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    INDUSTRIAL

    TRAINING

    AT

    REPORT

    Submitted by,

    SOHAN RAM CHOUDHARY

    08M268

    MECHANICAL ENGINEERING

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    Introduction to NTPC Ltd.NTPC, the largest power Company in India, was setup in 1975 to accelerate power

    development in the country. It is among the worlds largest and most efficient power

    generation companies. In Forbes list of Worlds 2000 Largest Companies for the year

    2009, NTPC occupies 317th

    place.

    NTPC has installed capacity of 31,704 MW. It has 15 coal based power stations

    (24,825 MW), 7 gas based power stations (3,955 MW) and 5 power stations in Joint

    Ventures (2,864MW). The company has power generating facilities in all major regions

    of the country. It plans to be a 75,000 MW company by 2017.

    NTPC has gone beyond the thermal power generation. It has diversified into hydro

    power, coal mining, power equipment manufacturing, oil & gas exploration, power

    trading & distribution. NTPC is now in the entire power value chain and is poised to

    become an Integrated Power Major.

    NTPC's share on 31 Mar 2008 in the total installed capacity of the country was19.1% and it contributed 28.50% of the total power generation of the country during

    2007-08. NTPC has set new benchmarks for the power industry both in the area of power

    plant construction and operation.

    With its experience and expertise in the power sector, NTPC is extending

    consultancy services to various organizations in the power business. It provides

    consultancy in the area of power plant constructions and power generation to companies

    in India and abroad.

    Recognizing its excellent performance and vast potential, Government of the Indiahas identified NTPC as one of the jewels of Public Sector 'Navratnas'- a potential global

    giant. Inspired by its glorious past and vibrant present, NTPC is well on its way to realize

    its vision of being "A world class integrated power major, powering India's growth, with

    increasing global presence".

    THE TRAINING:

    I was given the opportunity to broaden my field of knowledge by having an exposure in

    such an industry. The industrial training commenced in 1 June, 2010 to 30 June, 2010. Iwas given the following machines to visit during my 4 weeks of training period:

    1. Gas Turbine

    2. Steam Turbine

    3. Combustion Chamber

    4. Cooling Tower

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    FLOW CHART OF NTPC KAWAS PLANT:

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    SALIENT FEATURES OF PROJECT01) Gas Turbine : 106 MW, 3 Stage Impulse Type

    02) GT Compressor : 17 Stages Axial Flow Compressor

    03) Combustion Chambers : Cannular type with 2 Igniters and

    14 Combustor baskets

    04) Air filter type and Particle Size : Self cleaning inlet air filter, for

    removing 5 micron particle size and

    above and Handling air flow 380

    kg/sec.

    05) Bypass Stack : Vertical circular 5.93 m. dia & 55 m.

    high

    06) Waste Heat Recovery Boiler : Double drum, non-firing, assisted

    (WHRB) Circulation Type heat recovery boiler

    07) WHRB Steam Parameters : Press Flow Temperature

    (Kg/cm) (Ton/hr) (Deg. C.)

    HP Steam 71.3 174 520LP Steam 7.1 40 192

    08) Steam Turbine : 116 MW, impulse, tandem

    Compound, Double exhaust, condensing

    type, with HP Turbine 13 stage horizontal

    single flow LP Turbine 5 stage horizontal

    double flow

    09) Condenser : Two Pass Surface Condenser, each

    Having 9200 no. Stainless Steel Tubes

    10) Generator rated output : 134 MVA for GT & 145 MVA for ST

    Rated Terminal voltage : 11.5 KV with Blushless Excitation

    Rated speed : 3000 RPM

    Type of cooling : Air-Cooled

    11) Black start facility : 2.5 MW Diesel Generator Set

    12) Cooling Tower type : Two Natural Draft Cooling Tower

    (One for each module)

    Cooling water (Design flow) : 24000 m/hr

    Range of cooling : 10 C

    Dimensions : 106.3 meters height & Base diameter of

    92 m.13) Cooling water pumps/ : 5 (one common standby)/11910 m/hr &

    Design parameters 22.4 MWC

    14) Pre-treatment Plant : 2 Clariflocculators each rated for

    1500 m/hr

    15) DM Water Plant : Two streams of 55 m/hr

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    COMBINED CYCLE POWER PLANT:Combine cycle power plant integrates two power conversion cycle-Brayton cycle (Gas turbine)

    and Rankine cycle (Steam turbine) with the principal objective of increasing overall plant

    efficiency.

