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Showing posts from May, 2020

CIRCULATING WATER SYSTEM

CIRCULATING WATER SYSTEM ·       The circulating water system supply cold water to the condenser. ·       The cold water absorbs the latent heat of condensation from exhaust steam in the form of sensible heat . ·       Steam exhaust from low pressure steam turbine condenses in a condenser & condensed water reused in the cycle again. ·       In a surface condenser, the steam flows over a tube bundle & condensed and cooling water flowing inside the tubes. ·       Heat is transferred from steam to water with the help of tubes. Tubes are works as a barrier between cooling water and stem to be condensed. ·       Further the temperature of cooling water increases and become warm. ·       It is a continuous process in which heat is continues removed from the condenser. ·       This warm water reject their heat to the atmosphere through cooling towers or spray ponds or warm water dumped in to the natural water reservoir ·       In all thermal power plants surface co

Feed water system

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In a boiler feed water system following sub systems are involved. FST Booster pump Boiler feed pump  Drive of boiler feed pump (motor or turbine) High pressure feed water heater Feed regulating station / feed control station Economiser Feed Storage Tank      Water is pumped from feed storage tank to the boiler or boiler drum with the help of boiler feed pump. there are two or three boiler feed pumps are installed in a single unit. this is a high pressure pump. the discharge pressure of this pump is greater than that the boiler drum pressure due to which water in flow in to the boiler drum.      Boiler feed pump is a special type of pump. this is a multistage pump. generally a multistage pump is called as a turbine type pump.     FST(Feed Storage Tank) is a part of Deaerator which reserve store the treated condensate water. fst may be an integral part of deaerator or it may be installed bellow the deaerator tank. The FST is installed at a specific height to provide the NPSH to the boile

Why Hydrogen Cooling

Why Hydrogen Cooling  Lowest density gas yields lowest drag Highest heat conductivity of any gas Controlled atmosphere to maintain Clean & Dry Inexpensive  Easy to detect  Excellent electrical properties Easy to manage – not readily miscible with CO2 purge gas Flammable Hydrogen Flammability Range Hydrogen has a wide flammability range generally 4% to 75% hydrogen in air is hydrogen flammability range.  So 4% is lower flammability range & 75% is upper flammability range. If hydrogen in air is bellow 4% then no chance of flame & if hydrogen percentage is above 75% then no chance flammable.then always in generator maintain hydrogen purity as higher as possible.above upper flammability level no chance of ignition if system is leak proof. Generator is always under pressure (higher than atmosphere). Generally in generator  casing hydrogen purity is maintain above 96%. H 2  is lightest  gas  with   0.09 gm/litre while air is 1.3  i.e. 14.4 times. The

Generator Cooling System

Generator Cooling System Air cooled generator In generator large amount of heat is generated and is not possible to dissipate this heat from natural system. So forced air cooling system is adopted. In this air is forced into the generator due to which large amount of heat is removed. Air is forced circulated inside generator. This air is pick up the heat from conductors of the generators and further air is cooled in a heat exchanger in which cooling water is flowing. In generator small ducts are provided in which air is flowing. The heat dissipation with air cooling system is limited. It is used in small size generator. This system is some limitations like it is not possible to used in a large size of generator. The air should be clean and free from dust & moisture (So instrument air is supplied through a line). There is an optimum rating of the generator beyond which air cooling system is not economical because of air have a limit of heat for heat transfer.

LABYRINTH SEAL

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Its name from fact from its construction. Labyrinth seals consist of series of thin strips fixed to the casing or other stationary member and arranged so as to maintain the smallest possible clearance with the shaft. The labyrinth seals have small restrictions that increase the velocity of leaking fluid only to have it dissipated in the pockets, thereby throttling the fluid.  The tips of the strips are extremely thin so that if rubbing occurs the tip gets worn away without damaging the shaft.  These labyrinth seals do not prevent complete leakage of fluid. These are effective in only reducing leakage. In it steam in leaking must follow a winding path and change i ts direction many times. It is constructed from thin strip at the outer circumference of shaft of turbine at both end. It is installed at the inner circumferential surface of casing at both end. There are several types of Labyrinth packing is subjected to a throttling action.  This action produced a reduction in

