Project report of kota super thermal power plant

A
Practical Training Report
On
KOTA SUPER THERMAL POWER STATION
Submitted in partial fulfillment for the award of the degree of
BACHELOR OF TECHNOLOGY
In
Electrical Engineering
2013-2014
(01 June 2013- 30 June 2013)
Submitted to: - Submitted by: -
Mr. Nutan Paliwal Himanshu Derwal
Lecturer, 10EDAEE020
Electrical Engineering B.Tech. IV Yr. VII Sem
RAJASTHAN TECHNICAL UNIVERSITY, KOTA
DEPARTMENT OF ELECTRICAL ENGINEERING
ANAND INTERNATIONAL COLLEGE OF ENGINEERING

ii
PREFACE
A student gets theoretical knowledge from classroom and gets practical knowledge from
industrial training. When these two aspects of theoretical knowledge and practical experience
together then a student is full equipped to secure his best.
In conducting the project study in an industry, students get exposed and have
knowledge of real situation in the work field and gains experience from them. The object of the
summer training cum project is to provide an opportunity to experience the practical aspect of
Technology in any organization. It provides a chance to get the feel of the organization and its
function.
The fact that thermal energy is the major source of power generation itself shows the
importance of thermal power generation in India – more than 60 percent of electric power is
produced by steam plant in India.
In steam power plants, the heat of combustion of fossil fuels is utilized by the boilers
to raise steam at high pressure and temperature. The steam so produced is used in driving
the steam turbine coupled to generators and thus in generating ELECTRICAL ENERGY

iii
ACKNOWLEDGEMENT
It is a matter of great pleasure and privilege for me to present this report of 30 days
on the basis of practical knowledge gained by me during practical training at KOTA SUPER
THERMAL POWER STATION (K.S.T.P.S.), KOTA (Rajasthan) during session 2012-2013.
I with full pleasure converge my heartiest thanks to Head of Electrical Department,
Mr. Virendra Sangtani, Anand International College Of Engineering and to my guide Mr.
Nutan Paliwal, Assistant Professor, Department of Electrical Engineering.
I am also grateful to Er. S.C.Madan & Er. G.K.Rathi to support me at each and
every step of my training Schedule. I attribute hearties thanks to all Engineering departments
and Engineers for their Ample Guidance during my training period.
Himanshu derwal

iv
FIGURE LIST
Figure 1.1
Figure
VIEW OF KOTA SUPER THERMAL POWER PLANT
Page No
04
Figure 2.1 LAYOUT OF POWER PLANT 05
Figure 2.2 CROSS SECTIONAL VIEW OF FOUR MAJOR PART 07
Figure 3.1 WAGON TRIPLER 09
Figure 4.1 CROSS SECTIONAL VIEW OF ASH HANDLING PLANT 14
Figure 6.1 CROSS SECTIONAL VIEW OF FURNANCE 18
Figure 6.2 PULVERISED SYSTEM 19
Figure 6.3 CROSS SECTIONAL VIEW OF STEAM DRUM 21
Figure 6.4 ECONOMIZER 23
Figure 6.5 AIR PRE-HEATER 24
Figure 7.1 STEAM TURBINE 29
Figure 8.1 CROSS SECTIONAL VIEW OF TURBO GENERATOR 40
Figure 9.1 HYDROGEN COOLED ALTERNATOR 42
Figure 12.1 CROSS SECTIONAL VIEW OF CONTROL ROOM 50

v
CONTENTS
Title Page No
CHAPTER 1 INTRODUCTION………………………………….………... 1-4
1.1 DESIGN OF K.S.T.P.S. ……………………..... 3
1.2 SITE SELECTION CRITERIA………………….. 3
1.3 DESIGN FEATURES………………………....... 4
CHAPTER 2 GENERAL LAYOUT AND BASIC IDEA………………... 5-7
2.1 FUEL AND ASH CIRCUIT………………………. 6
2.2 AIR AND GAS CIRCUIT………………………… 6
2.3 FEED WATER AND STEAM CIRCUIT………… 6
2.4 COOLING WATER CIRCUIT…………….......... 7
CHAPTER 3 COAL HANDLING PLANT……………………………….. 8 -11
3.1 WAGON UNLOADING SYSTEM……………… 8
3.2 CRUSHING SYSTEM………………………….. 10
3.3 CONSTRUCTION AND OPERATION………… 10
3.4 CONVEYING SYSTEM…………………………. 11
3.5 CONVEYOR BELT SPECIFICATION………….. 11
CHAPTER 4 ASH HANDLING PLANT…………………………........... 12-14
4.1 FUEL AND ASH PLANT………………………….. 12
4.2 AIR AND GAS PLANT……………………………. 12
4.3 ASH AND DUST COLLECTION PLANT………… 13
4.4 UTILISATION……………………………………….. 13
CHAPTER 5 ELECTRO-STATIC PRECIPITATOR…………………….. 15-16
5.1 PRINCIPLE OF OPERATION…………………… 15

vi
5.2 CONTROLLER…………………………………… 15
` 5.3 HIGH VOLTAGE RECTIFIER TRANSFORMER… 16
5.4 E.S.P. FIELD……………………………………... 16
CHAPTER 6 BOILER…………………………………………………… 17-28
6.1 BOILER CLASSIFICATION………………….. 17
6.2 FURNANCE…………………………………… 18
6.3 PULVERISED FUEL SYSTEM……………… 19
6.4 FUEL OIL SYSTEM………………………….. 19
6.5 BOILER DRUM……………………………….. 20
6.6 DRAFT SYSTEM…………………………….. 22
6.7 DRAUGHT FAN………………………………. 22
6.8 ECONOMIZER………………………………. . 23
6.9 AIR-PREHEATER……………………………. 23
6.10 SUPERHEATER……………………………. 24
6.11 REHEATER…………………………………. 25
6.12 CIRCULATION SYSYTEM………………... 25
6.13 SOOT BLOWER……………………………. 26
6.14 TECHNICAL SPECIFICATION OF BOILER... 26
CHAPTER 7 STEAM TURBINE………………………………………… 29-32
7.1 PRINCIPLE …………………………………… 30
7.2 DESCRIPTION OF STEAM TURBINE……… 31
CHAPTER 8 TURBO GENERATOR……………………………………. 33-40
8.1 THEORY………………………………………. 33
8.2 ROTOR……………………………………….. 37
CHAPTER 9 COOLING SYSTEM……………………………………… 41-42
9.1 INTRODUCTION………………………………. 41
9.2 HYDROGEN DRYER………………………… 41

vii
CHAPTER 10 EXCITATION SYSTEM…………………………………. 43-45
10.1 FUNCTION OF EXCITATION SYSTEM…… 43
10.2 TYPES OF EXCITATION SYSTEM………… 43
10.3 STATIC EXCITATION SYSTEM……………. 43
10.4 GENERAL ARRANGEMENT……………….. 44
CHAPTER 11 WATER TREATMENT PLANT…………………………. 46- 47
11.1 D.M. PLANT……………………………………… 46
11.2 C.W. PLANT……………………………………… 47
11.3 B.C.W PUMP HOUSE…………………………… 47
CHAPTER 12 CONTROL ROOM……………………………………….. 48-50
12.1 MAIN CONTROL ROOM…………………………. 48
12.2 CONTROL PANEL I……………………………… 49
12.3 CONTROL PANEL II…………………………… 49
12.4 CONTROL PANEL III……………………………. 49
12.5 CONTROL PANEL IV……………………………. 50
12.6 CONTROL PANEL V……………………………. 50
CHAPTER 13 PROTECTIONS………………………………………. 51
13.1 GENERAL PROTECTION……………………… 51
CHAPTER 14 SALIENT FEATURES OF K.S.T.P.S……………………. 52-53
14.1 LOCATION……………………………………….. 52
14.2 CAPACITY………………………………………… 52
14.3 SOURCE OF WATER…………………………….. 52
14.4 BOILER……………………………………………. 52
14.5 FUELS……………………………………………… 53
CONCLUSIONS ……………………………………….………………………. 54
REFERENCES ………………...………………………………………........... 55

[1 ]
CHAPTER -1
INTRODUCTION
For the power generation with 2x110 MW, 2x195 MW and 3x210 MW of K.T.P.S.
authorities are required to be operative to active full operation. The auxiliaries are
basically operation either on L.T. System i.e. 415 V 3 Ø power supply is made available to
the system after providing the station transformer of 3x50 MVA capacity with voltage 220
KV/ 7.2/7.2 KV & different service transformers of capacity 1.0 MVA, 1.5 MVA, 2.0 MVA,
which are located near the load centre as the transformer having the voltage of 6.6 KV
/415 V. The 6.6 KV power is distributed through 6.6 KV interconnected Bus System for all
the Seven units with a control through DC of 220 V.
The 415 V power supply is done through a L.T. SWGR (Switchgear) which are
located nearby the distribution transformer as well as the load centers. The all in -comers,
which are breaker controlled, are having the control the L.T. SWGR are having the control
system on 110/ 220 V AC. The 6.6 KV power supply which are either MOCB (Minimum Oil
Circuit Breaker) of JYOTI MAKE or Air Circuit Breakers.
The 6.6 KV power supply to various draining equipment’s i.e. more is made
through breakers which are either MOCB of Jyoti make air circuit breaker which are either
of voltage makers as well as SF 6 of NGEF make. The LT supply is also controlled
through air break circuit breaker, which is either L&T make or English Electric Company
of India. The various H.T. motors are switched on / started through on direct ON line
(DOL) in order to inverse the availability of equipment at full efficiency without time gap.
Further , the 6.6 KV system which is normally in delta configuration and terms as an
unearthed system so also to keep the running motor complete in operating condition in
case of anyone .phase of motor winding is earthed due to any one reason. Earthling is
detected by an protection system with alarm facility to take remedial measures
immediately and at the same time to maintain the generation level in the same condition,
prior to occurring the earth fault the single phase earth fault is detected in due course till
the motor is not earthed to other or another phase.

