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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 Lab6.3.Automation Lab6.4.Pyrometry Lab6.5.Furnace Safety & Supervisory Lab

    6.6.Electronics Lab

    7. Ecological Monitoring Programme8. 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

    Fig. 5 Air Purge Level Measurement

    Fig. 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

    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 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.

    Figure 1

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    EVOLUTION OF NTPC

    NTPC was set up in 1975 with 100% ownership by the

    Government of India. In the last 30 years, NTPC has

    grown into the 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 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.

    NTPC is the largest power utility in India, accounting for about 20% of Indias

    installed capacity.

    1975

    1997

    2005

    2004

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    NTPC Limited

    Subsidiaries

    Joint Ventures

    NTPC Vidyut Vyapar

    Nigam Limited

    100%

    NTPC Electric Supply

    Co. Limited

    100%

    Pipavav Power

    Development Co. Ltd

    100%

    NTPC Hydro

    Limited

    100%

    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

    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 by coal feeders where it is pulverized and ground in

    the powered form. This crushed coal is taken away to the furnace through coal pipes

    with the 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 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. Water from the bottom ring header is divided

    to all the four sides of the furnace. Due to heat density difference the water rises up

    in the water 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 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 the various super heaters and finally through air pre

    heaters and goes to electrostatic precipitators where the ash particles are extracted.

    This ash is mixed with the water to from slurry is pumped to ash period. The steamfrom 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.

    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 high pressure cylinder of turbines, where it passes through

    the ring of blades fixed to the cylinder wall. These act as nozzles and direct the steam

    into a 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 the automation of a

    process / plant, such as a power station. In this last application, 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.

    During stable generation of power, the modulating portion of the automation 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 and switches ON or OFF process pieces, to automatically bring the individual

    processes in an optimally coordinated way to the new desired load demand. This load

    transfer is executed according to pre- programmed adaptively controlled load

    gradients and in a safe way.

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    AUTOMATION: THE BENEFITS

    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 load consumption during plant start- up,shut-down and operation, via:

    Faster plant start-up through elimination of control errors creating delays. Faster sequence of control actions compared to manual 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 to the generated power output.

    2. Ensure and maintain plant operation, even in case ofdisturbances in the control system, via:

    Coordinated ON / OFF and modulating control switchover capability froma sub process to a redundant one.

    Prevent sub-process and process tripping chain reaction following aprocess component trip.

    3. Reduce plant / process shutdown time for repair andmaintenance as well as repair costs, via:

    Protection of individual process components against overstress (in a stableor unstable plant operation).

    Bringing processes in a safe stage of operation, where process componentsare protected against overstress

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    CONTROL AND MONITORING MECHANISMS

    There are basically two types of Problems faced in a Power Plant 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.

    Monitoring of all the parameters is necessary for the safety of both:

    Employees Machines

    So the Parameters to be monitored are :

    Speed Temperature Current Voltage Pressure Eccentricity Flow of Gases Vaccum Pressure Valves Level Vibration

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    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:

    1. MANOMETRY LAB2. PROTECTION AND INTERLOCK LAB3. 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

    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 and amplified. 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 is mounted 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 difference in pressure across the two limbs.

    BOURDEN PRESSURE GAUGE :Its an oval section tube. Its one end is fixed. It isprovided with a pointer to indicate the pressure on a calibrated 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 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 will support calcium

    of Mercury approximately 30 inches in a U-tube provided a good vacuum is

    maintained in one limb. Ifa U-tube is replaced with a straight limb about 35 inches

    long, one end closed, then being filed with clean, dry mercury and then inverted in a

    container of mercury open to the atmosphere, the mercury would fall in the tube

    forming a good vacuum above it.

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    Fig.2 Fortin.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 tubeis 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 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 of oval 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 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 Bourden tube is not suitable and where power is required. By making the ovaltube in the form of a spiral an enlarged movement of the free end is achieved 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.

    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 Pressure Gauge

    Measurement of Level

    Direct Methods

    'Sight Glass' is used for local indication on closed or open vessels. A sight glass is a

    tube of toughened glass connected at both ends through packed unions and vessel.

    The liquid level will be the same as that in the vessel. Valves are provided for

    isolation and blow down.

    "Float with Gauge Post" is normally used 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.

    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.

