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Power plant engineering
Chapter 2
Rankine power cycle
Rankine power cycle
T-s diagram Rankine power cycle
p-v diagram Rankine power cycle
h-s diagram Rankine power cycle
Rankine cycle processes
Thermal Efficiency of Rankine Cycle:
• Consider one kg of working fluid, and applying
first law to flow system to various processes
with the assumption of neglecting changes in
potential and kinetic energy, we can write,
Thermal Efficiency of Rankine Cycle:
Thermal Efficiency of Rankine Cycle:
Thermal Efficiency of Rankine Cycle:
Reasons for Considering Rankine
Cycle as an Ideal Cycle For Steam
Power Plants:
Reasons for Considering Rankine
Cycle as an Ideal Cycle For Steam
Power Plants:
Practical Rankine cycle
Practical Rankine cycle
Practical Rankine cycle
• Pump and Turbine do not operate isentropically
in practice.
The practical Rankine cycle is shown as 1-2’-3-4’
1.
In the actual turbine, the work delivered is less
than the isentropic turbine.
Similarly, the work consumed by an actual pump is
greater than the work consumed by an isentropic
pump.
Practical Rankine cycle
• h3-h4’ < h3-h4
• h2’-h1 > h2-h1
'
23
1
'
2
'
43 )()(
hh
hhhh



Practical Rankine cycle
43
'
43
hh
hh
T



Isentropic efficiency of turbine (T)
Practical Rankine cycle
Isentropic efficiency of pump (P)
1
'
2
12
hh
hh
P



Methods to increase the efficiency of
the Rankine cycle
Basic idea:
• 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.
1. Lowering the condenser Pressure:-
1. Lowering the condenser Pressure
• Lowering the operating pressure of the
condenser lowers the temperature at which
heat is rejected.
• The overall effect of lowering the condenser
pressure is an increase in the thermal
efficiency of the cycle.
Superheating the steam to high
temperatures:-
Superheating the steam to high
temperatures:-
• The average temperature at which heat is
added to the steam can be increased without
increasing the boiler pressure by superheating
the steam to high temperatures.
• Superheating the steam to higher
temperatures has another very desirable
effect: It decreases the moisture content of
the steam at the turbine exit.
Increasing the Boiler pressure:-
Increasing the Boiler pressure:-
• Increasing the operating pressure of the
boiler, automatically raises the temperature at
which boiling takes place.
• This raises the average temperature at which
heat is added to the steam and thus raises the
thermal efficiency of the cycle
Reheat Rankine Cycle
Reheat Rankine Cycle
Reheat Rankine Cycle
The energy added ( per unit mass of steam ) in the steam generator
is given by,
)()( 45231 hhhhq 
The energy rejected in the condenser,
162 hhq 
Reheat Rankine Cycle
The thermal efficiency,
)()(
)()()(
4523
164523
hhhh
hhhhhh



Regenerative Cycle
Regenerative Cycle
Closed Feed water Heaters
In closed FWH, heat is transferred from the extracted steam to
the feedwater without any mixing taking place. Thus; two
streams can be at different pressures, since they don’t mix.
Binary vapor cycle
• In the vapour power cycles most commonly used
working fluid is water.
• But at high temperatures to get the high
efficiency of vapour power cycle, some other
working fluids are used.
• At high temperatures a few working fluids are
used, which are mercury, sodium, potassium and
sodium-potassium mixtures.
• Among these, only mercury has been used in
practice.
Binary vapor cycle
For the best performance, the working fluid
should have the following characteristics
High Critical temperature and safe maximum
pressure,
• Low triple point temperature,
• Condenser pressure which is not too low,
• High enthalpy of vaporization,
• Good heat transfer characteristics, and
• Inert, easy availability at low cost.
Binary vapor cycle
To increase the efficiency of Carnot
cycle, with an increase in initial
temperature or with the decrease in
exit temperature of the fluid.
At the normal pressure of 12 bar, the
saturation temperature for water and
mercury are 187oC, 560oC, respectively.
Binary vapor cycle
 The highest temperature achieved in a power
plants is about 550oC – 600oC. Therefore
mercury is a better working fluid in the high
temperature range, because its vaporization
pressure is relatively low.
 Mercury vapour at high temperature with low
pressure which avoid the difficulties
connected with high pressure.
Binary vapor cycle
• To get the high thermal efficiency of the
power plant, by using two working fluids such
as water and mercury, the binary vapour cycle
has been developed.
• The power cycle, which is a combination of
two cycles, one in the high temperature
region and the other in the low temperature
region, called the binary vapour cycle.
Binary vapor cycle
• In this cycle, the condenser of the high
temperature cycle called the tapping cycle
serves as the boiler of the low temperature
cycle, termed the bottom cycle.