    BRAYTON CYCLEGas turbine plants operate on this cycle in which air is compressed (process 1-2, in P-V diagram

    of figure-1B). This compressed air is heated in the combustor by burning fuel, where plant of

    compressed air is used for combustion (process 2-3) and the flue gases produced are allowed to

    expand in the turbine (process 3-4), which is coupled with the generator. In modern gas turbines

    the temp. of the exhaust gases is in the range of 500 C to 550 C.

    RANKINE CYCLE:The conversion of heat energy to mechanical energy with the aid of steam is based on

    this thermodynamic cycle. In its simplest form the cycle works as follows:

    The initial stage of working fluid is water (point 3 of figure 2), which at a certain

    temperature is pressurized by a pump (process 3-4) and fed to the boiler

    In the boiler the pressurized water is heated at constant pressure (process 4-5-6-1)

    Superheated steam (generated at point-1) is expanded in the turbine (process1-2), which

    is coupled with generator. Modern steam power plants have steam temperature in the

    range of 500C to 550 C at the inlet of the turbine.

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    COMBINING TWO CYCLES TO IMPROVE EFFICIENCYWe have seen in the above two cycles that exhaust is at temperature of 500-550 C and inRankine cycle heat is required to generate steam at the temperature of 500-550 C. Thereforegas turbine exhaust heat can be recovered using a waste heat recovery boiler to run a steam

    turbine on Rankine cycle.

    If efficiency of gas turbine cycle (when natural gas is used as fuel) is 31% and the efficiency of

    Rankine cycle is 35%, then over all efficiency comes to 49%. Conventional fossil fuel fired

    boiler of the steam power plant is replaced with a heat recovery steam generator (HRSG).Exhaust gas from the gas turbine is led to the HRSG where heat in exhaust gas is utilized to

    produce steam at desired parameters as required by the steam turbine.

    Evolution of gas turbines and combined cycle plants

    Early History

    Gas Turbines or Combustion turbines (an expression which has become popular in past

    few years) were first developed in the late 18th century. Patents for modern versions of

    combustion turbines were awarded in late nineteenth century to Franze Stolze and

    Charles Curtis, however all early versions of gas turbines were impractical because the

    power necessary to drive compressors outweighed the power generated by turbine. This

    is because of the fact that the turbine inlet temperature (TIT) required to deliver positive

    output and a certain minimum acceptable efficiency was above the allowable

    temperatures that could be faced by materials available in those days. For example in

    1904 two French engineers, Armengaud and Lemale built a unit, which did little more

    than turn itself over. The reasonmaximum temperature that could be used was about

    500 degree C and the compressor efficiency was abysmally low at 60 %.3.1.2Gas turbine performanceeffect of tit and compression ratio

    A Gas Turbine in its simplest form works on Joule Brayton Cycle, which consists of

    following:

    Compression (1-2): A rotating compressor acts as a fan to drive the working fluid into

    the heating system. The fluid is pressurized adiabatically, thus its temperature increases.

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    Compressors are of the dynamic type, in which each stage increases the fluid velocity,

    and then lets it diffuse to gain pressure.

    Combustion (2-3): The fluid is heated by internal combustion, in a continuous process-

    taking place at constant pressure. A steady supply of fuel mixes with air at high velocity

    from the compressor and burns as it flows through a flame zone. Combustion occurs in a

    very small volume, partly because it takes place at high pressure.

    Expansion (3-4): The working fluid at high pressure is then released to the turbine,

    which converts the fluid's energy into useful work as the temperature of the working fluid

    decreases. Part of this work is returned to the compressor. The remainder is used for the

    application intended: Generation of electricity, pumping, and turbojet propulsion.

    The use of a compressible gas such as air as working fluid permits the absorption and

    release of considerable amounts of energy. Such energy is basically the kinetic energy of

    its molecules, which is proportional to its temperature. Ideal gas turbine cycles are based

    on the Joule or Brayton cycles, i.e., compression and expansion at constant entropy, and

    heat addition and release at constant pressure.