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    Bourden Pressure Gauge A Bourdon pressure gauge calibrated in any fact head is

    often connected to a tank at or near the datum level. "Mercury Manometer" is used

    for remote indication of liquid level. The working principle is the same as that 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 the liquid in the vessel, andwhere 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 for remote level indication in open tanks or docks etc. A

    pressure change created by the movement of a diaphragm is proportional to a change

    in liquid level above the diaphragm. This consists of a cylindrical box with a rubber or

    plastic diaphragm across its open end as the level increases .the liquid pressure on the

    diaphragm increases and the air inside is compressed. This pressure is transmitted via

    a 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 this type, 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 a capillary 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 is still full, a spring loaded valve automatically shutting of

    the tapping point.

    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

    provided for all the equipments. Tripping can be considered as the series of

    instructions connected through OR GATE. When a fault occurs and any 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 circuitsby 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 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 full capacity normal current ratings

    are assured for the long time. b) The conductivity of the silver is unimpaired by thesurges of the current 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.

    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 carrying contacts, one movable and other fixed.

    When a fault occurs the contacts separate and are is stuck between them. There are

    three types of - MANUAL TRIP - THERMAL TRIP - SHORT CIRCUIT TRIP

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    AUTOMATION LAB

    This lab deals in automating the existing equipment and feeding routes. Earlier, the

    old technology dealt with only (DAS) Data Acquisition System and came to be known

    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. 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 having multiple applications. Another point is the universality of the

    supply, the laws of electronic state that it can be any where between 12V and 35V in

    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 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 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 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

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    coeficient of linear expansion wil expand more causing the sandwich to curl up or

    down depending on the position of this metal.

    Fig.7 Helical Bi-Metallic Strip

    Liquid in Glass Thermometers : The coeficient of cubical expansion of

    mercury is about eight time greater that of glass. Therefore, a glass container holding

    mercury, when heated, wil expand far less than the mercury it contains. At a high

    temperature the mercury will occupy a greater fraction of the 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 glass thermometer beyond this point the

    top end of a thermometer bore opens into a bulb which is many times larger in

    capacity than the bore. This bulb plus the bore above the mercury, is then filed with

    nitrogen or carbon dioxide gas at a sufficiently high pressure to prevent boiling at the

    highest temperature to which the thermometer may be used.

    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 common and simplest type Spiral type : More sensitive and used where compactness is necessary Helical Type : Most sensitive and compact.Pointer may be mounted direct on

    end of helix which rotates, thus eliminating backlash and lost motion.

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    Fig.8 Liquid Expansion Thermometer with C Bourden

    (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 isL shaped thermometer which is designed to reach all inaccessible places.

    Fig.9 Bulb Forms

    A. PLAIN BULB B. UNION BULB; C. POCKET BULB D. WALL MOUNTING

    E. SHORT COtL. F. LONG COIL; G. FINNED STRAIGHT H.WATCH CAPSULE

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    2) ULTRA VIOLET SENSOR : This device is used in furnace and it measures the

    intensity of ultra violet 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 junctions at different temperature. Then the emf is induced in the

    circuit due to the flow of electrons. This is an important part in the plant.

    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 (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 with relation to temperature change, and that at constant volume the

    pressure changes in relation to temperature. Therefore, if a bulb, capillary and

    bourdon tube enclose a certain volume of gas and the both of that assembly is

    subjected to heat, or change of the same, the changes of pressure, effected by the heat,

    within the system, can be directly related to temperature. The later will, of course be

    shown though the movement of the free end of the bourdon tube.

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    FURNACE SAFETY AND SUPERVISORY SYSTEM LAB

    This lab has the responsibility of starting fire in the furnace to enable the burning of

    coal. For first stage coal burners are in the front and 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 degree

    Celsius 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 ultra violet 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 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 employed that is feeder mills

    are not fed directly from coal but are fed from three feeders but are fed from

    pulverized coalbunkers. The furnace can 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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    ELECTRONICS LAB

    This lab undertakes the calibration and testing of various cards. It houses various

    types of analytical instruments like oscilloscopes, integrated circuits, cards auto

    analyzers 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 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 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 in

    average rainfall, decrease in waste land etc. In general, the studies, as such, 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 services.

    NTPC has adopted user friendly policy guidelines on ash utilisation.

    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 Government Authorities. Necessary techno-

    managerial assistance is given 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 adoption of best international practices on environment,

    occupational health and safety areas. The organization has pursued the

    Environmental Management System (EMS) ISO 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 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

    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 & Facilities

    Environmental Institutional Set-up

    Environment Reviews

    Up gradation & retrofitting of Pollution Control Systems