ntpc 1 (1)
TRANSCRIPT
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INDEX
1.Acknowledgements2.About the company2.1. NTPC group2.2. Evolution of NTPC2.3. Electricity from Coal
3.Definition of Automation4.Benefits of Automation5.Control Mechanisms6.Control & Instrumentation6.1. Manometry Lab6.2.
Protection & Interlock Lab
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6.3. Automation Lab6.4.
Pyrometry Lab
6.5.Furnace Safety & Supervisory
Lab
6.6.Electronics Lab
7.Ecological MonitoringProgramme
8.Ash Utilization9.Environment Management &
safety System
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List of Figures
Fig. 1 Installed Capacity &
its Growth
Fig. 2 Fortin Barometer
Fig. 3 Typical
Arrangement of Bourdon Gauge
Fig. 4 Dewrance Critical
Pressure Gauge
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Fig. 5 Air Purge Level
MeasurementFig. 6 Rod Type
Thermostat
Fig. 7 Helical Bi-Metal
Strip
Fig. 8 Liquid Expansion
Thermometer with C Bourden
Fig. 9 Bulb Forms
Fig.10 Thermocouple
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ABOUT THE COMPANY
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Corporate Vision:
A world class integrated power
major, powering Indias growth,
with increasing global presence
Core Values:
B-Business Ethics
C-Customer Focus
O-Organizational & Professional
pride
M-Mutual Respect and Trust
I- Innovation & Speed
T-Total quality for Excellence
NTPC Limited is the largest thermal
power generating company of India.
A public sector company, it was
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incorporated in the year 1975 to
accelerate power development in the
country as a wholly owned company
of the Government of India. At
present, Government of India holds
89.5% of the total equity shares of
the company and the balance 10.5%
is held by FIIs, Domestic Banks,
Public and others. Within a span of
31 years, NTPC has emerged as a
truly national power company, with
power generating facilities in all the
major regions of the country.
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Figure 1
EVOLUTION OF NTPC
NTPC was set up in 1975
with 100% ownership bythe Government of India.
In the last 30 years,
NTPC has grown into the
1975
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largest power utility in
India.
In 1997, Government of
India granted NTPC
status of Navratna
being one of the nine
jewels of India,
enhancing the powers to
the Board of Directors.
NTPC became a listed
company with majority
1997
2004
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Government ownership
of 89.5%.
NTPC becomes third
largest by Market
Capitalisation of listed
companies
The company
rechristened as NTPC
Limited in line with its
changing business
portfolio and transform
itself from a thermal
power utility to an
integrated power utility.
2005
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NTPC is the largest power utility inIndia, accounting for about 20% of
Indias installed capacity.
NTPC Limited
Subsidiaries
NTPC Vidyut Vyapar
Nigam Limited
100%
NTPC Electric Supply
Co. Limited
100%
Pipavav Power
Development Co. Ltd
100%
NTPC Hydro
Limited
100%
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Joint Ventures
Utility Powertech
Limited
50%
NTPC Alstom Power
Services Pvt. Limited
50%
Bhilai Electric Supply
Co. Pvt. Limited
50%
NTPC-SAIL Power
Company Pvt. Limited
50%
Ratnagiri Gas &
Power Private Ltd
28.33%
PTC India Limited
8%
NTPC Tamilnadu
Energy Co. Limited
50%
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GENERATION OF ELECTRICITY
FROM COAL
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Coal from the coal wagons is
unloaded with the help of wagon
tipplers in the C.H.P. this coal is
taken to the raw coal bunkers with
the help of conveyor belts. Coal is
then transported to bowl mills bycoal feeders where it is pulverized
and ground in the powered form.
This crushed coal is taken away to
the furnace through coal pipes withthe help of hot and cold mixture P.A
fan. This fan takes atmospheric air,
a part of which is sent to pre
heaters while a part goes to the mill
for temperature control.
Atmospheric air from F.D fan in the
air heaters and sent to the furnace
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as combustion air. Water from
boiler feed pump passes through
economizer and reaches the boiler
drum . Water from the drum passes
through the down comers and goes
to the bottom ring header. Waterfrom the bottom ring header is
divided to all the four sides of the
furnace. Due to heat density
difference the water rises up in thewater wall tubes. This steam and
water mixture is again taken to the
boiler drum where the steam is sent
to super heaters for super heating.