[2 ]
“PUBLIC ADDRESS SYSTEM” is available through in area of each unit which helps
in fast communication for prompt remedial measure.
Soot Blowers are there in the boiler area on the furnace side or Zone which helps in
blowing the soot / ash deposition regularly of the furnace wall / economizer tubes to keep
heat transfer at the required parameter.
In April 1973, Central Electricity Authority prepared a Project Report for power
station comprising of the two units of each of capacity 110 MW for RSEB subsequently in
September, 1975 this was revised by the Consultant Thermal Design Organization ,
Central Electricity Authority for invention of 2x110 MW units being manufactured by BHEL,
Hyderabad in 1st
Stage.
The planning commission cleared the project report in Sept., 1976 for installation of
two units each of 110 MW in first estimated cost of Rs. 143 Crores.
There are total 11 lines coming from KSTPS each having 220V over it. Each line is going
as
1 line Sanganer
1line Herapura
1line Modak gss
2lines Power grid nawta
2lines Byawar
4 lines Sakatpura gss

[3 ]
1.1.1 ENVIROUNMENTAL PROFILE
 Adequate measures have been taken at ktps to control pollution and comply to the norms
laid by environment protection act. 1986. being a power station, located in the heart of kota
city, continuous efforts are made to ensure atmospheric emission of suspended particulate
matter within the prescribed limits.
 180 meter high stacks have been provided to release flue gases into the atmosphere at an
approx. velocity of 25 m/sec. so as to disperse the emitted particulate matter over a wide
spread area.
 The on-line stack spm monitoring system of codel germany has been installed as per
requirement of central pollution control board.
 Microprocessor based intelligent controllers to optimize the esp of 99.82% efficiency have
been provided. esps of 110 mw units # 1 & 2 were augmented under r&m scheme with
installation of 7 additional field to enhance efficiency upto 99.82%. dummy fields provided in
esp of 210 mw units # 3 & 4 were also filled in with installation of 7th field as such the
efficiency has increased upto 99.84%.
 Adequate water spraying arrangements have been provided at coal unloading, transfer
and conveying system to arrest and restrict fugitive emission. the system is now further
upgraded with latest technology.
 Development of green belt, about 3 lakhs plants of various species have already been
planted in kstps and ash dyke. the survival rate of plants is watched periodically.
*existing green cover area within plant - 90 hect.
*existing green cover area within ash dyke - 100 hect.
 Regular monitoring of stack emission, ambient air quality and trade effluent is carried out.
 All the drains in the esp area and boiler area have been diverted to dedicated tanks and
the effluent collected is utilized for transportation of bottom ash disposal of the various units.
1.1.2 K.S.T.P.S. IS DESISIGNED IN FOLLOWING STAGES:-
 STAGE I - 2x110 MW
 STAGE II - 2X210 MW
 STAGE III - 1X210 MW


STAGE IV
STAGE V
- 1X195 MW
- 1X195MW
Total Power Generation - 1240 MW*

[4 ]
1.2 SITE SELECTION CRITERIA
1.2.1 LOCATION:-
The Kota Thermal Power Station is ideally on the left bank of
Chambal River at Up Stream of Kota Barrage. The large expanse of water reached by the
barrage provides an efficient direct circulation of cooling system for the power station. The
220 KV GSS is within ½ Kms. from the power station.
1.2.2 LAND:-
Land measuring approx. 250 hectares was required for the project in 1976,
For disposal of ash tank very near to power station is acquired which the ash in slurry form
is disposed off through ash and slurry disposal plants.
1.2.3 COAL:-
Coal India limited owns and operates all the major coal fields in India
through its coal producing subsidiary companies viz. Northern Coal Fields Limited, South
Eastern Coal Fields Limited, Coal India limited is supply coal from its coal mines of coal
producing subsidiaries SECL & NCL to Kota Thermal Power Station through railway
wagons. The average distances of SECL, NCL are 800, 950 Kms. respectively.
1.2.4 WATER:-
The source of water for power station is reservoir formed by Kota Barrage
on the Chambal River. In case of large capacity plants huge quantities of coal and water
is required. The cost of transporting coal and water is particularly high. Therefore, as far

[5 ]
as possible, the plant must be located near the pit rather than at load centre for load
above 200 MW and 375 MW. The transportation of electrical energy is more economical
as compared to the transportation of coal.
1.3 DESIGN FEATURES:-
The satisfactory design consists of the flowing steps.
 Estimation of cost.
 Selection of site.
 Capacity of Power Station.
 Selection of Boiler & Turbine.
 Selection of Condensing Unit.
 Selection of Electrical Generator.
 Selection of Cooling System.
 Design of Control and instrumentation system.
The design of steam power station requires wide experience as the subsequent
operation and maintenance are greatly affected by its design. The most efficient design
consist of properly sized component designed to operate safely and conveniently along
with its auxiliaries and installation.
Figure 1.1 VIEW OF KOTA SUPER THERMAL POWER PLANT

[6 ]
CHAPTER -2
General Layout & Basic Idea
A control system of station basically works on Rankin Cycle.
Steam is produced in Boiler is exported in prime mover and is condensed in condenser to
be fed into the boiler again. In practice of good number of modifications are affected so as
to have heat economy and to increase the thermal efficiency of plant.
Figure 2.1 Layout of Power Plant
The Kota Thermal Power Station is divided into four main circuits :
 Fuel and Ash Circuit.
 Air and Gas Circuit.
 Feed water and Steam Circuit.
 Cooling Water Circuit.

[7 ]
2.1 Fuel & Ash Circuit:-
Fuel from the storage is fed to the boiler through fuel handling
device. The fuel used in KSTPS is coal, which on combustion in the boiler produced the
ash. The quantity of ash produced is approximately 35-40% of coal used. This ash is
collected at the back of the boiler and removed to ash storage tank through ash disposal
equipment.
2.2 Air and Gas Circuit:-
Air from the atmosphere is supplied to the combustion chamber of
Boiler through the action of forced draft fan and induced draft fan. The flue gas gases are
first pass around the boiler tubes and super heated tubes in the furnace, next through dust
collector (ESP) & then economizer. Finally, they are exhausted to the atmosphere through
fans.
2.3 Feed Water and Steam Circuit:-
The condensate leaving the condenser is first heated
in low pressure (LP) heaters through extracted steam from the lower pressure extraction of
the turbine. Then its goes to dearator where extra air and non-condensable gases are
removed from the hot water to avoid pitting / oxidation. From deaerator it goes to boiler
feed pump which increases the pressure of the water. From the BFP it passes through
the high pressure heaters. A small part of water and steam is lost while passing through
different components therefore water is added in hot well. This water is called the make up
water. Thereafter, feed water enters into the boiler drum through economizer. In boiler
tubes water circulates because of density difference in lower and higher temperature
section of the boiler. The wet steam passes through superheated. From superheated it
goes into the HP turbine after expanding in the HP turbine. The low pressure steam called
the cold reheat steam (CRH) goes to the reheater (boiler). From reheater it goes to IP
turbine and then to the LP turbine and then exhausted through the condenser into hot well.

[8 ]
2.4 Cooling Water Circuit:-
A large quantity of cooling water is required to condense the
steam in condenser and marinating low pressure in it. The water is drawn from reservoir
and after use it is drained into the river.
Figure 2.2 CROSS SECTIONAL VIEW OF FOUR MAJOR PART FORM A POWER
PLANT

[9 ]
CHAPTER -3
COAL HANDLING PLANT
INTRODUCTION:-
It can be called the heart of thermal power plant because it provided
the fuel for combustion in boiler. The coal is brought to the KSTPS through rails there are
fourteen tracks in all for transportation of coal through rails. The main coal sources for
KSTPS are SECL (South Eastern Coalfields Limited), NCL (Northern Coalfield Limited).
Everyday 6 to 7 trains of coal are unloaded at KSTPS. Each train consists of 58 wagons
and each wagons consists of 50 tones of coal. The approximate per day consumption at
KSTPS is about 18000 metric tones. It costs approximate 4.5 crores of rupees per day
including transportation expenses. The coal is firstly unloaded from wagon by wagon
triplers then crushed by crushers and magnetic pulley and pulverized to be transformed to
the boiler. The whole transportation of coal is through conveyor belt operated by 3-Ø
Induction motor.
The coal handling plant can broadly be divided into three sections :-
1) Wagon Unloading System.
2) Crushing System.
3) Conveying System.
3.1 WAGON UNLOADING SYSTEM:-
3.1.1Wagon Tripler:-
It unloads the coal from wagon to hopper. The hopper, which is
made of Iron , is in the form of net so that coal pieces of only equal to and less than 200
mm. size pass through it. The bigger ones are broken by the workers with the help of
hammers. From the hopper coal pieces fall on the vibrator. It is a mechanical system
having two rollers each at its ends.
The rollers roll with the help of a rope moving on pulley operated
by a slip ring induction motor with specification:

[10
]
Figure 3.1 Wagon Tripler
Rated Output. : 71 KW.
Rated Voltage. : 415 V.
Rated Current. : 14.22 Amp.
Rated Speed. : 975 rpm.
No. of phases. : 3
Frequency. : 50 Hz.
No. of Wagon Tripler : 5
The four rollers place themselves respectively behind the first and
the last pair of wheels of the wagon. When the motor operates the rollers roll in forward
direction moving the wagon towards the “Wagon Table”. On the Wagon table a limit is
specified in which wagon to be has kept otherwise the triple would not be achieved.

