces large volume flow rates at turbine exit.**nimymech\openFWH.swf**nimymech\RankineCycleRegeneration\shell.swf**Open Feedwater Heaters**An open(or direct-contact) feedwater heateris basically a mixing chamber, where the steam extracted from the turbine mixes with the feedwater exiting the pump. Ideally, the mixture leaves the heater as a saturated liquid at the heater pressure. The ideal regenerative Rankine cycle with an open feedwater heater.**Simple Rankine Cycle**nimymech\steamPowerPlant.swf Reheat Nimymech\RankineCycleReheating\Source\shell.swf Nimymech\Animation\ReheatCycle.swf Regeneration nimymech\openFWH.swf nimymech\RankineCycleRegeneration\shell.swf