The super heaters are located inside
the furnace and the steam is super
heated (540 degree Celsius) and
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finally it goes to the turbine. Fuel
gases from the furnace are
extracted from the induced draft
fan, which maintains balance draft
in the furnace with F.D fan. These
fuel gases heat energy to thevarious super heaters and finally
through air pre heaters and goes to
electrostatic precipitators where
the ash particles are extracted. Thisash is mixed with the water to from
slurry is pumped to ash period. The
steam from boiler is conveyed to
turbine through the steam pipes
and through stop valve and control
valve that automatically regulate
the supply of steam to the turbine.
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Stop valves and controls valves are
located in steam chest and governor
driven from main turbine shaft
operates the control valves the
amount used. Steam from
controlled valves enter highpressure cylinder of turbines, where
it passes through the ring of blades
fixed to the cylinder wall. These act
as nozzles and direct the steam intoa second ring of moving blades
mounted on the disc secured in the
turbine shaft. The second ring turns
the shaft as a result of force of
steam. The stationary and moving
blades together.
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AUTOMATION : THE DEFINITION
The word automation is widely used
today in relation to various types of
applications, such as office
automation, plant or process
automation.
This subsection presents the
application of a control system for
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the automation of a process / plant,
such as a power station. In this lastapplication, the automation actively
controls the plant during the three
main phases of operation: plant
start-up, power generation in stable
or put During plant start-up and
shut-down, sequence controllers as
well as long range modulating
controllers in or out of operation
every piece of the plant, at the
correct time and in coordinated
modes, taking into account safety as
well as overstressing limits.
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During stable generation of power,
the modulating portion of theautomation system keeps the actual
generated power value within the
limits of the desired load demand.
During major load changes, the
automation system automatically
redefines new set points andswitches ON or OFF process pieces,
to automatically bring the individual
processes in an optimallycoordinated way to the new desired
load demand. This load transfer is
executed according to pre-
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programmed adaptively controlled
load gradients and in a safe way.
AUTOMATION: THE BENEFITS
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The main benefits of plant
automation are to increase overall
plant availability and efficiency. The
increase of these two factors is
achieved through a series of features
summarized as follows:
1. Optimisation of house loadconsumption during plant start-
up, shut-down and operation,
via:
Faster plant start-up throughelimination of control errors
creating delays.
Faster sequence of controlactions compared to manual
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ones. Figures 1 shows the
sequence of a rapid restart
using automation for a typical
coal-fired station. Even a well-
trained operator crew would
probably not be able to bring
the plant to full load in the
same time without considerable
risks.
Co-ordination of house load tothe generated power output.
2. Ensure and maintain plantoperation, even in case of
disturbances in the control
system, via:
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Coordinated ON / OFF andmodulating control switchover
capability from a sub process to
a redundant one.
Prevent sub-process andprocess tripping chain reaction
following a process component
trip.
3. Reduce plant / processshutdown time for repair and
maintenance as well as repair
costs, via:
Protection of individual processcomponents against overstress
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(in a stable or unstable plant
operation).
Bringing processes in a safestage of operation, where
process components are
protected against overstress
CONTROL AND MONITORING
MECHANISMS
There are basically two types of
Problems faced in a Power Plant
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Metallurgical
Mechanical
Mechanical Problemcan be related
to Turbines that is the max speed
permissible for a turbine is 3000 rpm
, so speed should be monitored and
maintained at that level
Metallurgical Problem can be view
as the max Inlet Temperature for
Turbile is 1060 oC so temperature
should be below the limit.
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Monitoring of all the parameters is
necessary for the safety of both:
EmployeesMachines
So the Parameters to be monitored
are :
SpeedTemperatureCurrentVoltagePressure
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Eccentricity
Flow of GasesVaccum PressureValvesLevelVibration
CONTROL AND INSTRUMENTATION
This division basically calibrates
various instruments and takes care
of any faults occur in any of the
auxiliaries in the plant. It has
following labs:
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1. MANOMETRY LAB2. PROTECTION AND INTERLOCK
LAB
3. AUTOMATION LAB4. WATER TREATEMENT LAB5. FURNACE SAFETY
SUPERVISORY SYSTEM(FSSS)6. ELECTRONICS TEST LAB
This department is the brain of the
plant because from the relays to
transmitters followed by the
electronic computation chipsets and
recorders and lastly the controlling
circuitry, all fall under this.
