et 2008 steam circulation system
TRANSCRIPT
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STEAM CIRCULATIONSTEAM CIRCULATION
SYSTEMSYSTEM
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Steam circuit diagramSuper HeaterDe-super heater /
AttemperatorRe-heaterIBR
Super Critical Boiler
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Pendant typeHorizontal type
Radiant SuperheaterConvectionSuperheaterCombined
Superheater
Types of SuperHeaters
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M.S
FROM F.R.S
Sh 1Sh 1
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M.S
FROM F.R.S
SH 2SH 2
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M.S
FRM F.R.S
LTSHLTSH
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M.S
FROM F.R.S
Final SHFinal SH
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M.S
H.
R.
HC.R.H
FROM F.R.S
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Super heater heats the high-
pressure steam from itssaturation temperature to ahigher specified temperature.
Super heaters are often dividedinto more than one stage.
Super heaters
Super heater heats the high-
pressure steam from itssaturation temperature to ahigher specified temperature.
Super heaters are often dividedinto more than one stage.
Super heater heats the
high-pressure steamfrom its saturationtemperature to a
higher specifiedtemperature.
Super heaters are oftendivided into more than
Super heater heats thehigh-pressure steam
from its saturationtemperature to a higherspecified temperature.
Super heaters are oftendivided into more thanone stage.
Super heater heats thehigh-pressure steamfrom its saturation
temperature to ahigher specifiedtemperature.
Super heaters are oftendivided into more than
one stage.
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Transfer of EnergyTransfer of Energy
Hot Flue
GasThermal Structure
SH
Steam
Convection &
Radiation HT
Convection HT
Drop in Enthalpy
of Flue Gas
Rise in Enthalpy of
Steam
Mechanism of Heat Transfer
Source/Supply Thermal Structure Sink /Demand
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Mechanism of Heat Transfer :Mechanism of Heat Transfer :
Rate of heat transfer from hot gas toRate of heat transfer from hot gas to
cold steam is proportional to:cold steam is proportional to:
Surface area of heat transferSurface area of heat transfer
Mean Temperature differenceMean Temperature differencebetween Hot Gas and Cold Steam.between Hot Gas and Cold Steam.
Thot gas,in
Tcold steam,in
Thot gas,out
Tcold steam,out
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Thot gas,in
Tcold steam,in
Thot gas,out
Tcold steam,out
Thot gas,in
Tcold steam,in
Thot gas,out
Tcold steam,out
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Mechanism of Heat Transfer :Mechanism of Heat Transfer :
Rate of heat transfer from hot gas toRate of heat transfer from hot gas to
cold steam is proportional to:cold steam is proportional to:
Surface area of heat transferSurface area of heat transfer
Mean Temperature differenceMean Temperature differencebetween Hot Gas and Cold Steam.between Hot Gas and Cold Steam.
Thot gas,in
Tcold steam,in
Thot gas,out
Tcold steam,out
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Platen SuperheaterPlaten Superheater Platen Superheater : FlatPlaten Superheater : Flat
panels of tubes located in thepanels of tubes located in theupper part of the furnace,upper part of the furnace,
where the gas temperature iswhere the gas temperature is
high.high.
The tubes of the platen SHThe tubes of the platen SH
receive very high radiation asreceive very high radiation aswell as a heavy dust burden.well as a heavy dust burden.
Mechanism of HT : HighMechanism of HT : High
Radiation & Low convectionRadiation & Low convection
Thermal Structure:Thermal Structure:
No. of platensNo. of platens No. of tubes in a platenNo. of tubes in a platen
Dia of a tubeDia of a tube
Length of a tubeLength of a tube
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Geometry of Thermal Structure :Geometry of Thermal Structure :
Platen SHPlaten SH
The outer diameter of platen SH isThe outer diameter of platen SH is
in the range of 32 42 mm.in the range of 32 42 mm.
The platens are usually widelyThe platens are usually widely
spaced, Sspaced, S11 = 500 900 mm.= 500 900 mm. The number of parallel tubes in aThe number of parallel tubes in a
platen is in the range of 15 35.platen is in the range of 15 35.
Design Constraints: Max. allowableDesign Constraints: Max. allowable
steam flow rates.steam flow rates.
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WAYS TO IMPROVEWAYS TO IMPROVE
EFFICIENCYEFFICIENCY
SUPERHEATINGSUPERHEATING
REHEATINGREHEATING
REGENERATIONREGENERATION
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REHEATING
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Rankine Cycle Efficiency
net workn = --------------
Qin
Cycle thermal efficiency is improved by increasing the
mean temperature of heat addition process. This
temperature is increased because the boiler inletpressure sets the saturation temperature in Rankine
cycle.
Total fuel input
Heat Rate =------------------
Electrical generation (KW)
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It effects improvement andIt effects improvement and
economy in the following wayseconomy in the following ways
It increases capacity of plant.It increases capacity of plant.
It eliminates errosion of the lastIt eliminates errosion of the last
stage of the turbine.stage of the turbine.
It reduces the steamIt reduces the steam
consumption of the turbine.consumption of the turbine.
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Horizontal SuperheaterHorizontal Superheater
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How it increases efficiency?How it increases efficiency?
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Rankine Cycle Efficiency
net workn = --------------
Qin
Cycle thermal efficiency is improved by increasing the
mean temperature of heat addition process. This
temperature is increased because the boiler inletpressure sets the saturation temperature in Rankine
cycle.
