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Generation of Eco-friendly Steam in Power Plants

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Presentation on theme: "Generation of Eco-friendly Steam in Power Plants"— Presentation transcript:

1 Generation of Eco-friendly Steam in Power Plants
P M V Subbarao Professor Mechanical Engineering Department Generation of Entropy to Generate Most Eligible Steam …..

2 Cost to Benefit Ratio Analysis of Rankine Cycle

3 Heat Rate: An International Standard
The term “heat rate” simply refers to energy conversion efficiency, in terms of “how much energy must be expended in order to obtain a unit of useful work.” In a combustion power plant, the fuel is the energy source, and the useful work is the electrical power supplied to the grid. Because “useful work” is typically defined as the electricity, engineers tend to work with the net plant heat rate (NPHR). Units: kJ/kW-hr or kCal /kW-hr

4 Method of Calculation Net Plant power output : Pnet in kW
Fuel consumption rate: mfuel kg/hr Higher heating value or higher calorific value: HHV in kJ/kg

5 Economics of Flow Steam generation

6 Economics of Flow Steam generation
Supercritical Steam Generation Subcritical Flow Boiling Pump Exit

7 Natural Circulation Boiler
Dry Steam to Super heaters Pump Exit Wet Steam Hot Water

8 Forced Circulation Boiler
Dry Steam to Super heaters Pump Exit Wet Steam Hot Water Recirculation Pump

9 Once Through Boiler Dry Steam to Super heaters Hot Water Pump

10 Once Through Subcritical Steam Generator
Once-through tangential fired Max. continuous rating: 520 kg/s Max.Steam temperature outlet: 540°C Live steam pressure outlet: > 18.3 MPa

11 Super Critical Nuclear Reactor

12 Ranking Cycle using Solar Thermal Energy
Steam at a pressure of 23.5 MPa and 570° C

13 Clues to Generate High Economy and Eco-friendly Steam

14 Constant Pressure Steam Generation Process
Theory of flowing Steam Generation

15 Selection of Steam Generation Pressure in A Rankine Cycle
T C v, m3/kg

16 Entropy, x=s : A Measure of State of Matter
So (J/K•mol) H2O(liq) 69.95 H2O(gas) 188.8 For a given substance S (gaseous state) > S (liquid state) > S (solid state)

17 Entropy and Order of Molecules of Matter
S˚(Br2 liq) < S˚(Br2 gas) S˚(H2O solid) < S˚(H2O liquid)

18 Entropy, S : Molecular Complexity
Increase in molecular complexity generally leads to increase in S.

19 Standard Molar Entropies

20 Entropy and Temperature
S increases slightly with T S increases a large amount with phase changes

21 Entropy Change during a Reversible Process
From the definition of the entropy, it is known that Q=TdS during a reversible process. The total heat transfer during this process is given by Qreversible =  TdS Therefore, it is useful to consider the T-S diagram for a reversible process involving heat transfer T S On a T-S diagram, the area under the process curve represents the heat transfer for a reversible process A reversible adiabatic process

22 Process : h-s Diagram : Mollier Diagram
Enthalpy-entropy diagram, h-s diagram: it is valuable in analyzing steady-flow devices such as turbines, compressors, etc. Dh: change of enthalpy from energy balance (from the first law of thermodynamics) Ds: change of entropy from the second law. A measure of the irreversibilities during an adiabatic process. Ds Dh h s

23 Enthalpy Vs Entropy Diagram

24 Constant Pressure Steam Generation Process
Theory of flowing Steam Generation Constant Pressure Steam Generation: A clue to get high temperature with same amount of burnt fuel

25 Steam Generation : Expenditure vs Wastage
Vapour h mfuel Liquid +Vapour Liquid x

26 Steam Generation At High Pressure
x=s

27 Analysis of Steam Generation at Various Pressures
Specific Pressure Enthalpy Entropy Temp MPa kJ/kg kJ/kg/K C 1 3500 7.79 509.9 2 5 7.06 528.4 3 10 6.755 549.6 4 15 6.582 569 20 6.461 586.7 6 25 6.37 602.9 7 30 6.297 617.7 8 35 6.235 631.3

28 Fuel Savings during Steam Generation
Specific Temp Pressure Enthalpy Entropy C MPa kJ/kg kJ/kg/K 575 5 3608 7.191 10 3563 6.831 12.5 3540 6.707 15 3516 6.601 17.5 3492 6.507 20 3467 6.422 22.5 3441 6.344 25 3415 6.271 30 3362 6.138 35 3307 6.015

29 Law of Nature Behavior of Vapour at Increasing Pressures
Reversible nature of substance at a given temperature All these show that the irreversible behavior of a fluid decreased with increasing pressure.

30 Reduction of Wastage

31 Less Fuel for Creation of Same Temperature

32 The Training for High Altitude Trekking

33 Classification of Rankine Cycles

34 Parametric Study of Rankine Cycle
h P max

35 Specific Volume vs Temperature
@15MPa @35MPa

36 Parametric Study of Rankine Cycle
23.5MPa 22MPa 18MPa 10MPa 6MPa 3MPa h 1MPa Tmax

37

38 Reheating : A Means to implement High Live Steam Pressure
Supercritical 593/6210C 593/5930C 565/5930C 565/5650C 538/5650C Improvement in Efficiency, % 538/5380C


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