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MANOMETRY LAB
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TRANSMITTERS: It is used for
pressure measurements of gases
and liquids, its working principle is
that the input pressure is converted
into electrostatic capacitance and
from there it is conditioned andamplified. It gives an output of 4-20
ma DC. It can be mounted on a pipe
or a wall. For liquid or steam
measurement transmitters ismounted below main process piping
and for gas measurement
transmitter is placed above pipe.
MANOMETER: Its a tube which is
bent, in U shape. It is filled with a
liquid. This device corresponds to a
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difference in pressure across the
two limbs.
BOURDEN PRESSURE GAUGE :Its
an oval section tube. Its one end is
fixed. It is provided with a pointer to
indicate the pressure on acalibrated scale. It is of 2 types: (a)
Spiral type: for Low pressure
measurement.
(b) Helical Type: for High pressure
measurement.
Pressure Measurement
The U-Tube or Manometer: Liquid
contained in a tube bend in the form
of a U will respond to a difference in
pressure across the two limbs. A
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glass tube of uniform cross-
sectional-area is bent to form a U
and partly filed with a liquid of
known density 'd' p.s.l.
Measurement of Atmospheric
Pressure: Atmospheric pressure willsupport calcium of Mercury
approximately 30 inches in a U-tube
provided a good vacuum is
maintained in one limb. Ifa U-tube isreplaced with a straight limb about
35 inches long, one end closed, then
being filed with clean, dry mercury
and then inverted in a container ofmercury open to the atmosphere, the
mercury would fall in the tube
forming a good vacuum above it.
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Fig.2Fortin.Barometer
Single Tube Manometer This is
used for measuring low pressure and
for testing and recalibration low-
pressure instruments of al types. If
the ratio of the area of one tube is
considerably greater than other, then
practically al the movement takes
place in the smal manometer tube
and for al practical purposes only the
one limb need be read.
Kenotometer The low pressures
produced in steam condensers are
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usually measured in inches of
mercury, marking downwards from
atmospheric pressure. A high
working vacuum of 29.5 inches of
mercury is the same as an absolute
pressure of 0.5 inch of mercury, or
approximately 0.25 p.s.i (absolute).
One device for measuring the
absolute pressure in a condenser is
the Kenotometer.
Bourdon Pressure Gauge: This is
the most commonly used of al
pressure measuring devices. (Range
10- 80,000 p.s.i). Here, a tube ofoval section is bent into a circular
arc. One end is sealed and the other
end fixed to a solid block into which
the applied pressure is fed. The tube
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will "uncurl" as the pressure
(operating Force) increases, or will
'Curl up' as the vacuum increases; so
giving a movement of the free end
which is proportional to the change
in pressure. The Controlling Force
will depend upon the thickness of
the tube and the material from which
it is made.
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Fig.3 Typical
Arrangement of Bourden Gauge
SpecialTypes Of Pressure Gauges
Spiral Tube: This type is used for
low-pressure indication and
recording when a C-shaped Bourdentube is not suitable and where power
is required. By making the oval tube
in the form of a spiral an enlarged
movement of the free end isachieved and thus the tube becomes
more sensitive over pressure ranges
below 10 p.s.i.
Helical Tube: For higher pressures
the tube is wound in the form of a
helix and is often used in pressure
recorders. Range 0-80,000 p.s.i.
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Critical Type: This is used in boiler
houses to enable distant reading of
the steam pressure to be made to the
nearest 1 p.s.i over a range of say
15 p.s.i. The movement of a pressure
sensitive element is transmitted to a
pointer and scale via linkages, which
only allow the pointer to operate
over a selected range of pressure to
either side of the normal steam
pressure.
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Fig.4 Dewrance Critical PressureGauge
Measurement of Level
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Direct Methods
'Sight Glass' is used for localindication on closed or open vessels.
A sight glass is a tube of toughened
glass connected at both ends through
packed unions and vessel. The liquidlevel will be the same as that in the
vessel. Valves are provided for
isolation and blow down.
"Float with Gauge Post" is normallyused tor local indication on closed or
open vessels.
"Float Operated Dial" are used for
small tanks and congested areas. The
float arm is connected to a quadrant
and pinion which rotates the pointer
over a scale.
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Pressure operated types Since the
pressure acting on any area at the
bottom of a tank depends only upon
the depth and density of the
contained liquid, a measure of this
pressure is proportional to the liquid
level.
Bourden Pressure Gauge A
Bourdon pressure gauge calibrated
in any fact head is often connectedto a tank at or near the datum level.