• Mercury water binary vapour cycle it is called
Binary vapor cycle
Super critical power cycles
Rankine Cycle Subcritical Unit
Rankine Cycle Supercritical Unit
VARIATION OF LATENT HEAT
WITH PRESSURE
Supercritical Unit
Advanced Supercritical Tube
Materials at 300 bar
Advantages of supercritical power
cycle
Higher cycle efficiency means Primarily
• less fuel consumption
• less per MW infrastructure
investments
• less emission
• less auxiliary power consumption
• less water consumption
Advantages of supercritical power
cycle
Operational flexibility
• Better temp. control and load change
flexibility
• Shorter start-up time
• More suitable for widely variable pressure
operation
Advantages of supercritical power
cycle
Higher Efficiency (η%)
• Less fuel input.
• Low capacity fuel handling system.
• Low capacity ash handling system.
• Less Emissions.
Advantages of supercritical power
cycle
Increase of Cycle Efficiency due to
Steam Parameters
Increase of Cycle Efficiency due to
Steam Parameters
COMBINED CYCLE POWER PLANT
Combined cycle is a characteristics’ of a power
producing engine or plant that employs more than
one thermodynamic cycle.
Heat engine are only able to use a portion of the
energy of their generation usually less than 50%.
The remaining heat from combustion is generally
wasted.
Combining two or more cycle such as Brayton cycle
and Rankine cycle results in improved overall
efficiency.
COMBINED CYCLE POWER PLANT
In a combined cycle power plant (CCPP) or combined
cycle gas turbine (CCGT) plant Turbine generator generates
electricity and waste heat is used to make steam to generate
additional electricity via a steam turbine, this last step enhances
the efficiency of electricity generation.
As a rule, in order to achieve high efficiency, the temperature
difference between the input and output heat levels be as high as
possible.
This is achieved by combined the Brayton (gas) and Rankine
(steam) thermodynamics cycle.
Energy distribution in CCPP
•distribution of the entering energy in to
its useful component and the energy
losses which are associated with the
condenser and stack losses.
•This distribution will vary some with
different cycle as the stack losses
decreased with more efficient multi level
pressure heat recovery steam generating
(HRSG) units.
Load sharing between power cycles
Load sharing between power cycles
• The gas turbine at design supplies 60%
of the total energy delivered and steam
turbine delivers 40% of energy.
• while at off design conditions (below
50% of design energy), the gas turbine
delivers 40% of the energy while the
steam turbine delivers 60% of energy
Main components of combined cycle
power plants:
Compressor:
• A compressor is a device, which pressurizes a
working fluid.
• There are three types of compressors. The
positive displacement compressors are used
for low flow and high head, centrifugal
compressor are medium flow and medium
head, and axial flow compressor for high flow
and low head.
• Nearly all gas turbine plants producing over 5
MW have axial flow compressors.
Main components of combined cycle
power plants:
Compressor of CCPP
•In an axial flow compressor air passes
from one stage to the next with each
stage raising the pressure slightly.
•By producing low pressure increases on
the order of 1.1 to 1.4, very high
efficiencies can be obtained.
•The use of multiple stages permits
overall pressure increase up to 40:1.
Compressor of CCPP
• The rule of thumb for a multiple stage gas
turbine compressor would be that the energy
raise per stage would be constant rather than
pressure raise per stage. The compressor
produces 30:1 pressure in 22 stages.
• The centrifugal compressor is slightly less
efficient than the axial flow compressor, but it
has a higher stability.
• A higher stability that it’s operating range is
greater (surge to choke margin).
Combustor of CCPP
Combustor of CCPP
• All gas turbine combustors perform the same function;
they increase the temperature of the high-pressure
gas.
• The gas turbine combustor uses very little of its air
(10%) in the combustion process.
• The rest of the air is used for cooling and mixing.
• The new combustors are also used circulating steam
for cooling purposes.
• The air from the compressor must be diffused before it
enters the combustor.
• The velocity of the air leaving the compressor is about
122 to 183 (m/sec) and the velocity in the combustor
must be maintained below 15.2 (m/sec).
Combustor of CCPP
• Even at these low velocities care must be
taken to avoid the flame to be carried on
downstream.
• The combustor is a direct-fired air heater in
which fuel is burned almost
stoichiometrically with one third or less of
the compressor discharge air.
• Combustion products are then mixed with
the remaining air to arrive at a suitable
turbine inlet temperature.
Combustor of CCPP
• Despite the many design differences in
combustors, all gas turbine combustion
chambers have three features: (1) a
recirculation zone, (2) a burning zone (with a
recirculation zone, which extends to the
dilution region), and (3) a dilution zone.
• The air entering a combustor is divided so that
the flow is distributed between three major
regions: (1) Primary Zone, (2) Dilution Zone,
and (3) Annular space between the liner and
casing.
Combustor of CCPP
• Combustor performance is measured by
efficiency, the pressure decrease encountered
in the combustor, and the evenness of the
outlet temperature profile.