[11
]
3.2 CRUSHING SYSTEM:-
3.2.1Crusher House:-
It consists of crushers which are used to crush the coal to 20 mm.
size. There are 10 Coal Crushers in K.S.T.P.S. There are mainly two type of crushers
working in KSTPS:-
Primary Crushers i.e. i) Rail crushers or ii) Rotary breaker.
Secondary Crushers. i.e. Ring granulators.
3.2.1.1 Primary Crushers:-
Primary crushers are provided in only CHP stage 3 system, which
breaking of coal in CHO Stage 1 & Stage 2 system is done at wagon tripler hopper jail up
to the size (-) 250 mm.
3.2.1.2 Secondary Crusher:-
Basically there are four ways to reduce material size : impact attrition , Shearing and
Compression. Most of the crushers employ a combination of three crushing methods.
Ring granulators crush by compressing accompanied by impact and shearing.The unique
feature of this granulator is the minimum power required for tone for this type of material to
be crushed compared to that of other type of crushers.
3.3 Construction & Operation:-
Secondary crushers are ring type granulators crushing at the rate of 550 TPH
/ 750 TPH for input size of 250 mm. and output size of 20 mm. The crusher is coupled with
motor and gearbox by fluid coupling.
Main parts of granulator like break plates, cages , crushing rings and other internal parts
are made of tough manganese (Mn) steel.
The rotor consists of four rows of crushing rings each set having 20 Nos. of
toothed rings and 18 Nos. of plain rings. In CHP Stage 1 & 2 having 64 Nos. of ring
hammers. These rows are hung on a pair of suspension shaft mounted on rotor discs.
Crushers of this type employ the centrifugal force of swinging
rings stroking the coal to produce the crushing action. The coal is admitted at the top and
the rings stroke the coal downward. The coal discharges through grating at the bottom.

[12
]
3.4 CONVEYING SYSTEM:-
3.4.1 Stacker Reclaimer:-
The stacker re-claimer unit can stack the material on to the pipe or reclaim the
stack filed material and fed on to the main line conveyor. While stacking material is being
fed from the main line conveyor via Tripler unit and vibrating feeder on the intermediate
conveyor which feds the boom conveyor of the stacker cum reclaimer. During reclaiming
the material dis discharged on to the boom conveyor by the bucket fitted to the bucket
wheel body and boom conveyor feeds the material on the main line conveyor running in
the reverse direction.
3.5 Conveyor belt Specification of Stacker / Reclaimer:-
Belt width. : 1400 mm.
Speed. : 2.2 m/second.
Schedule of motor : All 3-Ø induction motors.
Bucket wheel motor : 90 KW.
Boom Conveyor motor : 70 KW.
Intermediate Conveyor Motor : 90 KW.
Boom Housing Motor : 22 KW.
Slewing assembly. : 10 KW.
Travel Motor : 7.5 KW.
Vibrating Feeder. : 2x6 KW.
Total installed power. : 360 KW.

[13
]
CHAPTER -4
ASH HANDLING PLANT
This plant can be divided into 3 sub plants as follows:-
1) Fuel and Ash Plant.
2) Air and Gas Plant.
3) Ash Disposal and & Dust Collection Plant.
4.1 Fuel and ash plant:-
Coal is used as combustion material in KTPS, In order to get an efficient
utilization of coal mills. The Pulverization also increases the overall efficiency and flexibility
of boilers. However for light up and with stand static load , oil burners are also used. Ash
produced as the result of combustion of coal is connected and removed by ash handling
plant. Ash Handling Plant at KTPS consists of specially designed bottom ash and fly ash
in electro static precipitator economizer and air pre-heaters hoppers.
4.2 Air & Gas Plant:-
Air from atmosphere is supplied to combustion chamber of boiler through
the action of forced draft fan. In KTPS there are two FD fans and three ID fans available
for draft system per unit. The air before being supplied to the boiler passes through pre-
heater where the flue gases heat it. The pre heating of primary air causes improved and
intensified combustion of coal.
The flue gases formed due to combustion of coal first passes round the
boiler tubes and then it passes through the super heater and then through economizer . In
re-heater the temperature of the steam (CRH) coming from the HP turbines heated with
increasing the number of steps of re-heater the efficiency of cycle also increases. In
economizer the heat of flue gases raises the temperature of feed water. Finally the flue
gases after passing through the Electro-Static Precipitator is exhausted through chimney.

[14
]
4.3 Ash Disposal & Dust Collection Plant:-
KSTPS has dry bottom furnace. Ash Handling Plant consists of
especially designed bottom and fly ash system for two path boiler. The system for both
units is identical and following description is applied to both the units the water
compounded bottom ash hopper receives the bottom ash from the furnace from where it is
stores and discharged through the clinker grinder. Two slurry pumps are provided which is
common to both units & used to make slurry and further transportation to ash dyke through
pipe line.
Dry free fly ash is collected in two number of 31 fly ash hoppers
which are handled by two independent fly ash system. The ash is removed from fly ash
hoppers in dry state is carried to the collecting equipment where it is mixed with water and
resulting slurry sump is discharged
4.4 Utilization:-
In compliance to Govt. of India Gazatte Notification issued on 14th
Sept. 1999
for making available ash free of cost, KSTPS has achieved 100% Dry Fly ash utilization.
KSPS signed agreements for dedicated generating units allocations including Construction
& Operation of complete dry fly ash evacuation system from each unit in two phases i.e.
from ESP to Intermediate silo and intermediate silo to Main Supply Silo near KSTPS
boundary with following cement manufacturing companies –
Unit # 1&2 – M/s. Associated Cement Co. Ltd.
Unit # 3 – M/s Birla Cement Works Ltd.
Unit # 4&5 – M/s Grasim Industries Ltd.
Unit # 6 – M/s Manglam Cement Ltd. & Shree Cement Ltd.
Unit # 7 – M/s Grasim Industries & Shree Cement Ltd.
Concerted efforts have been made towards utilization of disposed fly & bottom ash
accumulated in KSTPS ash dykes. The ash is provided free of cost and has been utilized
by various small entrepreneurs i.e. Brick-kiln industries, small fly ash product industries,
Cement manufacturing Industries and for land filling by National Highway Authority of India
in construction of NH-12 and NH-76.

Figure 4.1 ASH HANDING PLANT
[14]

[15
]
CHAPTER -5
ELECTRO-STATIC PRECIPITATOR
5.1 Scope & Principle of Operation:-
For general mankind, today an Eco friendly
industry is must. As far as air pollution is concerned now a days various flue gases filter
are there in service. The choice depends on the size of suspended particle matter. These
filters are E.S.P. Fabric filter high efficiency cyclone separations and sitelling room. Fop fly
ash , where the particle size vary from 0.75 microns to 100 micron use gradually use
E.S.P. to purify the flue gases due to its higher efficiency & low running cost etc. In an
ESP the dust lidder gas is passed through an intense electric field, which causes ionization
of the gases & they changed into ion while traveling towards opposite charged electrode
get deposited as particles and thus dust is electric deposited an electrode creating the
field. It is continuous process.
5.2 CONTROLLER:-
Now a day micro-processor based intelligent controllers are
used to regulate the power fed to the HVR. The controls the firing / ignition angle of the
thyristor connected in parallel mode. Input out waves of the controller and HVR are also
shown above, which clearly indicates that average power fed to ESP field can be
controlled by variation of the firing angle of thyristor.
The output of controller with respect to time is also controlled by
microprocessor, so that ESP operation is smooth and efficient . The chars are as shown:
As can be seen in the event of spark between electrode the output of
controller is reduced to zero for few millisecond for quenching the spark. Controller also
takes place care of fault in KVR and gives a trapping and non-trapping alarm as per the
nature of fault.

[16
]
5.3 HIGH VOLTAGE RECTIFIER TRANSFORMER:-
HVR receives the regulated supply from controller. It
steps up to high voltage rectifier. The D.C. supply is fed to E.S.P. field through its negative
bushing. The positive bushing so connected to earth through small resistance which forms
a current feed back circuit. A very high resistance column is also connected with negative
bushing . It forms the voltage feed back circuit. These two feedback are used in the
controller for indication and control purpose.
5.4 E.S.P. FIELD:-
The field consists of emitting and collecting electrodes structure which
are totally isolated from each other and hanging with the top roof of field. The emitting is
also isolated from the roof through the support insulators which are supporting the emitting
electrode frame works and also the supply to these electrodes is fed through support
insulators. The collecting electrodes are of the shape of flat plates. By several similar
plates which the emitting electrodes are of the shape of spring. Strong on the emitting
frame work with the help of hooks in both the ends.
The ash depositing on these electrode is rapped down by separate
wrapping mechanism happens at the bottom of the field. From these hoppers ash is
evacuated by ash handling system and dispose to the disposal area. The wrapping
system is automatically controlled with the help of the programmable metal controller,
located in the ESP auxiliaries control panels.