"Mercury Manometer" is used for
remote indication of liquid level.
The working principle is the same asthat of a manometer one limp of a
U-tube is connected to the tank, the
other being open to atmosphere. The
manometer liquid must not mix with
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the liquid in the vessel, and where
the manometer is at a different level
to the vessel, the static head must be
allowed in the design of the
manometer.
'Diaphragm Type' is used forremote level indication in open tanks
or docks etc. A pressure change
created by the movement of a
diaphragm is proportional to achange in liquid level above the
diaphragm. This consists of a
cylindrical box with a rubber or
plastic diaphragm across its openend as the level increases .the liquid
pressure on the diaphragm increases
and the air inside is compressed.
This pressure is transmitted via a
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capillary tube to an indicator or
recorder incorporating a pressure
measuring element.
Sealed Capsule Type The
application and principle is the same
as for the diaphragm box. In thistype, a capsule filed with an inert
gas under a slight pressure is
exposed to the pressure due to the
head of liquid and is connected by acapillary to an indicator. In some
cases the capsule is fitted external to
the tank and is so arranged that it
can be removed whilst the tank isstill full, a spring loaded valve
automatically shutting of the tapping
point.
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Air Purge System This system
provides the simplest means of
obtaining an indication of level, or
volume, at a reasonable distance and
above or below, the liquid being
measured. The pressure exerted
inside an open ended tube below the
surface of a liquid is proportional to
the depth of the liquid.
Fig.5 Air Purge Level
Measurement
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PROTECTION AND INTERLOCK LAB
INTERLOCKING : It is basically
interconnecting two or more
equipments so that if one
equipments fails other one can
perform the tasks. This type of
interdependence is also created so
that equipments connected
together are started and shut down
in the specific sequence to avoid
damage. For protection of
equipments tripping are providedfor all the equipments. Tripping can
be considered as the series of
instructions connected through OR
GATE. When a fault occurs and any
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one of the tripping is satisfied a
signal is sent to the relay, which
trips the circuit. The main
equipments of this lab are relay and
circuit breakers. Some of the
instrument uses for protection are:1. RELAY : It is a protective device. It
can detect wrong condition in
electrical circuits by constantly
measuring the electrical quantities
flowing under normal and faulty
conditions. Some of the electrical
quantities are voltage, current,
phase angle and velocity.
2. FUSES: It is a short piece of metal
inserted in the circuit, which melts
when heavy current flows through it
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and thus breaks the circuit. Usually
silver is used as a fuse material
because: a) The coefficient of
expansion of silver is very small. As
a result no critical fatigue occurs
and thus the continuous fullcapacity normal current ratings are
assured for the long time. b) The
conductivity of the silver is
unimpaired by the surges of thecurrent that produces temperatures
just near the melting point. c) Silver
fusible elements can be raised from
normal operating temperature to
vaporization quicker than any other
material because of its
comparatively low specific heat.
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3. MINIATURE CIRCUIT BREAKER :
They are used with combination of
the control circuits to. a) Enable the
staring of plant and distributors. b)
Protect the circuit in case of a fault.
In consists of current carryingcontacts, one movable and other
fixed. When a fault occurs the
contacts separate and are is stuck
between them. There are threetypes of - MANUAL TRIP - THERMAL
TRIP - SHORT CIRCUIT TRIP
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AUTOMATION LAB
This lab deals in automating theexisting equipment and feeding
routes. Earlier, the old technology
dealt with only (DAS) Data
Acquisition System and came to beknown as primary systems. The
modern technology or the
secondary systems are coupled with
(MIS) Management Information
System. But this lab universally
applies the pressure measuring
instruments as the controlling force.
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However, the relays are also
provided but they are used only for
protection and interlocks. Once the
measured is common i.e. pressure
the control circuits can easily be
designed with single chips havingmultiple applications. Another point
is the universality of the supply, the
laws of electronic state that it can
be any where between 12V and 35Vin the plant. All the control
instruments are excited by 24V
supply (4-20mA) because voltage
can be mathematically handled with
ease therefore all control systems
use voltage system for
computation. The latest technology
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is the use of ETHERNET for control
signals.
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PYROMETERY LAB
The most important parameter in
thermal power plant is temperature
and its measurement plays a vital
role in safe operation of the plant.
