52
Vapor and Combined Power Cycles TOPICS Vapor Power Cycles Rankine Power Cycle modifications to increase efficiency Reheat and Regenerative cycles Combined cycles Binary cycles

Vapor Power Cycles

Embed Size (px)

Citation preview

Page 1: Vapor Power Cycles

Vapor and Combined Power Cycles

TOPICSVapor Power CyclesRankine Power Cycle modifications to increase efficiencyReheat and Regenerative cyclesCombined cyclesBinary cycles

Page 2: Vapor Power Cycles

STEAM ENGINE

Page 3: Vapor Power Cycles

The Carnot Vapor Cycle

Impracticability: ??!!!Impracticability: ??!!

Max temp Tcr2-phase devices

(Is it possible ???!!!)

Page 4: Vapor Power Cycles

4

Page 5: Vapor Power Cycles

5

Page 6: Vapor Power Cycles

6

Page 7: Vapor Power Cycles
Page 8: Vapor Power Cycles

The General James M Gavin Steam Power Plant ,Ohiofull capacity: 2,600,000kW

Page 9: Vapor Power Cycles

9

BOILERTURBINE

PUMP

CONDENSER

q in

w out

qout

w in

1

3

42

We’ll simplify the power plant

Page 10: Vapor Power Cycles

Rankine - the ideal cycle for Vapor Power Cycles

Page 11: Vapor Power Cycles

Example 10-1

Page 12: Vapor Power Cycles

Deviations of actual from ideal

Page 13: Vapor Power Cycles

Example 10-2 Actual cycle

Page 14: Vapor Power Cycles

Increasing the Efficiency: lowering cond. pr

Page 15: Vapor Power Cycles

Increasing the Efficiency: superheating the steam

Page 16: Vapor Power Cycles

Increasing the Efficiency: increasing boiler pr.

Page 17: Vapor Power Cycles

A supercritical Rankine cycle

Page 18: Vapor Power Cycles

Example 10-1

Page 19: Vapor Power Cycles

Example 10-3 Effect of Boiler pr, temp on efficiency

Page 20: Vapor Power Cycles

Ideal Reheat Rankine Cycle

Page 21: Vapor Power Cycles

Example 10-4

Page 22: Vapor Power Cycles
Page 23: Vapor Power Cycles

Regenerative Rankine Cycle: with Open FWH

Page 24: Vapor Power Cycles

Examples of closed feedwater heaters

Page 25: Vapor Power Cycles

Regenerative Rankine Cycle: with Closed FWH with a pump

Page 26: Vapor Power Cycles

Closed feedwater heater with TRAP

Page 27: Vapor Power Cycles
Page 28: Vapor Power Cycles
Page 29: Vapor Power Cycles

The General James M Gavin Steam Power Plant ,Ohiofull capacity: 2,600,000kW

Page 30: Vapor Power Cycles

Gavin power plant schematic

Page 31: Vapor Power Cycles

six turbines on two separate parallel shafts,

feedwater pump is driven by a separate 65,000HP turbine (FPT)

The system has four low pressure closed feedwater heaters, one open feedwater heater / de-aerator, and three high pressure closed feedwater heaters.

Page 32: Vapor Power Cycles

• Consider a steam power plant operating on the ideal regenerative Rankine cycle with one open feedwater heater. Steam enters the turbine at 15 Mpa and 600°C and is condensed in the condenser at a pressure of 10 kPa. Some steam leaves the turbine at a pressure of 1.2 MPa and enters the open feedwater heater. Determine the fraction of steam extracted from the turbine and the thermal efficiency of the cycle.

Page 33: Vapor Power Cycles

Example 10-5

Page 34: Vapor Power Cycles

Example 10-6

Page 35: Vapor Power Cycles

Problem 10-42

Page 36: Vapor Power Cycles

Problem 10-53

Page 37: Vapor Power Cycles

Problem 10-61E

Page 38: Vapor Power Cycles

Problem 10-62

Page 39: Vapor Power Cycles
Page 40: Vapor Power Cycles

Problem 10-78

Page 41: Vapor Power Cycles

Problem 10-81

Page 42: Vapor Power Cycles

Problem 10-91

Page 43: Vapor Power Cycles

Problem 10-28

Page 44: Vapor Power Cycles

Problem 10-29

Page 45: Vapor Power Cycles

Problem 10-30

Page 46: Vapor Power Cycles

1.A high critical temperature and a safe maximum pressure. A critical temperature above the metallurgically allowed maximum temperature (about 620°C) makes it possible to transfer a considerable portion of the heat isothermally at the maximum temperature as the fluid changes phase. This makes the cycle approach the Carnot cycle.

2.Very high pressures at the maximum temperature are undesirable because they create material-strength problems

3.A condenser pressure that is not too low. Condensers usually operate below atmospheric pressure. Pressures well below the atmospheric pressure create air-leakage problems. Therefore, a substance whose saturation pressure at the ambient temperature is too low is not a good candidate.

Desirable properties of working fluid

Page 47: Vapor Power Cycles

5. A high enthalpy of vaporization (hfg) so that heat transfer to the working fluid is nearly isothermal and large mass flow rates are not needed.

6. Low triple-point temperature. A triple-point temperature below the temperature of the cooling medium prevents any solidification problems.

7. A saturation dome that resembles an inverted U. This eliminates the formation of excessive moisture in the turbine and the need for reheating.

8. Good heat transfer characteristics (high thermal conductivity).

9. Other properties such as being inert, inexpensive, readily available, and nontoxic.

Page 48: Vapor Power Cycles

Well, we cannot change the way water behaves during the high-temperature part of the cycle, but we certainly can replace it with a more suitable fluid.

The result is a power cycle that is actually a combination of two cycles, one in the high-temperature region and the other in the low-temperature region.

Such a cycle is called a binary vapor cycle. In binary vapor cycles, the condenser of the high-temperature cycle (also called the topping cycle) serves as the boiler of the low-temperature cycle (also called the bottoming cycle).

That is, the heat output of the high-temperature cycle is used as the heat input to the low-temperature one.

Page 49: Vapor Power Cycles

Mercury–water binary vapour cycle.

cascadeCycle.swf

Page 50: Vapor Power Cycles

New ideas

• Cogeneration• Gas-vapor Combined power cycles

Page 51: Vapor Power Cycles

MODIFIED RANKINE CYCLE

Page 52: Vapor Power Cycles

MODIFIED RANKINE