[17
]
CHAPTER -6
BOILER
A boiler (or steam generator) is a closed vessel in which water, under
pressure is converted into steam. It is one of the major components of a thermal power
plant. A boiler is always designed to absorb maximum amount of heat released in process
of combustion. This is transferred to the boiler by all the three modes of heat transfer i.e.
conduction, convection and radiation.
6.1 Boilers are classified as:-
6.1.1 Fire tube boiler: -
In this type the products of combustion pass through the tubes
which are surrounded by water. These are economical for low pressure only.
6.1.2 Water tube boiler:-
In this type of boiler water flows inside the tubes and hot gases flow
outside the tubes. These tubes are interconnected to common water channels and to
steam outlet.
 The water tube boilers have many advantages over the fire tube boilers
 High evaporation capacity due to availability of large heating surface.
 Better heat transfer to the mass of water.
 Better efficiency of plant owing to rapid and uniform circulation of water in tubes.
 Better overall control.
 Easy removal of scale from inside the tubes.
In KSTPS, Natural circulation, tangentially fired, over
hanged type, Water tube boilers are used. Oil burners are provided between coal burners
for initial start up and flame stabilization. Firstly, light oil (diesel oil) is sprayed for

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initialization then heavy oil (high speed diesel oil) is used for stabilization of flame.
Pulverized coal is directly fed from the coal mills to the burners at the four corners of the
furnace through coal pipes with the help of heated air coming from PA fan. Four nos. of
ball mills of 34MT/hr. capacity each have been installed for each boiler. The pressure
inside boiler is -ive so as to minimized the pollution and looses & to prevent the accidents
outside the boiler.
For ensuring safe operation of boilers, furnace safe
guard supervisory system (FSSS) of combustion engineering USA designed has been
installed. This equipment systematically feed fuel to furnace as per load requireme. The
UV flame scanners installed in each of the four corners of the furnace, scan the flame
conditions and in case of unsafe working conditions trip the boiler and consequently the
turbine. Turbine - boiler interlocks safe guarding the boiler against possibility furnace
explosion owing to flame failure.
6.2 Furnace:
Figure 6.1 furnace

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]
Furnace is primary part of the boiler where the chemical energy available
in the fuel is converted into thermal energy by combustion. Furnace is designed for
efficient and complete combustion. Major factors that assist for efficient combustion are
the temperature inside the furnace and turbulance, which causes rapid mixing of fuel and
air. In modern boilers, water-cooled furnaces are used.
6.3 PULVERISED FUEL SYSTEM:-
The boiler fuel firing system is tangentially firing system in which the fuel is introduced from
wind nozzle located in the four corners inside the boiler.
The crushed coal from the coal crusher is transferred into
the unit coalbunkers where the coal is stored for feeding
into pulverizing mill through rotary feeder The rotary
feeders feed the coal to pulverize mill at a definite rate.
Then coal burners are employed to fire the pulverized
coal along with primary air into furnace. These burners
are placed in the corners of the furnace and they send
horizontal streams of air and fuel tangent to an imaginary
circle in the center of the furnace. Figure 6.2 Pulverised System
6.4 Fuel Oil System:-
The functional requirement of the fuel burning system is to supply a
controllable and uninterrupted flammable furnace input of fuel and air and to continuously
ignite and burn the fuel as rapidly as it is introduced into the furnace. This system provides
efficient conversion of chemical energy of fuel into heat energy. The fuel burning system
should function such that fuel and air input is ignited continuously and immediately upon its
entry into furnace.
The Fuel air (secondary air) provided FD fan, surrounds the fuel nozzles. Since
this air provides covering for the fuel nozzles so it is called as mantle air. Dampers are
provided so that quantity of air can be modulated. Coal burners distribute the fuel and air
evenly in the furnace.

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Ignition takes place when the flammable furnace input is heated above the ignition
temperature. No flammable mixture should be allowed to accumulate in the furnace.
Ignition energy is usually supplied in the form of heat. This ignition
energy is provided by oil guns and by igniters.
6.5 Boiler Drum:-
The drum is a pressure vessel. Its function is to separate water and steam from
mixture (of steam & water) generated in the furnace walls. It provides water storage for
preventing the saturation of tubes. It also houses the equipment needed for purification of
steam. The steam purification primarily depends on the extent of moisture removal, since
solids in steam are carried by the moisture associated with it. The drum internals reduce
the dissolved solids content of the steam to below the acceptable limit. drum is made up of
two halves of carbon steel plates having thickness of 133 mm.
The top half and bottom half are heated in a plate heating furnace at a very high
temperature and are pressured to form a semi cylindrical shape. The top and bottom semi
cylinders with hemispherical dished ends are fusion welded to form the boiler drum. The
drum is provided with stubs for welding all the connecting tubes i.e. down comer stubs,
riser tubes stubs and super-heater outlet tube stubs.
Boiler drum is located at a height of 53m from ground. The drum is provided with
manholes and manhole covers. Manhole is used for facilitating the maintenance person to
go inside the drum for maintenance.

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. Figure 6.3 Steam Drum
The drum form the part of boiler circulating system i.e. movement of fluid from the
drum to the combustion zone and back to boiler drum. Feed water is supplied to the drum
from the economizer through feed nozzles. Water from the drum goes to water walls
through six down comers.
Main parts of boiler drum are:-
 Feed pipe
 Riser tube
 Down comer
 Baffle plate
 Chemical dosing pipe
 Turbo separation
 Screen dryer
 Drum level gauge

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6.6 Draft System:-
The combustion process in a furnace can take place only when it receives
a steady flow of air and has the combustion gases continuously removed. Theoretically
balanced draft means keeping furnace pressure equal to atmospheric pressure, but in
practice the furnace is kept slightly below atmospheric pressure. It ensures that there is no
egress of air or hot gas and ash into boiler house.
6.7 Draught Fans:-
A fan can be defined as volumetric machine which like pumps moves quantities of
air or gas from one place to another. In doing this it overcomes resistance to flow by
supplying the fluid with the energy necessary for contained motion. The following fans are
used in boiler house.
6.7.1 Primary air fan (P.A. fan) or Exhauster fan-
Pulverized coal is directly fed from coal mills to the burners at the four corners of the
furnace through coal pipes with the help of heated air coming from PA fan. Secondly, this
fan also dries the coal. Usually sized for 1500 RPM due to high pressure.
6.7.2 Forced draught fan (F.D. fan):-
The combustion process in the furnace can take place only when it receives a
steady flow of air. This air is supplied by FD fan. Thus FD fan takes air from atmosphere at
ambient temperature & so provides additional draught. Its speed varies from 600-1500
RPM.
6.7.3 Induced Draught fan (I.D. fan):-
The flue gases coming out of the boiler are passed to the ESP &
then dust free gases are discharged up by the chimney to the atmosphere through the ID
fan.

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]
6.8 Economizer:-
. Figure 6.4 Economizer
The flue gases coming out of the boiler carry lot of heat. An economizer extracts a part of
this heat from the flue gases and uses it for heating the feed water before it enters into the
steam drum. The use of economizer results in saving fuel consumption and higher boiler
efficiency but needs extra investment. In an economizer, a large number of small diameter
thin walled tubes are placed between two headers. Feed water enters the tubes through
the other. The flue gases flow outside the tubes.
6.9 Air preheaters:-
Air preheaters are employed to recover the heat from the flue gases
leaving the economizer and are used to heat the incoming air for combustion. This raises
the temperature of the furnace gases, improves combustion rates an efficiency and lowers
the stack (chimney) temperature, thus improving the overall efficiency of the boiler.
Cooling of flue gases by 20% raises the plant efficiency by 1%.

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]
Figure 6.5 air pre-heater
Air preheaters are employed to recover the heat from the flue gases leaving the
economizer and are used to heat the incoming air for combustion. This raises the
temperature of the furnace gases, improves combustion rates and efficiency and lowers
the stack (chimney) temperature, thus improving the overall efficiency of the boiler.
Cooling of flue gases by 20% raises the plant efficiency by 1%.
In KSTPS regenerative type of preheater is used. They use a cylindrical rotor made
of corrugated steel plate. The rotor is placed in a drum which is divided into two
compartments, i.e. air compartment (primary air coming from primary air fan and
secondary air for air coming from FD fan with + ive pressure) and flue gases (from
economizer with – ive pressure) compartments. To avoid leakage from one compartment
to other seals are provided.
The rotor is fixed on an electrical shaft rotating at a speed of 2 to 4 rpm. As the
rotor rotates the flue gases, are pass through alternatively gas and air zone. The rotor
elements are heated by flue gases in their zone and transfer the heat to air when they are
in air zone. The air temperature required for drying in the case of coal-fired boiler decided
the size of the air heaters
6.10 Super heater:-
Superheated steam is that steam, which contains more heat than the saturated
steam at the same pressure i.e. it, has been heated above the temperature corresponding

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to its pressure. This additional heat provides more energy to the turbine and thus the
electrical power output is more.
A super heater is a device which removes the last traces of moisture from the
saturated steam leaving the boiler tubes and also increases its temperature above
the saturation temperature.
The steam is superheated to the highest economical temperature not only to increase the
efficiency but also to have following advantages –
 Reduction in requirement of steam quantity for a given output of energy owing to its
high internal energy reduces the turbine size.
 Superheated steam being dry, turbine blades remain dry so the mechanical
resistance to the flow of steam over them is small resulting in high efficiency.
 No corrosion and pitting at the turbine blades occur owing to dryness of steam.
6.11 Re-heater:-
Re-heaters are provided to raise the temperature of the steam from which
part of energy has already been extracted by HP turbine. This is done so that the steam
remains dry as far as possible through the last stage of the turbine. A re-heater can also
be convection, radiation or combination of both.
6.12 Circulation System:-
In natural circulation system, water delivered to steam generator from header,
which are at a temperature well below the saturation value corresponding to that pressure.
After header, it is delivered to economizer, which heated to above the saturation
temperature.
From economizer the water enters the drum and thus joins the circulation system through
down covering water wall tubes. In water wall tubes a part of the water is converted to
steam due to boiler and the mixture flows back to the drum. In the drum, the steam is

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separated out through the steam separators and passed to the super heater. After the
super heater when the steam temperature becomes high and pressure upto 150 Kg./cm3
steam is allowed to enter the turbine to convert potential energy to kinetic energy.
6.13 Soot Blower:-
The boiler tubes are cleaned with the help of steam by the process called soot
blowing. We are well known that a greater no. of tubes are presented inside the boiler.
Slowly and slowly the fine ash particles are collected on the tube surface and from a layer
this is called soot. Soot is a thermal insulating material.
There are mainly three types of soot blower are used in KSTPS: -
 Water wall soot blower
 Super heater soot blower
 Air pre heater soot blower
6.14 TECHNICAL SPECIFICATION OF BOILER
1.Type : Direct fired, natural circulation
2. No. of Units. : Two.
3.Make : BHEL.
4.Capacity. : 375 tonnes per hour.
5.Steam Pressure. : 139 Kg./Cm2
6.Efficiency : 86.6 %.
7.No. of fans in service.
a) ID fans. : 2 Nos.
b) FD fans. : 2 Nos.
c) PA fans. : 2 Nos.
d) Seal Air fan. : 1 No.
e) Scanner Air fan. : 1 No.
f) Igniter fan. : 1 No.