Rise of temperature in a substance is
due to the resultant increase in
molecular activity of the substance
on application of heat; which
increases the internal energy of the
material
Temperature Measurement
. The change may be observed with
substance itself or in a subsidiary
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system in thermodynamic
equilibrium.
Fig.6 Rod Type Thermostat
Solid Rod Thermometers: A
temperature sensing - Controlling
device may be designed
incorporating in its construction the
principle that some metals expand
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more than others for the same
temperature range.
Bi-Metalic Strip : These are
composed of two metals, as the
name implies, whose coeficients of
linear expansion are dissimilar.These two metal plates are welded
together as a sandwich. When
heated, both metals expand, but the
metal with greatest coeficient oflinear expansion wil expand more
causing the sandwich to curl up or
down depending on the position of
this metal.
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Fig.7 Helical Bi-
Metallic Strip
Liquid in Glass Thermometers :
The coeficient of cubical expansionof mercury is about eight time
greater that of glass. Therefore, a
glass container holding mercury,
when heated, wil expand far lessthan the mercury it contains. At a
high temperature the mercury will
occupy a greater fraction of the
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volume of the container than it will
at a low temperature.
Under normal atmospheric
conditions mercury normally boils at
a temperature of (347C). To extend
the range of a mercury in glassthermometer beyond this point the
top end of a thermometer bore opens
into a bulb which is many times
larger in capacity than the bore. Thisbulb plus the bore above the
mercury, is then filed with nitrogen
or carbon dioxide gas at a
sufficiently high pressure to preventboiling at the highest temperature to
which the thermometer may be used.
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Mercury in Steel: The range of
liquid in glass thermometers
although quite large, does not lend
itself to al industrial practices. This
fact is obvious by the delicate nature
of glass also the position of the
measuring element is not always the
best position to read the result.
Types of Hg in Steel Thermometers
are:
Bourdon Tube : Most commonand simplest type
Spiral type : More sensitive andused where compactness is
necessary
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Helical Type : Most sensitive andcompact.Pointer may be mounteddirect on end of helix which
rotates, thus eliminating backlash
and lost motion.
Fig.8 Liquid Expansion
Thermometer with C Bourden
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(1) LIQUID IN GLASS
THERMOMETER : Mercury in the
glass thermometer boils at 340
degree Celsius which limits the
range of temperature that can be
measured. It is L shapedthermometer which is designed to
reach all inaccessible places.
Fig.9 Bulb Forms
A. PLAIN BULB B. UNION BULB; C.
POCKET BULB D. WALL MOUNTING
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E. SHORT COtL. F. LONG COIL; G.
FINNED STRAIGHT H.WATCH
CAPSULE
2) ULTRA VIOLET SENSOR : This
device is used in furnace and it
measures the intensity of ultraviolet rays there and according to
the wave generated which directly
indicates the temperature in the
furnace.
(3) THERMOCOUPLES : This device
is based on SEEBACK and PELTIER
effect. It comprises of two junctionsat different temperature. Then the
emf is induced in the circuit due to
the flow of electrons. This is an
important part in the plant.
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Fig.10
Thermocouple
(4) RTD (RESISTANCE
TEMPERATURE DETECTOR) : It
performs the function of
thermocouple basically but the
difference is of a resistance. In this
due to the change in the resistance
the temperature difference is
measured. In this lab, also the
measuring devices can be calibrated
in the oil bath or just boiling water
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(for low range devices) and in small
furnace (for high range devices).
Gas Thermometers : In Efect of
Heat, the volume of a gas. at
constant pressure, wil change withrelation to temperature change, and
that at constant volume the pressure
changes in relation to temperature.
Therefore, if a bulb, capillary andbourdon tube enclose a certain
volume of gas and the both of that
assembly is subjected to heat, or
change of the same, the changes ofpressure, effected by the heat, within
the system, can be directly related to
temperature. The later will, of
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course be shown though the
movement of the free end of the
bourdon tube.
FURNACE SAFETY AND
SUPERVISORY SYSTEM LAB
This lab has the responsibility ofstarting fire in the furnace to enable
the burning of coal. For first stage
coal burners are in the front and
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rear of the furnace and for the
second and third stage corner firing
is employed. Unburnt coal is
removed using forced draft or
induced draft fan. The temperature
inside the boiler is 1100 degreeCelsius and its height is 18 to 40 m.