    In an ideal cycle, efficiency varies with the temperature ratio of the working fluid in the

    compression process, which is related to its pressure ratio. The inlet temperature in the

    turbine section is generally limited by turbine technology, materials strength, corrosion

    and other considerations. The increment of temperature also depends on the initial

    Figure-1: Joule Brayton Cycle

    1

    23

    C

    T

    Fuel

    4Exhaust

    Figure 2: PV and TS Diagram of Joule BraytonCycle.

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    temperature of the working fluid. Some effects must be considered which diminish

    efficiency in real operating cycles, such as inefficiency in compression and expansion,

    loss of pressure during heat addition and rejection, variation of working fluid specific

    heat with temperature, incomplete combustion, etc.

    Gas Turbine Design Advancements:In gas turbine design the firing temperature, compression ratio, mass flow, and

    centrifugal stresses are the factors limiting both unit size and efficiency. For example,

    each 55C (100F) increase in firing temperature gives a 10 - 13 percent output increase

    and a 2 - 4 percent efficiency increase. The most critical areas in the gas turbine

    determining the engine efficiency and life are the hot gas path, i.e., the combustion

    chambers and the turbine first stage stationary nozzles and rotating buckets. The

    development process takes time, however, because each change of material

    may require years oflaboratory and field tests to ensure its suitability in terms of creepstrength, yield limit, fatigue strength, oxidation resistance, corrosion resistance, thermal

    cycling effects, etc.

    The above figure shows how overall (net) efficiency of simple and combined-cycle

    power plants has improved since 1950. The efficiency of simple cycle gas turbine plants

    has doubled, and with the advent of combined-cycle plants, efficiency has tripled in the

    past fifty years. Turbine nozzles and buckets are cast from nickel super alloys and arecoated under vacuum with special metals to resist the hot corrosion that occurs. The high

    temperatures encountered in the first stage of the turbine are of great importance,

    particularly if contaminants such as sodium, vanadium and potassium are present. Only a

    few parts per million of these contaminants can cause hot corrosion of uncoated

    components at the high firing temperature encountered. With proper coating of nozzles

    and buckets and treatment of fuels to minimize the contaminants, manufacturers claim

    the hot-gas-path components should last 30,000 to 40,000 hours of operation before

    Increase in Efficiency over the years.

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    replacement, particularly the hot-gas-path parts, that give rise to the relatively high

    maintenance cost for gas turbines (typical O&M annual costs 5 percent of the capital

    cost).

    GAS TURBINE PLANT:

    Introduction:

    The gas turbine is a common form of heat engine working with a series of processes

    consisting of compression of air taken from atmosphere, increase of working medium

    temperature by constant pressure ignition of fuel in combustion chamber, expansion of SI

    and IC engines in working medium and combustion, but it is like steam turbine in itsaspect of the steady flow of the working medium. It was in 1939, Brown Beaver

    developed the first industrial duty gas turbine. The out put being 4000 KW with open

    cycle efficiency of 18%. The development in the science of aerodynamics and metallurgy

    significantly contributed to increased compression and expansion efficiency in the recent

    years.

    At Kawas, the GE-Alsthom make Gas Turbine (Model 9E) has an operating

    efficiency of 31% and 49% in open cycle and combined cycle mode respectively when

    natural gas is used as fuel. Today gas turbine unit sizes with output above 250 MW at

    ISO conditions have been designed and developed. Thus the advances in metallurgical

    technology have brought with a good competitive edge over conventional steam cycle

    power plant.

    Kawas Gas Turbine Plant:The modern gas turbine plants are commonly available in package form with few

    functional sub assemblies.

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    The 9E model GEC-Alsthom package consists of

    Control compartment

    Accessory compartment

    Turbine compartment

    Inlet exhaust system

    Load package Generator excitation compartment

    CO2 fire protection unit

    Each station component is a factory assembled pretested assembly & is housed in all

    weather & acoustic proof enclosure. Advantages of gas turbine plant

    Some of the advantages are quite obvious, such as fast operation, minimum site investment.

    Low installation cost owing to standardization, factory assembly and test. This makes the

    installation of the station easy and keeps the cost per installed kilowatt low because the

    package power station is quickly ready to be put in operation.

    Site implementation includes one simple and robust structure to get unit alignment.

    Transport: Package concept makes easier shipping, handling, because of its robustness.

    Low standby cost: fast start up and shut down reduce conventional stand by cost.