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8. Steam Temperature : 540o
C.
9. No. of coal mills in : 3 Nos. service.
10. No. of soot blowers : 70 Nos.
FUEL :-
A) COAL:-
Type : Slack Coal.
Quantity consumed : 3074 tones per day.
Type of handing. : Conveyor.
Ash disposal : Wet system.
B) OIL:-
Type. : HSD and fuel oil.
Quantity. : a) HSD – 5520 KL per year.
b) Furnace Oil : 28800 KL per year.
No. of chimney / stack. : 1 / 2.
Height of Chimney. : 180 Meters.
Volume of flue Gas/ : 198 M3
/ Sec. Air emitted.
Temp. of flue gas. : 140o
C.
ESP : One for each unit.
6.15 GENERAL DESCRIPTION:-
Boilers are tangentially fired, balance draft,
natural circulation , radiant type, dry bottom with direct fired pulverized coal from bowl
mills. They are designed for burning low grade coal with high ash content. Oil burners are
located between coal burners for flame stabilization. Pulverized coal is directly fed from
the coal mills to the burners at the four corners of the furnace through coal pipes. The

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pulverized fuel pipes from the mills to the bunkers are provided with basalt lined bends to
reduce erosion and to improve the life of these pipes owing to poor grade of coal there is a
high percentage of mill rejects. The mill rejects are conveyed in a sluice way to an under-
ground tank. From this tank the mixture is taken to an overhead hydro-bin where water is
decanted and the mill reject are disposed off by trucking. ESP with collection efficiency of
99.8% have been provided to reduce environmental pollution and to minimize induce draft
fan wear. A multi-flue reinforced concrete stack with two internal flues has been provided.
Two boiler feed pumps each of 100 % capacity are driven by AC motor through
hyd. coupling with scoop tube arrangement for regulating feed water pressure for each
unit.
The air required for combustion is supplied by two forced draft fans.
Due to anticipated high abrasion of ID fans impellers. Three ID fans each of 60% capacity
have been provided one ID fan to serve as standby.
For ensuring safe operation of boilers, furnace safe guard supervisory system
(FSSS) of combustion engineering USA designed has been installed. This equipment
systematically feed fuel to furnace as per load requirement.
The UV flame scanners installed at two elevation in each of the four corners of the
furnace, scan the flame conditions and in case of unsafe working conditions but out fuel
and trip the boiler and consequently the turbine. Turbine – boiler interlocks safe guarding
the boiler against possibility furnace explosion owing to flame failure.
Facilities have been provided to simultaneously unload and transfer 10 light oil and
40 heavy oil tankers to the designated tanks. Oil preheating arrangement is provided on
the tanks floors for the heavy oil tanks. Superheated steam temperature is controlled by
attemperation.
Re-heater steam temperature is primarily by tilting fuel burners through + 30o
and
further control if necessary is done by attemperation.

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CHAPTER - 7
STEAM TURBINE
INTRODUCTION:-
Turbine is a machine in which a shaft is rotated steadily by impact or
reaction of current or stream of working substance (steam, air, water, gases etc) upon
blades of a wheel. It converts the potential or kinetic energy of the working substance into
mechanical power by virtue of dynamic action of working substance. When the working
substance is steam it is called the steam turbine.
Figure 7.1 steam turbine

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]
7.1 PRINCIPAL OF OPERATION OF STEAM TURBINE:-
Working of the steam turbine depends wholly upon the dynamic action of Steam.
The steam is caused to fall in pressure in a passage of nozzle: doe to this fall in pressure a
certain amount of heat energy is converted into mechanical kinetic energy and the steam is
set moving with a greater velocity. The rapidly moving particles of steam, enter the moving
part of the turbine and here suffer a change in direction of motion which gives rose to
change of momentum and therefore to a force. This constitutes the driving force of the
machine. The processor of expansion and direction changing may occur once or a number
of times in succession and may be carried out with difference of detail. The passage of
steam through moving part of the commonly called the blade, may take place in such a
manner that the pressure at the outlet side of the blade is equal to that at the inlet inside.
Such a turbine is broadly termed as impulse turbine. On the other hand the pressure of the
steam at outlet from the moving blade may be less than that at the inlet side of the
blades; the drop in pressure suffered by the steam during its flow through the moving
causes a further generation of kinetic energy within the blades and adds to the propelling
force which is applied to the turbine rotor. Such a turbine is broadly termed as impulse
reaction turbine.
The majority of the steam turbine have, therefore two important
elements, or Sets of such elements . These are (1) the nozzle in which the system
expands from high pressure end a state of comparative rest to a lower pressure end a
status of comparatively rapid motion.
The blade or deflector , in which the steam particles changes its
directions and hence its momentum changes . The blades are attach to the rotating
elements are attached to the stationary part of the turbine which is usually termed the
stator, casing or cylinder.
Although the fundamental principles on which all steam turbine operate
the same, yet the methods where by these principles carried into effect very end as a
result, certain types of turbine have come into existence.
1. Simple impulse steam turbine.
2. The pressure compounded impulse turbine.
3. Simple velocity compounded impulse turbine.

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4. Pressure-velocity compounded turbine.
5. Pure reaction turbine.
6. Impulse reaction turbine.
7.2 Description of Steam Turbines:-
7.2.1 Steam flow:-
210 MW steam turbine is a tandem compound machine with HP, IP & LP parts. The
HP part is single flow cylinder and HP & LP parts are double flow cylinders. The individual
turbine rotors and generator rotor are rigidly coupled. The HP cylinder has a throttle
control. Main steam is admitted before blending by two combined main stop and control
valves. The HP turbine exhaust (CRH) leading to reheated have tow swing check valves
that prevent back flow of hot steam from reheated, into HP turbine. The steam coming
from reheated called HRH is passed to turbine via two combined stop and control valves.
The IP turbine exhausts directly goes to LP turbine by cross ground pipes.
7.2.2 HP Turbine:-
The HP casing is a barrel type casing without axial joint. Because of its rotation
symmetry the barrel type casing remain constant in shape and leak proof during quick
change in temperature. The inner casing too is cylinder in shape as horizontal joint flange
are relieved by higher pressure arising outside and this can kept small. Due to this reason
barrel type casing are especially suitable for quick start up and loading.The HP turbine
consists of 25 reaction stages. The moving and stationary blades are inserted into
appropriately shapes into inner casing and the shaft to reduce leakage losses at blade
tips.
7.2.3 IP Turbine:-
The IP part of turbine is of double flow construction. The casing of IP turbine is split
horizontally and is of double shell construction. The double flow inner casing is supported
kinematically in the outer casing. The steam from HP turbine after reheating enters the
inner casing from above and below through two inlet nozzles. The centre flows
compensates the axial thrust and prevent steam inlet temperature affecting brackets,

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bearing etc. The arrangements of inner casing confines high steam inlet condition to
admission branch of casing, while the joints of outer casing is subjected only to lower
pressure and temperature at the exhaust of inner casing. The pressure in outer casing
relieves the joint of inner casing so that this joint is to be sealed only against resulting
differential pressure.
The IP turbine consists of 20 reaction stages per flow. The moving and
stationary blades are inserted in appropriately shaped grooves in shaft and inner
casing.
7.2.4 LP Turbine:-
The casing of double flow type LP turbine is of three shell design. The shells are
axially split and have rigidly welded construction. The outer casing consist of the front and
rear walls , the lateral longitudinal support bearing and upper part.
The outer casing is supported by the ends of longitudinal beams on the base plates
of foundation. The double flow inner casing consist of outer shell and inner shell. The
inner shell is attached to outer shell with provision of free thermal movement.
Steam admitted to LP turbine from IP turbine flows into the inner casing from both
sides through steam inlet nozzles.