It is made up of mild steel. An ultra
violet sensor is employed in furnace
to measure the intensity of ultraviolet rays inside the furnace and
according to it a signal in the same
order of same mV is generated
which directly indicates the
temperature of the furnace. For
firing the furnace a 10 KV spark plug
is operated for ten seconds over a
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spray of diesel fuel and pre-heater
air along each of the feeder-mills.
The furnace has six feeder mills
each separated by warm air pipes
fed from forced draft fans. In first
stage indirect firing is employedthat is feeder mills are not fed
directly from coal but are fed from
three feeders but are fed from
pulverized coalbunkers. The furnacecan operate on the minimum feed
from three feeders but under not
circumstances should any one be
left out under operation, to prevent
creation of pressure different with
in the furnace, which threatens to
blast it.
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67ELECTRONICS LAB
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This lab undertakes the calibrationand testing of various cards. It
houses various types of analytical
instruments like oscilloscopes,
integrated circuits, cards autoanalyzers etc. Various processes
undertaken in this lab are: 1.
Transmitter converts mV to mA. 2.
Auto analyzer purifies the sample
before it is sent to electrodes. It
extracts the magnetic portion.
ANNUNCIATION CARDS : They are
used to keep any parameter like
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temperature etc. within limits. It
gets a signal if parameter goes
beyond limit. It has a switching
transistor connected to relay that
helps in alerting the UCB.
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ECOLOGICAL MONITORING
PROGRAMME
NTPC has undertaken a
comprehensive Ecological
Monitoring Programme through
Satellite Imagery Studies covering
an area of about 25 Kms radius
around some of its major plants. The
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studies have been conducted through
National Remote Sensing Agency(NRSA), Hyderabad at its power
stations at Ramagundam, Farakka,
Korba, Vindhyachal, Rihand and
Singrauli. These studies have
revealed significant environmental
gains in the vicinity areas of the
project as a result of pursuing sound
environment management practices.
Some of these important gains
which have been noticed are
increase in dense forest area,
increase in agriculture area, increase
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in average rainfall, decrease in waste
land etc. In general, the studies, assuch, have revealed that there is no
significant adverse impact on the
ecology due to the project activities
in any of these stations. Such studies
conducted from time to time around
a power project have established
comprehensive environment status
at various post operational stages of
the project.
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USE OF WASTE PRODUCTS &
SERVICES -ASH UTILIZATION
Ash is the main solid waste which is
put into use for various products and
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services. NTPC has adopted user
friendly policy guidelines on ashutilisation.
In order to motivate entrepreneurs to
come forward with ash utilisation
schemes, NTPC offers several
facilities and incentives. These
include free issue of all types of ash
viz. Dry Fly Ash / Pond Ash /
Bottom Ash and infrastructure
facilities, wherever feasible.
Necessary help and assistance is also
offered to facilitate procurement of
land, supply of electricity etc from
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Government Authorities. Necessary
techno-managerial assistance isgiven wherever considered
necessary. Besides, NTPC uses only
ash based bricks and Fly Ash
portland pozzolana cement (FAPPC)
in most of its construction activities.
Demonstration projects are taken up
in areas of Agriculture, Building
materials, Mine filling etc. The
utilisation of ash and ash based
products is progressively increasing
as a result of the concrete efforts of
these groups.
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Environment Management,
Occupational Health and
SafetySystems:
NTPC has actively gone for adoptionof best international practices on
environment, occupational health
and safety areas. The organization
has pursued the Environmental
Management System (EMS) ISO
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14001 and the Occupational Health
and Safety Assessment System
OHSAS 18001 at its different
establishments. As a result of
pursuing these practices, all NTPC
power stations have been certified
for ISO 14001 & OHSAS 18001 by
reputed national and international
Certifying Agencies.
While deciding the appropriate
technology for its projects, NTPC
integrates many environmental
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provisions into the plant design. In
order to ensure that NTPC comply
with all the stipulated environment
norms, various state-of-the-art
pollution control systems / devices
as mentioned below have been
installed to control air and water
pollution.
Electrostatic Precipitators
Flue Gas Stacks
Neutralisation Pits
Low-NOX Burners
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Coal Settling Pits / Oil
Settling Pits
DE & DS System
Cooling Towers
Ash Dykes & Ash Disposal
systems
Ash Water Recycling
System
Dry Ash Extraction System
(DAES)
Liquid Waste Treatment
Plants & Management System
Sewage Treatment Plants &
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Facilities
Environmental Institutional
Set-up
Environment Reviews
Up gradation & retrofitting
of Pollution Control Systems