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CARNOT CYCLE
• This cycle is of great value to heat power theory
although it has not been possible to construct a
practical plant on this cycle. It has high
thermodynamics efficiency.
• It is a standard of comparison for all other cycles.
The thermal efficiency (η) of Carnot cycle is as
follows:
– η = (T1 – T2)/T1
– where, T1 = Temperature of heat source
– T2 = Temperature of receiver
RANKINE CYCLE
• Many of the impracticalities of Carnot Cycle can be eliminated by super heating
steam in boiler and condensing it completely in condenser.
• Steam engine and steam turbines in which steam is used as working medium
follow Rankine cycle.
• This cycle can be carried out in four pieces of equipment joint by pipes for
conveying working medium
• Efficiency of Rankine cycle = (H1 – H2)/ (H1 – Hw2)
where,
– Hl = Total heat of steam at entry pressure
– H2 = Total heat of steam at condenser pressure
– (exhaust pressure)
– Hw2= Total heat of water at exhaust pressure
REHEAT CYCLE
In this cycle steam is extracted from a suitable
point in the turbine and reheated generally to
the original temperature by flue gases.
Reheating is generally used when the pressure
is high say above 100 kg/cm2.
First turbine is high-pressure
turbine and second turbine is
low pressure (L.P.) turbine. This
cycle is shown on T-S
(Temperature entropy) diagram
If,
H1 = Total heat of steam at 1
H2 = Total heat of steam at 2
H3 = Total heat of steam at 3
H4 = Total heat of steam at 4
Hw4 = Total heat of water at 4
Efficiency = {(H1 – H2) + (H3 – H4)}/{H1 + (H3 – H2) – Hw4}
The various advantages of reheating are as follows:
(i) It increases dryness fraction of steam at exhaust so that
blade erosion due to impact of water particles is reduced.
(ii) It increases thermal efficiency.
(iii) It increases the work done per kg of steam and this results
in reduced size of boiler.
The disadvantages of reheating are as follows:
(i) Cost of plant is increased due to the reheater and its long
connections.
(ii) It increases condenser capacity due to increased dryness
fraction.
REGENERATIVE CYCLE (FEED WATER
HEATING)
The process of extracting steam from the
turbine at certain points during its expansion
and using this steam for heating for feed
water is known as Regeneration or Bleeding of
steam. The arrangement of bleeding the
steam at two stages
These heat exchangers are called regenrator
or feedwater heater.
Let,
• m2 = Weight of bled steam at
a per kg of feed water heated
• m2 = Weight of bled steam at a
per kg of feed water heated
• H1 = Enthalpies of steam and water
in boiler
• Hw1 = Enthalpies of steam and water in boiler
• H2, H3 = Enthalpies of steam at points a and b
• t2, t3 = Temperatures of steam at points a and b
• H4, Hw4 = Enthalpy of steam and water exhausted to hot well.
• Work done in turbine per kg of feed water between entrance and
a = H1 – H2
• Work done between a and b = (1 – m2)(H2 – H3)
• Work done between b and exhaust = (1 – m2 – m3)(H3 – H4)
• Total heat supplied per kg of feed water = H1 – Hw2
• Efficiency (η) = Total work done/Total heat supplied
= {(H1 – H2) + (1 – m2)(H2 – H3) + (1 – m2 – m3)(H3 – H4)}/(H1 – Hw2)
BINARY VAPOUR CYCLE
In this cycle two working fluids are
used. The mercury boiler heats the
mercury into mercury vapours in a dry
and saturated state. These mercury
vapours expand in the mercury
turbine and then flow through heat
exchanger where they transfer the
heat to the feed water, convert it into
steam. The steam is passed through
the steam super heater where the
steam is super-heated by the hot flue
gases. The steam then expands in the
steam turbine.

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Types of thermodynamic Cycles for Power Generator

  • 1. CARNOT CYCLE • This cycle is of great value to heat power theory although it has not been possible to construct a practical plant on this cycle. It has high thermodynamics efficiency. • It is a standard of comparison for all other cycles. The thermal efficiency (η) of Carnot cycle is as follows: – η = (T1 – T2)/T1 – where, T1 = Temperature of heat source – T2 = Temperature of receiver
  • 2. RANKINE CYCLE • Many of the impracticalities of Carnot Cycle can be eliminated by super heating steam in boiler and condensing it completely in condenser. • Steam engine and steam turbines in which steam is used as working medium follow Rankine cycle. • This cycle can be carried out in four pieces of equipment joint by pipes for conveying working medium • Efficiency of Rankine cycle = (H1 – H2)/ (H1 – Hw2) where, – Hl = Total heat of steam at entry pressure – H2 = Total heat of steam at condenser pressure – (exhaust pressure) – Hw2= Total heat of water at exhaust pressure
  • 3. REHEAT CYCLE In this cycle steam is extracted from a suitable point in the turbine and reheated generally to the original temperature by flue gases. Reheating is generally used when the pressure is high say above 100 kg/cm2.
  • 4. First turbine is high-pressure turbine and second turbine is low pressure (L.P.) turbine. This cycle is shown on T-S (Temperature entropy) diagram If, H1 = Total heat of steam at 1 H2 = Total heat of steam at 2 H3 = Total heat of steam at 3 H4 = Total heat of steam at 4 Hw4 = Total heat of water at 4 Efficiency = {(H1 – H2) + (H3 – H4)}/{H1 + (H3 – H2) – Hw4}
  • 5. The various advantages of reheating are as follows: (i) It increases dryness fraction of steam at exhaust so that blade erosion due to impact of water particles is reduced. (ii) It increases thermal efficiency. (iii) It increases the work done per kg of steam and this results in reduced size of boiler. The disadvantages of reheating are as follows: (i) Cost of plant is increased due to the reheater and its long connections. (ii) It increases condenser capacity due to increased dryness fraction.
  • 6. REGENERATIVE CYCLE (FEED WATER HEATING) The process of extracting steam from the turbine at certain points during its expansion and using this steam for heating for feed water is known as Regeneration or Bleeding of steam. The arrangement of bleeding the steam at two stages These heat exchangers are called regenrator or feedwater heater.
  • 7. Let, • m2 = Weight of bled steam at a per kg of feed water heated • m2 = Weight of bled steam at a per kg of feed water heated • H1 = Enthalpies of steam and water in boiler • Hw1 = Enthalpies of steam and water in boiler • H2, H3 = Enthalpies of steam at points a and b • t2, t3 = Temperatures of steam at points a and b • H4, Hw4 = Enthalpy of steam and water exhausted to hot well. • Work done in turbine per kg of feed water between entrance and a = H1 – H2 • Work done between a and b = (1 – m2)(H2 – H3) • Work done between b and exhaust = (1 – m2 – m3)(H3 – H4) • Total heat supplied per kg of feed water = H1 – Hw2 • Efficiency (η) = Total work done/Total heat supplied = {(H1 – H2) + (1 – m2)(H2 – H3) + (1 – m2 – m3)(H3 – H4)}/(H1 – Hw2)
  • 8. BINARY VAPOUR CYCLE In this cycle two working fluids are used. The mercury boiler heats the mercury into mercury vapours in a dry and saturated state. These mercury vapours expand in the mercury turbine and then flow through heat exchanger where they transfer the heat to the feed water, convert it into steam. The steam is passed through the steam super heater where the steam is super-heated by the hot flue gases. The steam then expands in the steam turbine.