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CHAPTER – 8
TURBO GENERATOR
8.1.1 THEORY
TURBO GENERATOR manufactured by B.H.E.L. and incorporated with most
modern design concepts and constructional features, which ensures reliability, with
constructional & operational economy.
The generator stator is a tight construction, supporting & enclosing the stator
windings, core and hydrogen coolers. Cooling medium hydrogen is contained within frame
& circulated by fans mounted at either ends of rotor. The generator is driven by directly
coupled steam turbine at a speed of 3000 r.p.m. the Generator is designed for continuous
operation at the rated output. Temperature detectors and other devices installed or
connected within then machine, permit the windings, teeth core & hydrogen temperature,
pressure & purity in machine under the conditions. The source of excitation of rotor
windings is thyristor controlled D.C. supply. The auxiliary equipment‟s supplied with the
machine suppresses and enables the control of hydrogen pressure and purity, shaft sealing
lubricating oils. There is a provision for cooling water in order to maintain a constant
temperature of coolant (hydrogen) which controls the temperature of windings.
8.1.2 STATOR FRAME
The stator frame of welded steel frame construction, which gives sufficient &
necessary rigidity to minimize the vibrations and to withstand the thermal gas pressure.
Heavy end shields enclose the ends of frame and form mounting of generator bearings and
radial shaft seals. Ribs subdivide the frame and axial members to form duct from which the
cooling gas to & fro radial ducts in the core and is re-circulated through internally mounted
coolers. All the gas ducts are designed so as to secure the balanced flow of hydrogen to all
parts of the core. The stator constructed in a single piece houses the core and windings.
The horizontally mounted water cooled gas coolers being so arranged that it may be

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cleaned on the water side without opening the machine to atmosphere. All welded joints
exposed to hydrogen are specially made to prevent leakage. The complete frame is
subjected to hydraulic test at a pressure of 7 ATA.
8.1.3 STATOR CORE
It is built up of special sheet laminations and whose assembly is supported by a
special guide bass. The method of construction ensures that the core is firmly supported at
a large number of points on its periphery. The laminations of high quality silicon steel which
combines high permeability with low hysteresis and eddy current losses. After stamping
each lamination is varnished on both sides with two coats. The segment of insulating
material is inserted at frequent intervals to provide additional insulation. The laminations
are stamped out with accurately fine combination of ties. Laminations are assembled on
guide bass of group separated by radial ducts to provide ventilation passage. The
ventilation ducts are disposed so as to distribute the gas evenly over the core & in
particularly to give adequate supports to the teeth. At frequent intervals during stacking the
assembled laminations are passed together in powerful hydraulic press to ensure tight core
which is finally kept between heavy clamping plates which are non-magnetic steel. Use of
non-magnetic steel reduces considerably by heating of end iron clamping. The footed
region of the core is provided by pressing figures of non-magnetic steel, which are welded
to the inner periphery of the clamping plates. In order to reduce the losses in the ends
packets special dampers are provided at either ends of core. Mostly dampers are provided
to prevent hunting in ac machines.
8.1.4 STATOR BARS
Stator bars are manufactured as half bars. Each stator half coil is composed of
double glass cover and bars of copper transposed in straight portion of “Robill Method” so
that each strip occupies every radial portion in the bar. For an equal length along the bar.
They are made in strips to reduce skin effect. The winding overhead is in volute shape. The
overhung portion of the bar is divided into four quadrants & insulated. The arrangement
reduces additional losses due to damping currents which otherwise be present due to self-
induced non-uniform flux distribution in the coil slots. The main distribution for the bar
consists of resin rich mica loosed thermosetting epoxy. This has excellent mechanical and
electrical properties & does not require any impregnation. Its moisture absorbing tendency

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is very low and behavior of mica is for superior than any other conventional tape insulation
system. Semi-conductor coating is also applied to a part of overhung with a straight overlap
of conductive coil in the sides to reduce eddy currents to minimum. Conductor material is
electrolytic copper connections brazed with free coating silver alloy to obtain joints, which
are both electrically & mechanically sound.
8.1.5 STATOR WINDINGS
Stator windings are double star layers, lap wound, three phase, and short pitch type.
The top & bottom are brazed and insulated at either end to form turns. Several such turns
form a phase. Phases are connected to form a double star winding. The end of winding
form involutes shape ends, inclined towards machine axis by 20o
, thus form a basket
winding with total induced conical angle of 400
. Due to this stray load losses in the stator
ends to zero. The arrangement of complete stator winding electrical circuit is viewed from
turbine end of generator & rotor windings. Slot numbering is clockwise from turbine end. A
thick line identifies the top bar in slot No.1. End windings will be sealed against movement
of short circuit by both axial & peripheral bracing. The later consists of hardened glass
laminated blocks inserted between adjacent coil sides in coil overhangs, so that with the
coils, they form a continuous rigid ring. Glass cord or top is used lashing the packing of
blocks. The complete assembly is secured b y high tensile brass blots. The winding is
designed to withstand short circuit stresses. The exposed portion of windings is finally
coated. Insulation of individual bars & stator windings at various stresses is tested with
applied high voltages of AC of Hz.
8.1.6 TERMINAL BUSHINGS
Six output leads (3 long, 3 short) have been brought out of the coming on the exciter
side. External connections are to be made to the three shorter terminals, which are phase
terminals. The large terminals are of neutral & current transformer is inserted. The
conductor of Generator terminal bushing having hollow copper tubes with Copper brazed at
the ends to avoid leakage of hydrogen. Hollow portions enable bushings to be hydrogen
cooled. Ends of bushings are Silver-plated: middle portion of the bushing is adequately
insulated & has a circular flange for bolting the stator casing. Gaskets are provided
between the Flange of terminal bushings and castings to make it absolutely gas tight.

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]
8.1.7 BEARINGS
Generator bearings have electrical seats of consists of steel bodies with removable
steel pads. The bearings are formed for forced lubrication of oil at a pressure of 2-3 ATM/
from the same pump that supplies oils to the turbine, bearings & governing gears. There is
a provision to ensure & measure the rotor bearing temperature by inserting a resistance
thermometer in the oil pockets.
8.1.8 VENTILATION SYSTEM
The machine is designed with ventilation system having 2 ATM rated hydrogen
pressure. Two axial fans mounted on either side of the rotor to ensure circulation of
hydrogen. The stator is designed for radial ventilation by stem. The end stator core packets
& core clamping & plates are intensively cooled by Hydrogen through special ventilation
system. Design of special ventilation is so as to ensure almost uniform temperature of rotor
windings and stator core. Rated load operating temperature is well within the limits
corresponding to the Class B operation. Embedded Resistance Temperature Detectors do
continuous monitoring of Hydrogen temperature at active parts of Generator.
8.1.9 RESISTANCE TEMPERATURE DETECTORS (R.T.D.)
An R.T.D. is a point resistance element. Operation of R.T.D. depends on the principal
that electrical resistance of metallic conductor varies linearly with temperature.
8.1.10 APPLICATIONS
RTD & its associated equipments are designed for use with Generator to determine
temperature at various parts & places. The equipment‟s consists of two parts:-
1. Switch Board Equipment: is usually includes a temperature indicating meter, test
resistor transfer switch & leads.
2. Machine Equipment: is usually includes temperature R.T.D.leads and terminal blocks
with grounding connections.

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Leads from RTD are brought out to the terminal board by cables through conduits to protect
them from physical damage and from contact with high voltage coils. Some RTDs are in
stator teeth with 7 spacers, 7 RTDs between the coil sides in stator slots with 7 spacers and
3 RTDs are there in the stator core with spacers. The location of RTDs is in three phase‟s
i.e. in the centre of machine, in each region of machine and midway between them. The
detectors in the stator slots are distributed uniformly in all three phases. Measurement of
temperature of Hydrogen cooling water for Hydrogen coolers & metals is as:
Six RTDs are provided at the inlets of each of six individual Hydrogen cooler elements for
measurement of temperature of Hydrogen, similarly Six RTDs are provided at the outlets
also. One RTD along-with one spacer is provided in the lower part of stator frame for
measurement & signalization of hot Hydrogen. Six RTDs are provided at outlets of each of
six individual Hydrogen Cooler elements for measurement of temperature of cooling water
at the outlet.
8.1.11 MEASUREMENT OF BEARING TEMPERATURE
Two RTDs are provided in the shelves of Turbo-Generator for measurement of
signalization of the bearing metal cap. All the terminals of RTDs are brought out to a
common terminal board located on the stator frame.
8.1.12 HYDROGEN COOLERS
Three Hydrogen Coolers each comprising of two individual units are mounted inside
the stator frame. The inlet and outlet of cooling water from both of machine i.e. from non-
driving side as well as turbine side. The Clearing of the individual cooler element can be
carried out from both ends of the Generator even during operation. The assembly of
individual cooler elements in stator frame is however carried out only from the non-driving
side.
8.2 ROTOR
Rotor shaft consists of single piece alloy steel forging of high mechanical and
magnetic properties performance test includes :-
1. Tensile test on specimen piece.

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2. Surface examination.
3. Sulfur prist tests.
4. Magnetic crack detection.
5. Visual examination of bore.
6. Ultrasonic examination.
Slots are milled on the rotor gorging to receive the rotor winding. Transverse slots
machined in the pole faces of the rotor to equalize the moment of inertia in direct and
quadrilateral axis of rotor with a view minimizing the double frequency.
8.2.1 VIBRATION OF ROTOR
The fully brazed rotor is dynamically balanced and subject to 120 % over speed test
at the work balancing tunnel so as to ensure reliable operation.
8.2.2 ROTOR WINDINGS
Rotor winding is of direct coil type and consists of parallel strips of very high
conductivity Silver Bearing Copper, bent on edge to form coil. The coils are placed in
impregnated glass, laminated short shells; using glass strips inter turn insulation and will be
brazed at the end to form continuous winding. The complete winging will be packed at high
temperature and pressed to size by heavy steel damping rings. When the windings have
cooled, heavy dove tail wedges of non-magnetic materials will seal the insulation at the top
of slot portion. The cooling medium hydrogen gas will be brought in direct contact with
copper by means of radial slots in embedded portion. Treated glass spacers inserted
between the coils and solid ring prevent lateral movement of coil overhang. The formation
and description of glass spacer is such as to leave ample space for ventilation.
8.2.3 BEARINGS
The bearings are self-aligned & consist of slip steel shells linked with special bearing
metal having very low coefficient of friction. The bore is machined on an elliptical shape so
as to increase the mechanical stability of the rotor. The bearings are pressure lubricated

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]
from the turbine oil supply. Special precautions are taken to prevent oil & oil vapor from
shaft seals and bearing along the shaft. The circulation of shaft current is liable to damage.
The bearing surface is protected by insulation so placed that the bearings, seals &
necessary pipes are inclined from the frame.
8.2.4 SLIP RINGS
The slip rings are made of forged steel. They are located at either side of Generator
Shaft. The slip ring towards the exciter side is given +ve polarity initially. They have helical
grooves and skewed holes in the body for cooling purpose by air. Calibrated mica is first
built up to required thickness on the shaft where slip rings are located. The slip rings are
insulated from the rotor shaft. Excitation current is supplied to the rotor winding. Through
the slip rings, which are connected to the winding. On one end and to the slip ring on the
other end with insulated (terminal) studs passing „though‟ the radial holes in the rotor shaft.
The terminal studs at both the ends of excitation leads are fitted gas cat seals to prevent
leakage.
8.2.5 BUSH GEAR ASEMBLY
Generator bushes are made from the various compositions of natural graphite and
binding material. They have a low coefficient of friction and are self lubricating. The
brushes are provided with a double flexible copper or pigtails. A helical spring is mounted
rapidly over each bush so that pressure is applied on the centerline of bush. A metal cap is
riveted to the brass bead and is provided with a hole to maintain the position of the spring
plug. Several brush holder, each carrying on brush in radial position are fixed to a silver
plated copper studs mounted on the collecting arm concentric with each slip rings. The
collecting arm is made out of a copper strip.
8.2.6 DRYING OF WINDING
Generator stator bars are insulated with mica insulation, which is homogeneous in
nature and practically impervious to moisture, and reduce time required to draught. The
insulation resistance of the stator phase winging against earth and with reference to other
phases under hot condition shall not be less than the value obtained automatically.