• The combustion efficiency is a measure of
combustion completeness.
• The combustion completeness affects fuel
consumption directly, since the heating value
of any unburned fuel is not used to increase
the turbine inlet temperature.
• Normal combustion temperatures range from
1871°C to 1927°C.
Combustor of CCPP
• At this temperature, the volume of nitric oxide
in the combustion gas is about 0.01%.
• If the combustion temperature is lowered, the
amount of nitric oxide is substantially
reduced.
Gas turbine
There are two types of turbine used in
gas turbine
• I. Axial flow turbine
• II. Radial flow turbine
Gas turbine
• The axial flow turbine, like its counter
parts the axial flow compressor, has
flow which inter and leaves in the axial
direction.
• Most axial flow turbine consist of more
than one stage: the front stages are
usually impulses (zero reaction) and the
later stages have about 50% reaction.
Gas turbine
• The impulses stages produces about
twice output of a comparable 50%
reaction stage, while the efficiency of an
impulses stage is less than that of 50%
reaction stages.
• The high temperatures that are now
available in the turbine section are due to
improvements of the metallurgy of the
blades in the turbines.
Gas turbine
• The developments of directionally solidified
blades as well as the new single crystal blades,
with the new coatings, and the new cooling
schemes, are responsible for the increase in firing
temperatures.
• The high-pressure ratio in the compressor also
causes the cooling air used in the first stages of
the turbine to be very hot.
• The temperatures leaving the gas turbine
compressor can reach as high as 649 °C.
Gas turbine
• Thus, the present cooling schemes need revisiting
and the cooling passages are in many cases also
coated.
• The cooling schemes are limited in the amount of
air they can use, before there is a negative effort
in overall thermal efficiency due to an increase in
the amount of air used in cooling.
• The rule of thumb in this area is that if you need
more than 8% of the air for cooling we are loosing
the advantage from the increase in the firing
temperature.
Gas turbine
• The new gas turbines being designed
for the new millennium are
investigating the use of steam as a
cooling agent for the first and second
stages of the turbines.
• Steam cooling is possible in the new
combined cycle power plants, which is
the base of most of the new High
Performance Gas Turbines (HPGT).
Gas turbine
• Steam as part of the cooling as well as part of the
cycle power will be used in the new gas turbines
in the combined cycle mode.
• The injection of about 5% of steam by weight of
air amounts to about 12% more power.
• The pressure of the injected steam must be at
least 4 bar above the compressor discharge.
• The way of steam injected must be done very
carefully so as to avoid compressor surge. By
using the steam cooling the firing temperature
reaches upto 1649°C.
Gas turbine
• Since 1950, turbine bucket material temperature
capability has advanced approximately 472°C.
• The importance of this increase can be
appreciated by noting that an increase of 56°C in
turbine firing temperature can provide a
corresponding increase of 8–13% in output and 2–
4% improvement in simple-cycle efficiency.
• Advances in alloys and processing, while expensive
and time-consuming, provide significant incentives
through increased power density and improved
efficiency.
Gas turbine
• In the late 1990s, single-crystal blades were
introduced in gas turbines.
• These blades offer additional creep and
fatigue benefits through the elimination of
grain boundaries.
• In single-crystal material, all grain
boundaries are eliminated from the
material structure and a single crystal with
controlled orientation is produced in an
airfoil shape.
Gas turbine
• By eliminating all grain boundaries and the
associated grain boundary strengthening
additives, a substantial increase in the melting
point of the alloy can be achieved, thus providing
a corresponding increase in high-temperature
strength.
• The transverse creep and fatigue strength is
increased, compared to equiaxed or DS
structures.
• The advantage of single-crystal alloys compared
to equiaxed and DS alloys in low-cycle fatigue
(LCF) life is increased by about 10%.
Coatings
• There are three basic types of coatings:
thermal barrier coatings, diffusion coatings,
and plasma sprayed coatings.
• The advancements in coating have also been
essential in ensuring that the blade base metal
is protected at these high temperatures.
• Coatings ensure that the life of the blades is
extended and in many cases are used as
sacrificial layers, which can be stripped and
recoated.
Coatings
• The life of a coating depends on
composition, thickness, and the standard
of evenness to which it has been
deposited.
• The general type of coatings is little
different from the coatings used 10-15
years ago.
• These include various types of diffusion
coatings such as aluminide coatings
originally developed nearly 40 years ago.
Coatings
• The thickness required is between 25–75 μm
thick.
• The new aluminide coatings with platinum
increase the oxidation resistance, and also the
corrosion resistance.
• The thermal barrier coatings have an insulation
layer of 100–300 μm thick, are based on ZrO2-
Y2O3, and can reduce metal temperatures by
50°C–150°C.
• This type of coating is used in combustion cans,
transition pieces, nozzle guide vanes, and also
blade platforms.
