energy conservation in steam turbine
TRANSCRIPT
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ENERGY
CONSERVATION INSTEAM TURBINE CYCLE
Presented ByM.V.Pande
Dy.Director
NPTI, Nagpur
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Costing of Thermal Power Generation
The fuel consumption can bereasonably brought down byconservation techniques
Major cost is fuel cost inthermal power generation
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210 MW KWU Steam Turbine Steam & Water Cycle
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Steam Cycle For 210 Mw Unit
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Principles Of Cycle Efficiency Improvement
Superheated or dry steam should not enter
into condenser
Wetness of steam at turbine exhaust should
not exceed 12%
Maximum possible temperatures at SH & RH
outlet are used,however, restricted due to
metallurgical constraints 560 0C
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The mean temperature of heat addition inboiler should be as high as possible so as to
approach Carnot cycle process
The temperature of heat rejection should belowest possible to reduce heat rejection to
condenser
The throttling across turbine Stop & ControlValves Should be minimum
Principles Of Cycle Efficiency Improvement
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500 MW Turbine Generator Unit
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210 MW Utility Steam Turbine
HP Turbine
IP Turbine
LP Turbine
Foundation
Gen.EndBearing
Condenser
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Barrel Type HP Turbine
BalancePiston
MovingBlades
Barrel Casing
Inner Casing
Gland
SteamInlet
Steam Exhaust
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Reaction Type KWU HP Turbine Rotor
Impulse-Reaction Type HPT Rotor KWU LP Turbine Rotor
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Thermal Process Losses
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Turbine Cycle Losses
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Controllable Plant Parameters
M.S. & R.H. Steam Temperatures
M.S. Steam Pressure
Condenser Vacuum
Final Feed Water Temperature
DP Across Feed Regulation Station
Auxiliary Power Consumption
Make Up Water Consumption
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Description Effect on Effect onTG HR KW
1% HPT Efficiency 0.16% 0.3%
1% IPT Efficiency 0.16% 0.16%
1% LPT Efficiency 0.5 % 0.5 %
Impact of Turbine Cylinder Efficiency onHR/Output
FOLLOW TEST CODES
ASME PTC - 6 For Steam Turbines
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Effect Of Steam Parameters
Effect of Changing Reheat Pressure Effect of Changing Reheat Temp.
SS
HH
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Comparison of Actual Expansion
with Isentropic Expansion in Turbine
Actual Expansion in HP, IP & LP
Cylinder
ActualProcess
1-2-3-4-5
Turbine Heat Rate & Efficiency Evaluation
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Turbine Cycle Efficiency =860
Heat RateX 100
Turbine Heat Rate = Q1 x (H1 h2) + Q2 X (H3
H2)
Gross Generator Output
Actual Heat DropCylinder Efficiency = ------------------------------ x 100
Isentropic Heat Drop
Turbine Heat Rate & Efficiency Evaluation
kCal/ kWh
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18Heat Rate Characteristics withCondenser Exhaust Pressure
Variation of Heat Rate with Load
Turbine Heat Rate Variation
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Turbine Efficiency Evaluation Data
Kcal/kg/oK
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Turbine Performance Monitoring
Indicators of Reduced Performance - Increase of turbine inlet Steam pressure
- High exhaust steam temperature
- Gland steam supply header leak-off
valve opening increased
- Increase of condenser back pressure
- Higher MS flow at rated load
- Increasing trend of bearing oil temperaturesat outlet
- Axial shift on higher side
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Steam Turbine Heat Consumption Test
These tests are conducted for acceptancepurpose or for routine assessment of turbineperformance
The objective of test is to determine requiredheat input to the turbine for an output on themachine
The heat rate is calculated from the data &compared with optimum
The tests are conducted at 40%,60%,80% &100% load
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Heat Consumption vs Load
7% forthrottle
governed
machines
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Cylinder Efficiency Factors
Cylinder Efficiency depends on
Internal Losses occurring in the steam
flow path inside the turbine + ExternalLosses of steam through Glands &
Mechanical Power Transmission Losses
Cylinder efficiency varies from 85 90%
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Internal Losses of Turbine
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Wetness Loss
This loss is incurred by moisture entrained inthe low pressure steam towards exhauststages of turbine