CONDENSATE EXTRACTION PUMP

CONDENSATE EXTRACTION PUMP SYSTEM DESCRIPTION Condensate from condenser hot-well is pumped through LP heaters up to deaerator by Condensate Extraction Pumps (3 nos. CEP).  In full load operation two pumps will be in operation and one in standby condition. CEP is of vertical sleeve type multi stage pump.  So it is called as turbine type pump. Each pump is directly driven through an electric motor and is delivering to condensate water. All the CEP are connected to a common header through a non-return valve and motorized discharge valve. From that discharge header condensate passes through Gland Steam Condenser (GSC) and through a Deaerator control station. By modulating this valve Deaerator level is maintained according to the set point given. A recirculation valve is provided before Deaerator level control valve to maintain a minimum condensate flow through the pump & GSC. The main condensate is passed through Condensate Polishing Unit, GSC, LP heater-1, LP hea

Auxiliary Steam common Header Charging

Auxiliary Steam common Header Charging SYSTEM DESCRIPTION : Aux steam system includes four  ways of steam source:  Start-up boiler or aux boiler,(If it is available in plant ) Low-temperature reheated steam supply  Main steam steam supply line Near by unit common header In normal, each unit aux steam is supplied by CRH steam. There is interconnection between aux steam headers of all units and also connected to start-up aux boiler.  Parameters of aux steam are: Aux steam pressure normal range: 8-12 kg/cm2 Aux steam normal temperature: 300-350 deg C. Initial conditions Aux boiler is running hot boxed-up condition station APRDS Pre Checks & Charging Procedure: Ensure that Auxiliary Boiler is ready for Aux Steam header charging from aux. boiler. Generally temperature maintain before charging from  aux boiler between range is 180 to 300 deg C and pressure is 4 to 5 Kg/cm2 All the way from Auxiliary boiler MS stop valve to Start up steam

Drum Level Control in Larger Capacity Boiler

Drum Level Control in Larger Capacity Boiler In a large capacity boilers feed pump motor is not directly connected to the boiler feed pump. Between motor and feed pump a hydraulic coupling is used in which an arrangement is given for speed increasing and then regulating through the scoop tube. This provide a variable speed operation while motor is running at constant speed. With the help of scoop tube motor is started with no load and pump is running with it on a re-circulation mode. No direct mechanical connection is there between the motor and the pump shafts.  The coupling consists of a radial pump impeller mounted on the motor shaft and a radial flow reaction turbine runner mounted on the pump  shaft. Both the impeller and runner are identical in shape and they together form a casing which  is completely enclosed and filled with oil. When motor shaft is rotated, the oil starts moving from the inner radius to the outer radius of the pump impeller. This oil enters

ECONOMIZER

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ECONOMIZER Economiser is a pressurized back end equipment because of it is installed at the end of boiler. Where after no heat is added to the water or steam. Heat transfer surface used to increase the temperature of the feed water before it enters to the boiler drum. When flue gases travel across water-walls then latent heat is absorb & super heaters absorb sensible heat from flue gases. The economizer is composed of low-temperature convection pass surface. Economizer is placed in series with the feed water heaters of the regenerative system. The function of the economizer is, to raise the temperature of feed water downstream of the highest pressure feed water heater to the saturation temperature corresponding to the boiler pressure. After absorbing the heat from flue gases to the super heater and reheater by steam some heat is present in flue gas this heat is absorbed by sub cooled feed water which is flow in side economizer before entry of boiler drum. With this typ

GOVERNING OF STEAM TURBINES

GOVERNING OF STEAM TURBINES Requirement of governing system:- Controlling and regulating of a turbine according to variable demand. The regulation of turbine is done by maintaining control of speed, pressure and flow by the help of governors. Governing of turbine maintains the speed of turbine at constant level irrespective of load. Governing of steam turbine is classified according to the mechanism  (i) Throttle governing (ii) Nozzle control governing (iii) By-pass governing (iv) Combined governing (i.e., Combination of above as throttle and nozzle control governing or ‘throttle and by-pass governing). (i) Throttle Governing:   Throttle governing of steam turbine bases upon the throttling of steam up  to suitable pressure and regulate the mass flow of steam through the turbine so as to control the output  of turbine.  Here in throttle governing, aim is to alter the mass flow rate as for example by reducing it, the  available energy gets reduced and hence l

BOILER DRAUGHT

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BOILER DRAUGHT Draught refers to the pressure difference created for the flow of gases inside the boiler. Boiler unit has a requirement of the expulsion of combustion products and supply of fresh air inside furnace for continuous combustion. The flues gases or combustion products formed during combustion should be discharged at such a height. A chimney or stack is generally used for carrying these combustion products from inside of boiler to outside , i.e. draught is created by use of chimney. Draught may be c reated naturally or artificially by using some external device.  Draught can be classified as below: In natural draught the pressure difference is created naturally without using any positive displacement device. Artificial draught is created using some external assistance causing forced displacement of gases . It can be created either by using mechanical devices or steam. Artificial draught can be of induced type, forced type or combination of