Heat recovery steam generator
(HRSG)
• The gas turbine exhaust gases enter the Heat
Recovery Steam Generator (HRSG), where the
energy is transferred to the water to produce steam.
• There are many different configurations of the HRSG
units.
• Most HRSG units are divided into the same amount
of sections as the steam turbine.
• In most cases, each section of the HRSG has a Pre-
heater, an Economizer and Feed-water, and then a
Super heater.
• The steam entering in the steam turbine is
superheated.
Heat recovery steam generator
(HRSG)
• The most common type of an HRSG in a
large Combined Cycle Power plant is the
drum type HRSG with forced circulation.
• These types of HRSGs are vertical; the
exhaust gas flow is vertical with horizontal
tube bundles suspended in the steel
structure.
• The steel structure of the HRSG supports the
drums.
Heat recovery steam generator
(HRSG)
• In a forced circulation HRSG, then the steam water
mixture is circulated through evaporator tubes
using a pump.
• These pumps increase the parasitic load and thus
detract from the cycle efficiency.
• In this type of HRSG the heat transfer tubes are
horizontal, suspended from un-cooled tube
supports located in the hot gas path.
• Some vertical HRSGs are designed with
evaporators, which operate without the use of
circulation pumps.
Multipressure Steam Generators
• These are becoming increasingly popular.
• With a single pressure boiler, there is a
limit to the heat recovery because the
exhaust gas temperature cannot be
reduced below the steam saturation
temperature.
• This problem is avoided by the use of
multipressure levels.
Pinch Point
• This is defined as the difference
between the exhaust gas temperature
leaving the evaporator section and the
saturation temperature of the steam.
• Ideally, the lower the pinch point, the
more heat recovered, but this calls for
more surface area and, consequently,
increases the backpressure and cost.
Pinch Point
• Also, excessively low pinch points can
mean inadequate steam production if the
exhaust gas is low in energy (low mass
flow or low exhaust gas temperature).
• General guidelines call for a pinch point of
8°C–22°C.
• The final choice is obviously based on
economic considerations.
Approach Temperature
• This is defined as the difference between the
saturation temperatures of the steam and the inlet
water.
• Lowering the approach temperature can result in
increased steam production, but at increased cost.
• Conservatively high-approach temperatures ensure
that no steam generation takes place in the
economizer.
• Typically, approach temperatures are in the
5.5°C –11°C range.
Gas turbine Design considerations
• The two factors, which most affect high turbine
efficiencies, are pressure ratios and
temperature.
• The axial-flow compressor, which produces the
high-pressure gas in the turbine, has seen
dramatic change as the gas turbine pressure
ratio has increased from 7:1 to 40:1.
• The increase in pressure ratio increases the gas
turbine thermal efficiency when accompanied
with the increase in turbine firing temperature.
Gas turbine Design considerations
• The increase in the pressure ratio
increases the overall efficiency at a given
temperature, however increasing the
pressure ratio beyond a certain value at
any given firing temperature can actually
result in lowering the overall cycle
efficiency.
• It should also be noted that the very high-
pressure ratios tend to reduce the
operating range of the turbine
compressor.
Gas turbine Design considerations
• This causes the turbine compressor to be
much more intolerant to dirt build-up in the
inlet air filter and on the compressor blades
and creates large drops in cycle efficiency and
performance.
• In some cases, it can lead to compressor
surge, which in turn can lead to a flame out,
or even serious damage and failure of the
compressor blades and the radial and thrust
bearings of the gas turbine.
Gas turbine Design considerations
• The effect of firing temperature is very
predominant—for every 55.5°C increase in
temperature, the work output increases
approximately 10% and gives about a 1.5%
increase in efficiency.
• Higher-pressure ratios and turbine inlet
temperatures improve efficiencies on the
simple-cycle gas turbine.
Gas turbine Design considerations
• The latest frame type unit introduce are 480
MW units using steam cooling in combined
cycle mode, enabling the firing temperature to
reach 1427°C.
• This enables efficiency in the combined cycle
mode to reach more than 60% in the area of
performance; the steam turbine power plants
have an efficiency of about 35%, as compared to
combined cycle power plants, which have an
efficiency of about 55%.
Gas turbine Design considerations
• Newer Gas Turbine technology will make
combined cycle efficiencies range between
60–65%.
• As a rule of thumb a 1% increase in efficiency
could mean that 3.3% more capital can be
invested.
• However one must be careful that the increase
in efficiency does not lead to a decrease in
availability.
Gas turbine Design considerations
• It can be seen from literature the
growth in efficiency of about 10% and
a loss in availability of about 10%.
• This trend must be turned around
since many analyses show that a 1%
drop in the availability needs about a
2–3% increase in efficiency to offset
that loss.
Gas turbine Design considerations
• The time taken to install a steam plant
from conception to production is about
42–60 months as compared to 22–36
months for combined cycle power plants.