    The power requirements to keep the plant in standby condition are significantly lower than

    those for other types of prime movers.

    Maximum application flexibility: The package plant may be operated either in parallel with

    existing plants or as a completely isolated station. These units have been used, widely for

    base, peaking and even emergency service. The station can be equipped with remote control

    for starting, synchronizing & loading.Control reliability: the microcomputer based control, with an integrated temperature system

    (ITS) provides accurate control, quick protection and complete sequential start up & shut

    down & operation. Maintenance Cost is comparatively low.

    GAS TURBINE EQUIPMENT DATA SUMMARYCOMPRESSOR SECTION

    Number of compressor stages Seventeen (17)

    Compressor type Axial flow, heavy duty

    Casing split Horizontal flange

    Inlet guide vanes Modulated

    TURBINE SECTION

    Number of turbine stages Three (3)

    Casing splits Horizontal

    Nozzles Fixed area

    COMBUSTION SECTION

    Type Fourteen (14) multiple combustors, reverse flow design

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    Fuel nozzles One (1) per combustion chamber i.e. (one for gas & one forliquid)

    Spark plugs Two-(2) electrode type, spring-injected self-retracting.

    Flame detectors Four (4),ultra-violet type

    BEARING ASSEMBLIES

    Quantity Three (3)

    Lubrication Pressure lubrication

    No.1 bearing assembly (Located in inletcasing assembly)

    Active and inactive thrust and journal, all contained in oneassembly

    Journal Elliptical

    Active thrust Tilting pad, self-equalizing

    Inactive thrust Tapered land

    No.2 bearing assembly (Located in the

    compressor discharge casing)

    Elliptical journal

    No.3 bearing assembly (Located in theexhaust frame)

    Journal, tilting pad

    STARTING SYSTEM

    Starting device Electrical starting motor 1 MW drive

    Torque converter Hydraulic with adjustor drive

    Fuel pump Accessory gear-driven, Continuous out put screw type pump

    Gas stop ratio & control valve Electro hydraulic servo-control

    LUBRICATION SYSTEM

    Lubricant Petroleum base

    MOT capacity- 3,300 gallons (aprox.) i.e.12,540 litres (aprox.)

    Main tube pump Shaft driven.

    Emergency lube pump D.C. motor driven vertical submerged, centrifugal type

    (88QE)

    Auxiliary lube pump A.C. motor driven, vertical submerged, centrifugal (88QA)

    Heat exchanger (s)Type Oil heat to fresh water

    Quantity Two in parallel

    Filter (s)

    Type Full flow with transfer valve

    Quantity Two (Duplex)

    Cartridge type Five-micron filtration pleated paper.

    HYDRAULIC SUPPLY SYSTEM

    Main hydraulic supply pump Accessory gear-driven, variable positive displacement, axial

    piston

    Auxiliary hydraulic supply pump Driven by electric motor (88HQ), with accumulators- 2 nos.

    COOLING WATER SYSTEM

    Pumps Two water pumps located on lube oil tank inside theaccessory compartment.

    Water cooling modules 15 nos. fans and finned tube radiators

    CONTROL SYSTEM

    SPEEDTRONIC MARK IV control system

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    Gas Fuel SystemThe gas fuel system is designed to deliver gas fuel to the turbine combustion chamber at the

    proper pressure and flow rates to meet all of the starting, acceleration and loading requirements of gasturbine operation. A schematic diagram of the gas fuel system is given in figure. The major components

    of a gas fuel system are the gas stop/ratio and gas control valves located on the accessory base.Associated with the two gas valves are the necessary inlet piping strainer, fuel vent valve, control servovalves, pressure gauges and the distribution piping to the 14 combustion fuel nozzles. The fuel gas stop

    ratio valve and the gas control valve, two independent valves, are located inside the gas fuel panel, of

    the accessory base. The gas fuel flows through the gas stoop ratio valve and then into the gas controlvalve on its way to the gas manifold and individual combustion chambers. The position of each valve is

    servo controlled by electrical signals from the gas turbine SPEEDTRONIC control system. Both the gas

    stop ratio valve and gas control valve are actuated by single acting, hydraulic cylinders

    The following major components comprise the gas fuel system:

    Strainer

    Fuel gas supply pressure alarm switch

    Gas stop ratio valve VSR

    Gas control valve VGC

    Stop ratio LVDTS 96GC-1, 2

    Stop ratio valve-control servo valve 90SR

    Gas control valve- control servo valve 65 GC

    Gas fuel dump valves VH5 and VH12

    Gas fuel vent solenoid valve 20 VG-1 and 2

    Pressure gauges

    Lines to the 14 combustion chambers

    Liquid Fuel System:The liquid fuel system pumps and distributes fuel as supplied from the off base forwarding

    system, to the fourteen fuel nozzles of the combustion system. The fuel system filters the fuel and device

    the fuel flow in to 14 equal parts for distribution to the combustion chamber at the required pressure andflow rates. Controlling the position of the fuel pump bypass valve VC3 regulates the amount of fuel

    input to the turbine combustion system by varying the amount of bypassed fuel. The fuel system shownin the schematic diagram is comprised of the following major components plus several other control

    devices, switches and gauge.

    Temporary fuel oil strainer SFI

    Fuel oil stop valve VSI. Liquid fuel pumps PFI.

    Fuel pump discharge relief valve VR-4

    Fuel bypass valve VC-3

    High-pressure fuel strainer Fuel line check valve

    Fuel nozzle assemblies

    False start drain valve VA17-1 andVA17-2 (in bottom of combustion wrapper and exhaust frame)Control device also associated with the fuel system include the liquid fuel pressure switches 63 FL-2,

    Servo valve 65 FP that controls the fuel bypass valve, fuel clutch solenoid 20 CF, and permissive limit

    switches 33 FL-1 an2 and trip relay valve VH4 in the fuel oil stop trip control circuit.

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    Atomizing Air SystemAtomizing air system provides sufficient pressure in the air atomizing chamber of the fuel nozzle

    body to maintain the ratio of atomizing air pressure to compressor discharge pressure at approximately

    1.2 or greater over the full operating range of the turbine. Since the output of the main atomizing air

    compressor, driven by the accessory gear, is low at turbine firing speed, during starting, atomizing aircompressor provides a similar pressure ratio during the firing and warm up period of the starting cycle

    and during a portion of the accelerating cycle. Continuous blow down to atmosphere is also provided toclear the main gas turbine compressor of accumulated dirt. Major system components include: the mainatomizing air compressor, starting air compressor, atomizing air heat exchanger and an air filter.

    WASTE HEAT RECOVERY BOILER: (WHRB)The exhaust hot gases of the GT come to the Waste Heat Recovery Boiler (WHRB) if we do not

    bypass them through bypass stack.

    The WHRB produces superheated steam at Low & High pressures. The steam generator

    comprises of an economizer, an evaporator with drum and a super heater section for both LP & HPsystems. Boiler used here in KGPP is waste heat recovery type which is generally denoted WHRB.

    Waste heat recovery boiler general details:

    The WHRB includes the following:

    1. Water heater2. L.P economizer3. H.P economizer4. L.P evaporator5. H.P evaporator6. L.P super heater7. Two H.P super heater8. L.P & H.P drum

    9. L.P & H.P circulating pumps10.Diverter damper11.Weather protection damper12.Bypass stack13.Chimney

    Make : COCKERILL mechanical industries

    Qty. installed : 4

    Type : dual drum, assisted circulation, vertical

    Unfired, dual pressure boilerTotal heating surface : H.P=655504sq.m

    L.P=19938sq.m

    Final temp of steam : H.P=520deg.C

    L.P=109deg.COverall length : 15440mm

    Design press : H.P=83bar

    L.P=7.6bar

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    STEAM TURBINE:Rankine Cycle :

    Process 1-2 : Water from the condenser at low pressure is pumped into the boiler at highpressure.this process is reversible adiabatic.

    Process 2-3: Water is converted into the steam at constant pressure by addition of heat inthe boiler.

    Process 3-4 : Reversible adiabatic expansion of the steam in the steam turbine.

    Process 4-1 : Constant pressure heat rejection in the condenser to convert condensate intowater.

    The steam leaving the boiler may be dry and saturated, wet or superheated. The

    corresponding T-S

    Diagram are 1-2-3-4-1; 1-2-3-4-1; 1-2-3-4-1.