Total fuel input
Heat Rate =------------------
Electrical generation (KW)
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Superheated cycleSuperheated cycle
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Based on the position of headerBased on the position of header
1.Vertical superheater.1.Vertical superheater.2.Horizontal superheater.2.Horizontal superheater.
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Based on heat receiving capacityBased on heat receiving capacity
Convective superheaterConvective superheater
Radiant superheaterRadiant superheater
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STEAM OUTLETSTEAM OUTLET
TEMPERATURETEMPERATURE
RESPONSE OFRESPONSE OFDIFFERENTDIFFERENT
SUPRHEATERSSUPRHEATERS
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Radiant SH & Convective SH each hasRadiant SH & Convective SH each has
different steam outlet temp response.different steam outlet temp response.
As demand for steam increases withAs demand for steam increases with
increase in load, fuel and airflow andincrease in load, fuel and airflow and
hence combustion gas flow arehence combustion gas flow areincreased.increased.
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Load response of SHLoad response of SH
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In CSH heat transfer co-efficient (Hi&Ho)In CSH heat transfer co-efficient (Hi&Ho)
increases both outside & inside due toincreases both outside & inside due toincrease in gas flow rate and increase inincrease in gas flow rate and increase in
steam flow rate respectively.steam flow rate respectively.
In case of RSH since furnace temperatureIn case of RSH since furnace temperatureand hence the amount of available heatand hence the amount of available heat
from radiation does not rise as rapidly asfrom radiation does not rise as rapidly as
the steam flow rate it has fallingthe steam flow rate it has fallingcharacteristic.characteristic.
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In CSH steam O/T Temp.In CSH steam O/T Temp.
increases with incease in steamincreases with incease in steam
flow rate while in RSH itflow rate while in RSH it
decreases with steam flow rate.decreases with steam flow rate. Hence combination of RSHHence combination of RSH
&CSH is used in series which&CSH is used in series which
gives a relatevely flat curve forgives a relatevely flat curve forsteam O/T temp. and is thussteam O/T temp. and is thus
insensetive to load change.insensetive to load change.
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Basically the control of temperature is to protect the
superheater by preventing the metal temperatures
reaching a dangerously high level reducing mechanical
strength and leading to failure. Water flowing through atube conducts heat away much more effectively than
steam due to its higher specific heat capacity. This
means that tubes carrying water have a metal
temperature much closer to the fluid passing through it.
For superheat temperatures alloys of chromemolybdenum steels are used (upto 560oC)
Superheat temperature control is therefore fitted to
ensure superheat temperature does not exceed design
limits
Superheater Temperature Control
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Reheater and DesuperheaterReheater and Desuperheater
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Reheat pressure for optimumReheat pressure for optimum
efficiencyefficiency
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Reheater in 500 MW plantReheater in 500 MW plant
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M.S
FROM F.R.S
RHRH
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CRHCRHpressure 43.5 KSCpressure 43.5 KSC
temperature 340temperature 340 CC
HRHHRHpressure 41.5 KSCpressure 41.5 KSC
temperature 535temperature 535 CC
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ATTEMPERATIONATTEMPERATION
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What is the purpose of attemperation andWhat is the purpose of attemperation and
its location in power plant?its location in power plant?
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Direct contact DesuperheaterDirect contact Desuperheater
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Enthalpy
538
Expansion Line
170 kg/cm2
240 kg/cm2
Condensation
EFFECT OF SUPERCRITICAL PARAMETERSEFFECT OF SUPERCRITICAL PARAMETERS
Critical Point 225 kg/cm2
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Enhancements
Plant efficiency 0.69% to 1.64%Fuel tolerance More tolerant to
coal quality changes
Reductions
Coal Consumption
Ash productionCO2
SO2
Nox
Improvements
Startup timeSliding Pressure Operation
Load following capability
SUPERCRITICAL ADVANTAGESSUPERCRITICAL ADVANTAGES
SELECTEDPARAMETERS
MSP 246 kg/cm2
MST 538 0C
RST 566 0C
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Sliding pressure V/s Constant pressure
In sliding operation, turbine inlet valves
remains fully open during normal
operation. As a result the live.
Advatages
lower thermal stresses
The control range of the reheater final
steam is extended.
Reduce pressure level at low loads prolong
the life span of plant components.
Overall reduction in power consumption
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Type Supercritical, suitable for variable pressure operation with spiralor rifled/plain water wall tubing Tower type or two pass type
Rating Flow (T/Hr) Temperature Deg CPressureKg/Cm2(a)
At SH Outlet 2225 540 256
At RH Outlet 1740 568 52.0
Flue gas temperature at air-heater outlet- 125 Deg C
Fuel GCV range 3000 to 4000 Kcal/kg with 10-16% moisture and 32 to 48%ash
Start upsystem
Start up system with one no. circulating pump is with alternate drainflow to condenser through flash tank .
Salient Features of the Steam Generator
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Indian Boiler Regulations
Scope (cover regulations on): Electric-Resistance-Welded
Steel Boiler And Super-Heater
Tubes
Boiler Tubes Subject To External
Pressure The Working Pressure To Be
Allowed On Various Parts Of
Boilers
Welded And Seamless ForgedDrums For Water Tube Boilers
And Super Heaters Requisite Mountings, Fittings
and Auxiliaries
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Boiler And Super Heater
Tubes, Headers And Other
Pressure Parts TubesSteam-Pipes And Fittings
Registration Of Boilers And
Inspection Of BoilersSafety Of Persons Inside
BoilersQualification Tests For
Welders Engaged In Welding
Of Boilers