• actual construction time is about 18
months, while environmental permits in
many cases take 12 months and
engineering 6–12 months.
Gas turbine Design considerations
• The time taken for bringing the plant
online affects the economics of the
plant, the longer capital is employed
without return, the plant accumulates
interest, insurance, and taxes.
• It is obvious from this that as long as
natural gas or diesel fuel is available the
choice of combined cycle power plants
is obvious.

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Power plant engineering chapter 2

  • 4. T-s diagram Rankine power cycle
  • 5. p-v diagram Rankine power cycle
  • 6. h-s diagram Rankine power cycle
  • 8. Thermal Efficiency of Rankine Cycle: • Consider one kg of working fluid, and applying first law to flow system to various processes with the assumption of neglecting changes in potential and kinetic energy, we can write,
  • 9. Thermal Efficiency of Rankine Cycle:
  • 10. Thermal Efficiency of Rankine Cycle:
  • 11. Thermal Efficiency of Rankine Cycle:
  • 12. Reasons for Considering Rankine Cycle as an Ideal Cycle For Steam Power Plants:
  • 13. Reasons for Considering Rankine Cycle as an Ideal Cycle For Steam Power Plants:
  • 16. Practical Rankine cycle • Pump and Turbine do not operate isentropically in practice. The practical Rankine cycle is shown as 1-2’-3-4’ 1. In the actual turbine, the work delivered is less than the isentropic turbine. Similarly, the work consumed by an actual pump is greater than the work consumed by an isentropic pump.
  • 17. Practical Rankine cycle • h3-h4’ < h3-h4 • h2’-h1 > h2-h1 ' 23 1 ' 2 ' 43 )()( hh hhhh   
  • 19. Practical Rankine cycle Isentropic efficiency of pump (P) 1 ' 2 12 hh hh P   
  • 20. Methods to increase the efficiency of the Rankine cycle Basic idea: • 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.
  • 21. 1. Lowering the condenser Pressure:-
  • 22. 1. Lowering the condenser Pressure • Lowering the operating pressure of the condenser lowers the temperature at which heat is rejected. • The overall effect of lowering the condenser pressure is an increase in the thermal efficiency of the cycle.
  • 23. Superheating the steam to high temperatures:-
  • 24. Superheating the steam to high temperatures:- • The average temperature at which heat is added to the steam can be increased without increasing the boiler pressure by superheating the steam to high temperatures. • Superheating the steam to higher temperatures has another very desirable effect: It decreases the moisture content of the steam at the turbine exit.
  • 25. Increasing the Boiler pressure:-
  • 26. Increasing the Boiler pressure:- • Increasing the operating pressure of the boiler, automatically raises the temperature at which boiling takes place. • This raises the average temperature at which heat is added to the steam and thus raises the thermal efficiency of the cycle
  • 29. Reheat Rankine Cycle The energy added ( per unit mass of steam ) in the steam generator is given by, )()( 45231 hhhhq  The energy rejected in the condenser, 162 hhq 
  • 30. Reheat Rankine Cycle The thermal efficiency, )()( )()()( 4523 164523 hhhh hhhhhh   
  • 32. Regenerative Cycle Closed Feed water Heaters In closed FWH, heat is transferred from the extracted steam to the feedwater without any mixing taking place. Thus; two streams can be at different pressures, since they don’t mix.
  • 33. Binary vapor cycle • In the vapour power cycles most commonly used working fluid is water. • But at high temperatures to get the high efficiency of vapour power cycle, some other working fluids are used. • At high temperatures a few working fluids are used, which are mercury, sodium, potassium and sodium-potassium mixtures. • Among these, only mercury has been used in practice.
  • 34. Binary vapor cycle For the best performance, the working fluid should have the following characteristics High Critical temperature and safe maximum pressure, • Low triple point temperature, • Condenser pressure which is not too low, • High enthalpy of vaporization, • Good heat transfer characteristics, and • Inert, easy availability at low cost.
  • 35. Binary vapor cycle To increase the efficiency of Carnot cycle, with an increase in initial temperature or with the decrease in exit temperature of the fluid. At the normal pressure of 12 bar, the saturation temperature for water and mercury are 187oC, 560oC, respectively.
  • 36. Binary vapor cycle  The highest temperature achieved in a power plants is about 550oC – 600oC. Therefore mercury is a better working fluid in the high temperature range, because its vaporization pressure is relatively low.  Mercury vapour at high temperature with low pressure which avoid the difficulties connected with high pressure.
  • 37. Binary vapor cycle • To get the high thermal efficiency of the power plant, by using two working fluids such as water and mercury, the binary vapour cycle has been developed. • The power cycle, which is a combination of two cycles, one in the high temperature region and the other in the low temperature region, called the binary vapour cycle.