[40
]
Rin
U
=
=
µ/(s/100+1000) m 52
rated winding Voltage under test.
Rin = insulation resistance under hot conditions
Rated o/p of turbo generator.
The insulation resistance of entire excitation system circuit. In hot condition must not fall
below 0.5 m 52. The insulation resistance in calculated as per the formula:
Rin = Rv (U1 +U2) / (U-1)
Rin = Insulation resistance of exciter ()
Rv = Internal resistance of voltmeter ()
U1 = Voltage measured btw. Slip ring & shaft/ earth (volts).
When starting the drying process, the winding insulation resistance will usually decrease
when the drying process becomes effective; the insulation will gradually increase.
Figure 8.1 CROSS SECTIONAL VIEW OF TURBO GENERATOR

[41
]
CHAPTER – 9
COOLING SYSTEM
9.1 INTRODUCTION:-
In KSTPS hydrogen cooling system is employed for generator
cooling. Hydrogen is used for cooling medium primarily because of its superior cooling
properties & low density. Thermal conductivity of hydrogen 7.3 times of air. It also has
higher transfer co-efficient . Its ability to transfer heat through forced convection is about
75% better than air. Density of hydrogen is approx. 7/14 of the air at a given temperature
and pressure. This reduces the wind age losses in high speed machine like turbo-
generator. Increasing the hydrogen pressure the machine improve its capacity to absorb
& remote heat. Relative cooling properties of air and hydrogen are given below :-
1) Elimination of fire risk because hydrogen will not support combustion.
2) Corona discharge is not harmful to insula. since oxidation is not possible.
3) Smooth operation of machine in view of vertical elimination of wind age noise & the
use of heavy gas light enclosure and dirty probe casing.
At pressure 0.035 atm. of hydrogen heat carrying capacity is 1. But at
2.0atm. of hydrogen heat carrying capacity is 1.95 to overcome the serious possibility of
hydrogen explosion with in the machine and to ensure the safety of operation purity of
hydrogen on the generator. Casing must be maintained as high as possible. The purity of
hydrogen should be 98% above but should not be less than 98% . In case of hydrogen
purity drops below 98% an alarm is provided.
9.2 HYDROGEN DRYERS:-
Two nos. of dryers are provided to absorb the hydrogen in the
Generator. Moisture in this gas is absorbed by silica gel in the dryer as the absorbed gas
passes through it. The satural of silica gel is indicated by change in its color from blue to
pink. The silica gel is reactivated by heating. By suitable change over from drier to the
other on un-interrupted drying isachieve.

Fig : 9.1 HYDROGEN COOLED ALTERNATOR
[42]

[43
]
CHAPTER - 10
EXCITATION SYSTEM
The electric power Generators requires direct current excited magnets for its field
system. The excitation system must be reliable, stable in operation and must response
quickly to excitation current requirements. When excitation system response is controlled
by fast acting regulators, it is chiefly dependent on exciter. Exciter supply is given from
transformer and then rectified.
10.1 Function of excitation system:-
The main function of excitation system is to supply required
excitation current at rated load condition of turbo Generator. It should be able to adjust the
field current of the Generator, either by normal controller automatic control so that for all
operation & between no load and rated load. The terminal voltage of the system machine
is maintained at its value. The excitation system makes contribution improving power
system stability steady state condition. The excitation system that are commonly termed
quick response system and have following principal feature :- Exciter of quick response &
high voltage of not less than 1.4 times the rated filed voltage and nominal exciter response
of minimum 0.5.
10.2 Type of Excitation System:-
There have been many developments in excitation system design. There has been continuing reac
makes turbo-generator I. Conventional DC excitation system. Brushes excitation system.
10.3 STATIC EXCITATION SYSTEM :-
In KSTPS static excitation system is provided it mainly consists of the following:-
1) Rectifier transformer.
2) Nos. of thyristor converters.
3) An automatic voltage regulator (AVR).
4) Field suppression equipment.

[44
]
5) Field flashing equipment.
10.4 GENERAL ARRANGEMENT:-
In the excitation system the power required for excitation of
Generation are tapped from 11 KV bus ducts through a step down rectifier transformer.
After rectification in thermistor, converter, the DC power is fed to the Generator field
winding through a field breaker. The AVR control the o/p from thyristor converter by
adjusting the firing angle depending upon Generator voltages. The field flashing system
facilitates initial built up of the Generator voltage from the static AC or DC supply.
10.4.1 RECTIFIER TRANSFORMER :-
This transformer steps down the bus voltage 11 KV to 640 V and has a
rating of 1360 KVA. It is dry type, it is however provided with current relays and two
temperature sensors.
10.4.2 A THYRISTOR CONVERTOR :-
The thyristor panel and are intended for controlled
rectification of AC Input power. 6. Thyristor converter are connected in parallel each rates
for continuous current o/p of 20 % of the rated capacity i.e. 20 % reserve. Each thyristor
converter consists of 6 thyristor connected in 3-3 , full wave, 6-pulse bridge from and they
are cooled by fans provided with a fuse for protection against short circuit.
10.4.3 AUTOMATIC VOLTAGE CONTROLS :-
The AVR is transistorized thyristor controlled equipment
with very fast response. The AVR is also having provision of stator and rotor currents
limits and load angle limits for optimum utilization of lagging and leading reactive
capacities of generator.
10.4.4 FIELD SUPRESSION EQUIPMENT:-
The field equipment consists of a field breaker with discharge resistors. The field breakers
have 4 main breaking contacts and two discharge contacts, which close before main
contact break.
(a) A very fast response.
(b) Extremely reliable in view of static components.

[45
]
(c) Low maintenance cost.
(d) High efficiency.
(e) Fast field suppression through field and discharge resistance as well as through
Thyristor Bridge, feeding the Generator field.
10.5 OPERATION:-
After bringing the speed to operation speed say 3000 r.p.m. , the voltage
is slowly built up with the help of excitation system. This action is taken for synchronizing
the Generator.
10.5.1 SYNCHRONIZING:-
For synchronizing the Generator to the grid system 5 condition of equality
have to be satisfied. These are (I)_Voltage (II) Frequency (III) Phase displacement (IV)
Phase sequence (V) Wave form. Wave form and phase sequence of the Generator are
determined at the design of each connection SYNCHRONIZING of the generator.

[46
]
CHAPTER – 11
WATER TREATMENT PLANT
The principle problem in high pressure boiler is to control corrosion
and steam quality. Internal corrosion costs power station crores of rupees in repair without
strict control impurities in steam also form deposit over turbine blades and nozzles. The
impurities present in water are as follows :-
1) Un-dissolved and suspended solid materials.
2) Dissolved slats and minerals.
3) Dissolved gases
4) Other minerals ( oil, acid etc.).
5). a) Turbidity & Sediment.
b) Silica.
c) Micro Biological.
d) Sodium & Potassium Salt.
e) Dissolved Sales Minerals.
6). a) O2gas.
b) CO2 gas.
11.1 D.M. PLANT:-
In this plant process water is fed from all these dissolved salts.
Equipment for demineralization cum softening plant is supplied and erected by M/s.
Wanson (India) Ld., Pune. This plant consists of two streams each stream with activated
carbon filter, weak acid , cation exchanger and mixed bed exchanger. The filter water to
DM plant through 250 dia. header from where a heater top off has been taken to softening
plant. Two filtered water booster pumps are provided on filtered water line for meeting the
pressure requirement in DM Plant.
Sodium Sulphate solution of required strength is dosed
into different filtered water by mean of dosing pump to neutralize chlorine prior to activated
carbon filter. When water passed an activated carbon filter will remove residual chlorine

[47
]
from water. Provision is made for back washing the activated carbon filter. When
pressure drop across filter exceeds a prescribed limit from the activated carbon filter the
works acid cation unit. The deception water the weak base anion exchanger unit water
then enters de-gasified unit where free CO2 is scrubbed out of water by upward counter
flow of low pr. air flow through degasified lower and degassed water is pumped to strong
base exchanger ( anion exchanger).
Arrangement for dosing ammonia solution into de-mineralized water after mixed
bed unit has been provided p+1
correction before water is taken in de-condensate transfer
pump the DM water to unit condensor as make up.
11.2 C.W. PLANT:-
Circulating water pump house has pumps for condensing the
steam for condensor. Five pumps are used for condensing Unit No.1 & 2 and after
condensing this water is discharged back into the river. Each pump has capacity of 8275
M3
/Hr, and develop pressure about 1.94 Kg./Cm2
.Three seal water pump are used for
sealing circulating water pump shaft at pr. 4.5 kg./cm2
.
Two pump for unit 1 & 2 with one stand by is used for supplying raw water to
chlrofied chemical dosing is tone between and chlorified water is taken through main line.
From main line water passes through filter bed to filter the water. Chlorified water is
pumped to 42 m elevation by two pumps of capacity 270 M3
/Inch at discharge pressure of
6.9 Kg./Cm2
. At 42 M elevation the water is stored in tank and used for cooling the oil
coolers and returned back to river. Oil coolers are situated on ground and there are no. of
tress for each unit.
11.3 B.C.W. PUMP HOUSE:-
Filter water after demineralization is used for bearing
cooling from BCW pump house after passing through strainer and heat exchanger it enters
at 30-32o
C and leave exchanger at 38o
C. The raw water used in ash handling plant and
remaining quantity is stored in sumps of BCW Pump House. From here the water is
pumped to CW Pump by TWS (Traveling water screens) pumps are run by motors of 90
KW and has a capacity of 240 Cum/hr/pump at pressure of 5 kg/cm2
. BCW here stand for
water used for cooling oil used for cooling the bearing. In CW pump house water is
discharged from nozzle and impinged for traveling water screens for cleaning it.