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    Steam TurbineST operates at 3000 rpm. The steam is provided to ST through the two WHRBS

    which are mounted at the exhaust of both the GT of each module. The single casing machine

    is equipped with two admissions to take HP & LP steam from HP & LP drums. The axial

    exhaust of ST is directly connected to the horizontally arranged 2 pass surface condenser.

    Steam Bypass System

    To increase operation and start-up flexibility of the plant, a steam bypass system is

    integrated, which automatically goes into operation, if any of the following operation cases

    occur:

    a. ST start-up or shutdown,

    b. Turbine trip

    The steam bypass system is designed to handle the whole steam production at full

    pressure under all ambient conditions. It consists of an isolating and a steam pressure

    reducing valves with integrated water injection and the associated measurement, control

    and protective devices. Injection water for desuperheating of the steam is taken from the

    main condensate line.

    Cooling Water System

    A natural draught wet cooling tower system transposes the waste heat of the water steam

    cycle to the atmosphere. Two 100% main cooling water pumps supply the cold water from the

    cold-water basin to the main condensers and the intercoolers of the CCW system. The condenser

    tubes in clean conditions.

    Losses in the system are made up by clarified raw water. The cooling water quality is

    controlled by the cooling water sampling water sampling and dosing station, where chemicals

    can be dosed.

    Closed Cooling Water System

    A separate closed cooling water system for each unit ensures the cooling of the lube

    oil system, the HP feed water pumps, the LP boiler preheated circulating pumps, the generator

    air coolers, the sampling system, etc.

    The heat is dissipated to the main cooling water system via 100% capacity water-to-

    water heat exchanger.

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    Losses in the system are made up by DM water from the DM water system. To achieve

    a defined quality of the water, and inhibitor dosing station is connected to CCW system.

    COOLING TOWER:

    Cooling Towers have one function:

    Remove heat from the water discharged from the condenser so that the water

    can be discharged to the river or re circulated and reused.

    Some power plants, usually located on lakes or rivers, use cooling towers as a method of

    cooling the circulating water (the third non-radioactive cycle) that has been heated in the

    condenser. During colder months and fish non-spawning periods, the discharge from the

    condenser may be directed to the river. Recirculation of the water back to the inlet to the

    condenser occurs during certain fish sensitive times of the year (e.g. spring, summer, and fall)so that only a limited amount of water from the plant condenser may be discharged to the

    lake or river. It is important to note that the heat transferred in a condenser may heat the

    circulating water as much as 40 degrees Fahrenheit (F). In some cases, power plants may

    have restrictions that prevent discharging water to the river at more than 90 degrees F. In

    other cases, they may have limits of no more than 5 degrees F difference between intake and

    discharge (averaged over a 24 hour period). When Cooling Towers are used, plant efficiency

    usually drops. One reason is that the Cooling Tower pumps (and fans, if used) consume a lot

    of power.

    Major Components

    Cooling Tower (Supply) Basin

    Water is supplied from the discharge of the Circulating Water System to a Distribution Basin,

    from which the Cooling Tower Pumps take suction.

    Cooling Tower Pumps

    These large pumps supply water at over 100,000 gallons per minute to one or more Cooling

    Towers. Each pump is usually over 15 feet deep. The motor assembly may be 8 to 10 feet

    high. The total electrical demand of all the Cooling Tower pumps may be as much as 5% of

    the electrical output of the station.

    Cooling Towers

    There are 2 types of towers - mechanical draft and natural draft

    Natural Draft Cooling Tower

    The green flow paths show how the warm water leaves the plant proper, is pumped to the

    natural draft cooling tower and is distributed. The cooled water, including makeup from the

    lake to account for evaporation losses to the atmosphere, is returned to the condenser.

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    PLANT AT A GLANCE:

    GAS TURBINE DESIGN EFFICIENCY

    Heat Rate

    (Kcal/Kwh)

    Efficiency (%)

    Open Cycle

    Gas 2695 31.8

    Liquid fuel 2730 31.4Combined Cycle

    Gas 1741 49.23

    Liquid fuel 1776 48.26

    CONCLUSION

    After analyzing the NTPC 656.2 MW combined cycle power plant, we can describe that this

    power plant is very efficient one as compare to other power plant is very efficient. One as

    compare to other power plants in its series. Also we would like to add up that it is very

    compact in size, less pollute in nature, easily controlled and decent power plant that we had

    ever seen