  • 38. Binary vapor cycle • In this cycle, the condenser of the high temperature cycle called the tapping cycle serves as the boiler of the low temperature cycle, termed the bottom cycle. • Mercury water binary vapour cycle it is called
  • 40.
  • 44. VARIATION OF LATENT HEAT WITH PRESSURE
  • 45.
  • 46.
  • 47.
  • 48.
  • 51.
  • 52. Advantages of supercritical power cycle Higher cycle efficiency means Primarily • less fuel consumption • less per MW infrastructure investments • less emission • less auxiliary power consumption • less water consumption
  • 53. Advantages of supercritical power cycle Operational flexibility • Better temp. control and load change flexibility • Shorter start-up time • More suitable for widely variable pressure operation
  • 54. Advantages of supercritical power cycle Higher Efficiency (η%) • Less fuel input. • Low capacity fuel handling system. • Low capacity ash handling system. • Less Emissions.
  • 56. Increase of Cycle Efficiency due to Steam Parameters
  • 57. Increase of Cycle Efficiency due to Steam Parameters
  • 58. COMBINED CYCLE POWER PLANT Combined cycle is a characteristics’ of a power producing engine or plant that employs more than one thermodynamic cycle. Heat engine are only able to use a portion of the energy of their generation usually less than 50%. The remaining heat from combustion is generally wasted. Combining two or more cycle such as Brayton cycle and Rankine cycle results in improved overall efficiency.
  • 59. COMBINED CYCLE POWER PLANT In a combined cycle power plant (CCPP) or combined cycle gas turbine (CCGT) plant Turbine generator generates electricity and waste heat is used to make steam to generate additional electricity via a steam turbine, this last step enhances the efficiency of electricity generation. As a rule, in order to achieve high efficiency, the temperature difference between the input and output heat levels be as high as possible. This is achieved by combined the Brayton (gas) and Rankine (steam) thermodynamics cycle.
  • 60.
  • 61.
  • 62. Energy distribution in CCPP •distribution of the entering energy in to its useful component and the energy losses which are associated with the condenser and stack losses. •This distribution will vary some with different cycle as the stack losses decreased with more efficient multi level pressure heat recovery steam generating (HRSG) units.
  • 63. Load sharing between power cycles
  • 64. Load sharing between power cycles • The gas turbine at design supplies 60% of the total energy delivered and steam turbine delivers 40% of energy. • while at off design conditions (below 50% of design energy), the gas turbine delivers 40% of the energy while the steam turbine delivers 60% of energy
  • 65. Main components of combined cycle power plants: Compressor: • A compressor is a device, which pressurizes a working fluid. • There are three types of compressors. The positive displacement compressors are used for low flow and high head, centrifugal compressor are medium flow and medium head, and axial flow compressor for high flow and low head. • Nearly all gas turbine plants producing over 5 MW have axial flow compressors.
  • 66. Main components of combined cycle power plants:
  • 67. Compressor of CCPP •In an axial flow compressor air passes from one stage to the next with each stage raising the pressure slightly. •By producing low pressure increases on the order of 1.1 to 1.4, very high efficiencies can be obtained. •The use of multiple stages permits overall pressure increase up to 40:1.
  • 68. Compressor of CCPP • The rule of thumb for a multiple stage gas turbine compressor would be that the energy raise per stage would be constant rather than pressure raise per stage. The compressor produces 30:1 pressure in 22 stages. • The centrifugal compressor is slightly less efficient than the axial flow compressor, but it has a higher stability. • A higher stability that it’s operating range is greater (surge to choke margin).
  • 70. Combustor of CCPP • All gas turbine combustors perform the same function; they increase the temperature of the high-pressure gas. • The gas turbine combustor uses very little of its air (10%) in the combustion process. • The rest of the air is used for cooling and mixing. • The new combustors are also used circulating steam for cooling purposes. • The air from the compressor must be diffused before it enters the combustor. • The velocity of the air leaving the compressor is about 122 to 183 (m/sec) and the velocity in the combustor must be maintained below 15.2 (m/sec).
  • 71. Combustor of CCPP • Even at these low velocities care must be taken to avoid the flame to be carried on downstream. • The combustor is a direct-fired air heater in which fuel is burned almost stoichiometrically with one third or less of the compressor discharge air. • Combustion products are then mixed with the remaining air to arrive at a suitable turbine inlet temperature.
  • 72. Combustor of CCPP • Despite the many design differences in combustors, all gas turbine combustion chambers have three features: (1) a recirculation zone, (2) a burning zone (with a recirculation zone, which extends to the dilution region), and (3) a dilution zone. • The air entering a combustor is divided so that the flow is distributed between three major regions: (1) Primary Zone, (2) Dilution Zone, and (3) Annular space between the liner and casing.
  • 73. Combustor of CCPP • Combustor performance is measured by efficiency, the pressure decrease encountered in the combustor, and the evenness of the outlet temperature profile. • The combustion efficiency is a measure of combustion completeness. • The combustion completeness affects fuel consumption directly, since the heating value of any unburned fuel is not used to increase the turbine inlet temperature. • Normal combustion temperatures range from 1871°C to 1927°C.