This reduces the efficiency due to absorptionof energy by water droplets
The result is the erosion of leading edges of
blades particularly at the tip Erosion cause the inlet blade angle to change
& prevents tangential entry of steam
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IPT & LPT Blade Erosion Due To Moisture
IPT Last Stage Moving
Blades
LPT Last Stage MovingBlades
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LPT Exhaust Losses
Residual Velocity or Leaving Loss
- This loss is due to exhaust velocity of steam
Leaving Loss=Ve2/2 J/Kg- This loss is reduced by increasing the laststage blade heights
Exhaust Hood Loss- This loss is due to the turning of steamthrough 900 to enter the condenser. Loss is
reduced by providing Diffusers at the exhaust
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KWU Turbine LPT Inner Top-Half Casing
Diffuser
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Effect of Reheater Spray
Reduction of cycle efficiency due to
fresh steam bypassing the HP turbine
Reduction of power output from HPturbine due to reduction of steam flow
through HP turbine
Higher Silica deposition in IP & LPturbine
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Effects of Silica Deposition on Turbine
Silica deposition causes the passage
areas between blades to progressively
reduce Increases the first stage pressure of
turbine progressively
The Cylinder efficiency is reduced
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Remedies To Reduce Silica Deposition
Do not raise the boiler
pressure until Silica level is
normal
Give Blow down as required
Minimum use of superheater
& reheater spray
Steam washing of turbine by
wet steam at low speeds
Silica in Steam with Boiler Pressure
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Feed Heaters Survey
Feed heaters survey evaluate the performance of heaters & predicts the
deterioration causes
Following parameters are noted down
- Steam pressure at heater
- Steam temperature at heater
- Feed water inlet & outlet temperature- Heater drain temperature
Evaluate the steam flow to each heater by heat balance
Compare the flow values with optimum
Calculate T.T.D. for each heater
The results indicate following problems
- The elevated TTDs on the heater train suggests water side
contamination (oil)
- The high steam flow to particular heater may be due to lower feed
water inlet temperature, suggesting the problem in previous heater
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Turbine Pressure Survey
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Optimum Condenser Back Pressure
It is a misconception that minimum backpressure should be maintained at all loads
The lower back pressure is justified only if the
efficiency gain due to this is greater than
power consumption of CW pumps & coolingtower fans
With the reduction in condenser back pr. the
isentropic heat drop across the last stage
increases & so additional work is done in the
turbine
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Effect of lower exhaust pr.
Volumetric flow rate increases ( high
specific volume of steam),giving rise to
more Leaving Losses
Wetness Loss increases
CW pumping power increases
Optimum Condenser Back Pressure
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36Optimum Back Pressure at
Full Load
Hence to overcome
above problems
optimum vacuum as
shown in graph is
maintained
Optimum Condenser Back Pressure
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External Losses of Turbine
Shaft & Gland leakage loss
-Steam leakage through labyrinth sealing
at the turbine shaft end,which is about3% of total steam flow. Loss increases insquare proportion with increase inlabyrinth clearances
Journal & Thrust Bearing losses
Governor & oil pump loss
KWU HP Turbine Rotor
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KWU HP Turbine RotorAdmission Side Sealing
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Sliding Pressure Operation at Part Loads
In sliding pressure operation,the controlvalves are kept wide open & the pressurebefore the stop valves is varied through boiler
to achieve required part load This reduces throttling losses across control
valves
The initial temperature is maintained atreduced pressure unlike throttling process
The net effect is to improve cycle efficiencyas compared to constant pressure operation
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Heat Saving By Sliding Pressure Operation
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Effect On Heat Rate For ParameterDeviation (500 MW Unit)
DEVIATION IN PARAMETER EFFECT ON HEATRATE (KCAL/KWH)
1. HPT inlet press. by 5.0 ata 6.25
2. HPT inlet temperature by 10.0 deg C 6.0
3. IPT inlet temperature by 10.0 deg C 5.6
4. Condenser pressure by 10.0 mm of
Hg
9.0
5. Re spray water quantity by 1.0% 4.0
6. HPT Cylinder efficiency by 1.0% 3.5
7. IPT Cylinder efficiency by 1.0% 4.0
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