[48
]
CHAPTER 12
CONTROL ROOM
12.1 MAIN CONTROL ROOM
In control room various controls are provided simultaneously various measurement
are made various relays are provided here. Instrumentation Limited Kota is major supplier
of apparatus.
There is one unit control from which two adjacent unit of 110 MW each can be
controlled. In addition are local panels at the boilers, turbo sets and boiler feed pumps.
The operation of unit is basically controlled from unit control room.
The operation of various rents and chain are done locally as per requirement. The
unit control room has a set of parameters panel for indicating or recording parameter of
boilers or turbo sets.
The parameters recorded in control room included per pr. and temp. of line steam,
reheat steam , feed water, fuel oil flow, mill outlet temp. ,mill differential , turbine speed,
control valve operation, turbine shaft , axial shaft , back pressure in condenser , metal
temperature etc. There is a data logger to ensure accurate lagging of essential data.
The VCB also control panel for one generator and contains exciter synchronizing
arrangement. The unit control room also houses most of electronic regulator, relay,
recorders and other devices in near side of room.
The scheme of control and instruction is provided to control the parameters and
safe operation of equipment. Automatic control is provided for combustion for feed water
regulation and reheat temp. The combustion control is designed to inlet maintain the
desired steam pressure at turbine only variation thereof utilized to very fuel input to the
boiler w.r.t. steam pressure. Ratio steam flow maintained automatically.
The feed water regulation is based on impulses from drum level, feed water flow to
boiler and steam flow for the boiler.

[49
]
Super heater temp. counted with feed water spray. The furnace draft control of draft fan.
The boiler oil system is provided with itself control for ignition control and also provided
with safety interlock to prevent operation under low oil pressure and temperature.
12.2 CONTROL PANEL I
12.2.1 FAN CONTROL DESK
a) Induced draft fan ( 3 Nos.) at full load and 2 Induce Draft Fans Run.
b) Forced draft fan ( 2 Nos.).
c) Primary Air Fan (3 Nos.) at full load.
d) Furnace Pressure (- 5 to 10 wcl).
e) Primary Air Header Pressure (750-800 mm. level wcl.)
f) FO Wind box pressure or wind box differential pressure.
12.3 CONTROL PANEL II
12.3.1 FUEL CONTROL DESK
a) Coal, oil flow.
b) Oil pressure.
c) Temp. of mill (inlet & outlet).
d) Flow of air.
e) Differential Pressure of mill.
12.4 CONTROL PANEL III
12.4.1 STEAM & WATER DESK
a) Drum Level Control

[50
]
b) Flow of steam & water.
c) Pressure of Steam & Water.
d) Temp. of steam and water.
12.5 CONTROL PANEL IV
12.5.1 TURBINE DESK
a) Pressure Control.
b) Load Control.
c) Speed Control.
d) Effectors, Control Values, Stop Values, Deaerators.
12.6 CONTROL PANEL V
12.6.1GENRATOR CONTROL PANEL
a) Voltage Current MVAR.
b) Stator Rotor Temp.
c) For Stator Cooling (a) H2 pressure. b) H2O pressure.
Fig : 12.1 control room

[51
]
CHAPTER -13
PROTECTION
1. Field Protection.
2. Pole Slipping.
3. Plane Overload Protection.
4. Inter-turn Fault
5. Negative Phase Sequence Protection.
6. Reverse Power Protection.
7. Forward Power Protection.
8. Under Frequency & Over Frequency Protection.
9. Generator Voltage Protection.
10. Rotor Earth Fault Protection.
13.1 General Protection:
It is most important electrical equipment of many generating station. Tripping of
even a generating unit may cause overloading of associated machines and even to system
un-stability . The basis function of protection applied to generator is to reduce voltage to
minimum by rapid discrimination clearance of faults. Unlike other apparatus the opening
of C.B. to isolate faulty generator is not sufficient to prevent future damage.

[52
]
CHAPTER -14
SALIENT FEATURE OF K.S.T.P.S.
(1) Location KOTA(RAJASTHAN)
(2) Installed Capacity 1240MW
(3) Land Details
(a) Plant Area 204 Hectare
(b) Ash Dump Area 423 Hectare
(4) Cooling Water
(a)
Source Of Cooling
Water
Kota Barrage (Chambal River)
(b)
Method Of
Cooling:
i) Unit # 1 to 5 Once through Cooling System(Open Cycle)-1180 Cusecs
i) Unit # 6 to 7
Re-circulating through Cooling Tower - 18 Cusecs (Including
Consumptive use)
(5) Coal
(a) Type Bituminous Coal
(b) Linked Coal Mines SECL (Korea-Rewa & Korba) & NCL (Singrauli)
(c)
Average Ash
Content
28-32%
(6) Fuel Oil :
(a) Type Furnace Oil / HSD
(b)
Available Storage
Capacity
HSD - 3100 KL & FO - 18600 KL
(7) Steam Generator M/s. BHEL make
(8) Turbo Generator M/s. BHEL make
(9)
Coal Handling
Plant
(a)
Stock Yard
Capacity
5,00,000 MT
(b) Wagon Tipplers 5 Nos.
(c) Coal Crushers 10 Nos
(d) Conveyor System 1.595 Kms
(10)
Transmission
Lines
Power evacuation through 9 Nos. 220 KV outgoing feeders.
Further 2 Nos. of new 220 KV feeders are under construction

[53
]
Sanction Of Schemes (Stage I to V)
Stage Unit No. Capacity(MW) Synchronising Date Cost(Rs.Crore)
I 1 110 17.1.1983 143
2 110 13.7.1983
II 3 210 25.9.1988 480
4 210 1.5.1989
III 5 210 26.3.1994 480
IV 6 195 31.7.2003 635
V 7 195 30.5 2009 880
Record Achievements
TOTAL STATION GENERATION _9891 MU(Highest since commissioning)
PLANT LOAD FACTOR _91.06 %
STATION AVAILABILITY _94.23 %
No. OF FORCED OUTAGES _6 Nos.(Lowest since commissioning)
SP. OIL CONSUMPTION U#3 _0.24 ml/Kwh(Lowest since commissioning)
SP. OIL CONSUMPTION U#7 _0.76 ml/Kwh(Lowest since commissioning)
DRY FLY ASH UTILISATION _99.40%(Highest since commissioning)
BOILER TUBE LEAKAGE UNIT # 7 _NIL (During Yr. 2010-11)
CONTINUOUS RUN 210 MW Unit # 4 _100 Days (Dt. 16.02.10 to 26.05.10)
STATION GENERATION (in a day) _30.895 MU(Highest in a day on 13.03.11)
STATION GENERATION (in a month) _30.895 MU (Highest in a day on 13.03.11)

[54
]
CONCLUSION
The first phase of practical training has proved to be quiet fruitful. It provided an
opportunity for encounter with such huge machines like wagon tippler .110 MW, 210 MW &
195 MW turbines and generators.
The architecture of the power plant the way various units are linked and the
way working of whole plant is controlled make the student realize that engineering is not
just learning the structured description and working of various machines, but the greater
part is of planning proper management.
It also provides an opportunities to lean low technology used at proper place
and time can cave a lot of labour e.g. wagon Tripler (CHP).But there are few factors that
require special mention. Training is not carried out into its tree sprit. It is recommended
that there should be some project specially meant for students where presence of
authorities should be ensured. There should be strict monitoring of the performance of
students and system of grading be improved on the basis of work done.
However training has proved to be quite fruitful. It has allowed an opportunity
to get an exposure of the practical implementation to theoretical fundamentals.

[55
]
REFERENCES
 http://www.mapsofindia.com/kota/industries/super-thermal-power-plant.html
 http://en.wikipedia.org/wiki/Thermal_power_station
 www.geocities.com
 http://www.energymanagertraining.com/power_plants/ThermalPowerPlants.htm
http://himaanshuderwal.blogspot.in/2013/06/at-kota-super-thermal-power-station.html
it’s easy to search me on Google then Facebook By Texting “Himanshu Derwal”
Email :- himanshuderwal@gmail.com
Contact number :- +9462815770
https://www.facebook.com/himaanshuderwal
BOOKS
 Electrical Power by J.B.Gupta
 Generation of Electrical Power by B.R.Gupta
 Power System by V.K.Mehta.
 Power System Design & Analysis by B.R.Gupta
 Steam & Gas turbines and Power Plant Engineering by R.Yadav

Project report of kota super thermal power plant

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