  • 74. Combustor of CCPP • At this temperature, the volume of nitric oxide in the combustion gas is about 0.01%. • If the combustion temperature is lowered, the amount of nitric oxide is substantially reduced.
  • 75. Gas turbine There are two types of turbine used in gas turbine • I. Axial flow turbine • II. Radial flow turbine
  • 76. Gas turbine • The axial flow turbine, like its counter parts the axial flow compressor, has flow which inter and leaves in the axial direction. • Most axial flow turbine consist of more than one stage: the front stages are usually impulses (zero reaction) and the later stages have about 50% reaction.
  • 77. Gas turbine • The impulses stages produces about twice output of a comparable 50% reaction stage, while the efficiency of an impulses stage is less than that of 50% reaction stages. • The high temperatures that are now available in the turbine section are due to improvements of the metallurgy of the blades in the turbines.
  • 78. Gas turbine • The developments of directionally solidified blades as well as the new single crystal blades, with the new coatings, and the new cooling schemes, are responsible for the increase in firing temperatures. • The high-pressure ratio in the compressor also causes the cooling air used in the first stages of the turbine to be very hot. • The temperatures leaving the gas turbine compressor can reach as high as 649 °C.
  • 79. Gas turbine • Thus, the present cooling schemes need revisiting and the cooling passages are in many cases also coated. • The cooling schemes are limited in the amount of air they can use, before there is a negative effort in overall thermal efficiency due to an increase in the amount of air used in cooling. • The rule of thumb in this area is that if you need more than 8% of the air for cooling we are loosing the advantage from the increase in the firing temperature.
  • 80. Gas turbine • The new gas turbines being designed for the new millennium are investigating the use of steam as a cooling agent for the first and second stages of the turbines. • Steam cooling is possible in the new combined cycle power plants, which is the base of most of the new High Performance Gas Turbines (HPGT).
  • 81. Gas turbine • Steam as part of the cooling as well as part of the cycle power will be used in the new gas turbines in the combined cycle mode. • The injection of about 5% of steam by weight of air amounts to about 12% more power. • The pressure of the injected steam must be at least 4 bar above the compressor discharge. • The way of steam injected must be done very carefully so as to avoid compressor surge. By using the steam cooling the firing temperature reaches upto 1649°C.
  • 82. Gas turbine • Since 1950, turbine bucket material temperature capability has advanced approximately 472°C. • The importance of this increase can be appreciated by noting that an increase of 56°C in turbine firing temperature can provide a corresponding increase of 8–13% in output and 2– 4% improvement in simple-cycle efficiency. • Advances in alloys and processing, while expensive and time-consuming, provide significant incentives through increased power density and improved efficiency.
  • 83. Gas turbine • In the late 1990s, single-crystal blades were introduced in gas turbines. • These blades offer additional creep and fatigue benefits through the elimination of grain boundaries. • In single-crystal material, all grain boundaries are eliminated from the material structure and a single crystal with controlled orientation is produced in an airfoil shape.
  • 84. Gas turbine • By eliminating all grain boundaries and the associated grain boundary strengthening additives, a substantial increase in the melting point of the alloy can be achieved, thus providing a corresponding increase in high-temperature strength. • The transverse creep and fatigue strength is increased, compared to equiaxed or DS structures. • The advantage of single-crystal alloys compared to equiaxed and DS alloys in low-cycle fatigue (LCF) life is increased by about 10%.
  • 85. Coatings • There are three basic types of coatings: thermal barrier coatings, diffusion coatings, and plasma sprayed coatings. • The advancements in coating have also been essential in ensuring that the blade base metal is protected at these high temperatures. • Coatings ensure that the life of the blades is extended and in many cases are used as sacrificial layers, which can be stripped and recoated.
  • 86. Coatings • The life of a coating depends on composition, thickness, and the standard of evenness to which it has been deposited. • The general type of coatings is little different from the coatings used 10-15 years ago. • These include various types of diffusion coatings such as aluminide coatings originally developed nearly 40 years ago.
  • 87. Coatings • The thickness required is between 25–75 μm thick. • The new aluminide coatings with platinum increase the oxidation resistance, and also the corrosion resistance. • The thermal barrier coatings have an insulation layer of 100–300 μm thick, are based on ZrO2- Y2O3, and can reduce metal temperatures by 50°C–150°C. • This type of coating is used in combustion cans, transition pieces, nozzle guide vanes, and also blade platforms.
  • 88. Heat recovery steam generator (HRSG) • The gas turbine exhaust gases enter the Heat Recovery Steam Generator (HRSG), where the energy is transferred to the water to produce steam. • There are many different configurations of the HRSG units. • Most HRSG units are divided into the same amount of sections as the steam turbine. • In most cases, each section of the HRSG has a Pre- heater, an Economizer and Feed-water, and then a Super heater. • The steam entering in the steam turbine is superheated.
  • 89. Heat recovery steam generator (HRSG) • The most common type of an HRSG in a large Combined Cycle Power plant is the drum type HRSG with forced circulation. • These types of HRSGs are vertical; the exhaust gas flow is vertical with horizontal tube bundles suspended in the steel structure. • The steel structure of the HRSG supports the drums.
  • 90. Heat recovery steam generator (HRSG) • In a forced circulation HRSG, then the steam water mixture is circulated through evaporator tubes using a pump. • These pumps increase the parasitic load and thus detract from the cycle efficiency. • In this type of HRSG the heat transfer tubes are horizontal, suspended from un-cooled tube supports located in the hot gas path. • Some vertical HRSGs are designed with evaporators, which operate without the use of circulation pumps.
  • 91. Multipressure Steam Generators • These are becoming increasingly popular. • With a single pressure boiler, there is a limit to the heat recovery because the exhaust gas temperature cannot be reduced below the steam saturation temperature. • This problem is avoided by the use of multipressure levels.
  • 92. Pinch Point • This is defined as the difference between the exhaust gas temperature leaving the evaporator section and the saturation temperature of the steam. • Ideally, the lower the pinch point, the more heat recovered, but this calls for more surface area and, consequently, increases the backpressure and cost.
  • 93. Pinch Point • Also, excessively low pinch points can mean inadequate steam production if the exhaust gas is low in energy (low mass flow or low exhaust gas temperature). • General guidelines call for a pinch point of 8°C–22°C. • The final choice is obviously based on economic considerations.
  • 94. Approach Temperature • This is defined as the difference between the saturation temperatures of the steam and the inlet water. • Lowering the approach temperature can result in increased steam production, but at increased cost. • Conservatively high-approach temperatures ensure that no steam generation takes place in the economizer. • Typically, approach temperatures are in the 5.5°C –11°C range.
  • 95. Gas turbine Design considerations • The two factors, which most affect high turbine efficiencies, are pressure ratios and temperature. • The axial-flow compressor, which produces the high-pressure gas in the turbine, has seen dramatic change as the gas turbine pressure ratio has increased from 7:1 to 40:1. • The increase in pressure ratio increases the gas turbine thermal efficiency when accompanied with the increase in turbine firing temperature.
  • 96. Gas turbine Design considerations • The increase in the pressure ratio increases the overall efficiency at a given temperature, however increasing the pressure ratio beyond a certain value at any given firing temperature can actually result in lowering the overall cycle efficiency. • It should also be noted that the very high- pressure ratios tend to reduce the operating range of the turbine compressor.
  • 97. Gas turbine Design considerations • This causes the turbine compressor to be much more intolerant to dirt build-up in the inlet air filter and on the compressor blades and creates large drops in cycle efficiency and performance. • In some cases, it can lead to compressor surge, which in turn can lead to a flame out, or even serious damage and failure of the compressor blades and the radial and thrust bearings of the gas turbine.
  • 98. Gas turbine Design considerations • The effect of firing temperature is very predominant—for every 55.5°C increase in temperature, the work output increases approximately 10% and gives about a 1.5% increase in efficiency. • Higher-pressure ratios and turbine inlet temperatures improve efficiencies on the simple-cycle gas turbine.
  • 99. Gas turbine Design considerations • The latest frame type unit introduce are 480 MW units using steam cooling in combined cycle mode, enabling the firing temperature to reach 1427°C. • This enables efficiency in the combined cycle mode to reach more than 60% in the area of performance; the steam turbine power plants have an efficiency of about 35%, as compared to combined cycle power plants, which have an efficiency of about 55%.
  • 100. Gas turbine Design considerations • Newer Gas Turbine technology will make combined cycle efficiencies range between 60–65%. • As a rule of thumb a 1% increase in efficiency could mean that 3.3% more capital can be invested. • However one must be careful that the increase in efficiency does not lead to a decrease in availability.
  • 101. Gas turbine Design considerations • It can be seen from literature the growth in efficiency of about 10% and a loss in availability of about 10%. • This trend must be turned around since many analyses show that a 1% drop in the availability needs about a 2–3% increase in efficiency to offset that loss.
  • 102. Gas turbine Design considerations • The time taken to install a steam plant from conception to production is about 42–60 months as compared to 22–36 months for combined cycle power plants. • actual construction time is about 18 months, while environmental permits in many cases take 12 months and engineering 6–12 months.
  • 103. Gas turbine Design considerations • The time taken for bringing the plant online affects the economics of the plant, the longer capital is employed without return, the plant accumulates interest, insurance, and taxes. • It is obvious from this that as long as natural gas or diesel fuel is available the choice of combined cycle power plants is obvious.