Friday, April 6, 2012

The gas turbine | combined-cycle | plants


The combined-cycle power station uses gas turbines to increase the efficiency
of the power-generation process. Like many other machines that we
assume to be products of the twentieth century, the gas turbine isn't that
new. In fact, Leonardo da Vinci (1452-1519) sketched a machine for
extracting mechanical energy from a gas stream. However, no practical
implementation of such a machine was considered until the nineteenth
century, when George Brayton proposed a cycle that used a combustion
chamber exhausting to the atmosphere. In 1872 Germany's F. Stolze
patented a machine that anticipated many features of a modern gasturbine
engine, although its performance was limited by the constraints of
the materials available at the time.



Many other developments across Europe culminated in the development
of an efficient gas turbine by Frank Whittle at the British Royal
Aircraft Establishment (RAE) in the early 1930s. Subsequent developments
at RAE led to viable axial-flow compressors, which could attain
higher efficiencies than the centrifugal counterpart developed by Whittle.
All these gas turbines employed the Brayton cycle, whose pressure/
volume characteristic is shown in Figure 1.5. Starting at point A in this
cycle air is compressed isentropically (A-B) before being fed into a combustion
chamber, where fuel is added and burned (B-C). The energy of the
expanding air is then converted to mechanical work in a turbine (C-D).
From C to D heat is rejected, and in a simple gas-turbine cycle this heat is
lost to the atmosphere.
The rotation of the gas turbine can be used to drive a generator (via
suitable reduction gearing) but, when used in a simple cycle with no heat
recovery, the thermal efficiency of the gas turbine is poor, because of the
heat lost to the atmosphere. The gases exhausted from the turbine are not
only plentiful and hot (400-550°C), but they also contain substantial
amounts of oxygen (in combustion terms, the excess air level for the gas
turbine is 200-300%). These factors point to the possibility of using the
hot, oxygen-rich air in a steam-generating plant, whose steam output
drives a turbine.

The use of such otherwise wasted heat in a heat-recovery steam
generator (HRSG) is the basis of the 'combined-cycle gas-turbine'
(CCGT) plant which has been a major development of the past few
decades. With the heat used to generate steam in this way, the whole plant
becomes a binary unit employing the features of both the Rankine and the
Brayton cycles to achieve efficiencies that are simply not possible with
either cycle on its own. In fact, the addition of the HRSG yields a thermal
efficiency that may be 50% higher than that of the gas turbine operating
in simple-cycle mode.
Once again, there is nothing really new about this concept• From the
moment when the gas turbine became a practical reality it was very
obvious that the hot compressed air it exhausted contained huge amounts
of heat. Therefore, the combined cycle was considered in some depth
almost as soon as the gas turbine was released from the constraints of
military applications. However, because of their use of gases at extremely
high temperatures, early machines suffered from limited blade life and
they were therefore used only in applications where no other source of
power was readily available. With improvements in materials technology
this difficulty has been overcome and, nowadays, combined-cycle plants employing gas turbines form the mainstream of modern power-station development.
But whether it is in a combined-cycle plant or a simple-cycle power
station, our interest in this chapter is in steam and its use, and this vapour
will now be examined in more detail. We shall see that what seems a fairly
simple and commonplace thing is, in fact, quite complex.
In spite of its complexities it is important to tackle this subject in some
depth, because the power-plant control and instrumentation engineer will
need to deal with the physical parameters of steam through the various
stages of designing or using a practical system.


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Thursday, March 22, 2012

Model 9224 | coal Feeder | CONSTRUCTION



The feeder is comprised of feeder frame, feeder belt assembly, cleanout conveyor, weighing system, coal
plug-gage and coal void signaling devices. lubrication piping and electric wiring, microprocessor control cabinet.
• The feeder frame is comprised of casing, inlet and discharge end doors, side doors and internal feeder light. The casing is an enclosed weldment that can resist explosive pressure up to 0.34 MPa to meet requirements specified in NFPA Code 85F by National Fire Protection Association of the U.S.A. Guide plate and skirt are provided in the inlet to form fixed section of coal flow on the belt after coal is dropped into the feeder. All parts contacting coal are made of OCr18Ni9Ti stainless steel. Inlet and discharge end doors are firmly bolted to the casing to ensure perfect seal. All doors are optional to open leftward or rightward. sight glasses are provided on all doors and nozzles are equipped interior of sight glasses to clear off accumulated coal dust by pressurized air or water. Internal feeder light of sealed construction enables observation of internal feeder operation.


• The feeder belt assembly is comprised of motor, reducer, drive pulley, take-up pulley, tension roll, belt supporting plate and the belt. The belt is rimmed and provided with a v-guide at the inner belt center to engage with grooves on rollers to keep good belt tracking. At the end of drive pulley scraper is equipped to clear off coal adhered on the outer surface of belt. The tension roll is located at the midpoint of bell travel, it keeps the belt under a fixed tension to obtain optimum weighing effect. The belt tension varies with different temperature and with temperature variation. Intensive observations should be frequently done and make tension adjustment by means of the take-up screws. Scaled indicator is equipped interior of side door to the feeder, the tension roll should be regulated to locate its center at the midpoint of the indicator. Totally enclosed, variable frequency motor is used to drive the belt. Which is comprised of a 3-phase ac motor, a tacho-generator. A variable frequency driver and variable frequency motor provide an ac stepless speed regulation .It can provide a smooth and stepless speed regulation within a rather broad range. The feeder belt reducer is a two-stage reducer, comprised of cylindrical gears and worm wheel. The worm wheel is oil bath lubricated while a cycloidal pump in the reducer pumps oil via a hole in the worm shaft to 3 lubricate the gears. The drive pulley is driven through a pin type coupling which is mounted on the worm wheel shaft.
• The coal void signaling device is located above the belt. When there is no coal on the belt, the paddle of signaling device deflects and causes cam on the axle of device to turn and actuate the limit switch, either to control the belt drive motor, or to initiate the coal bunker vibrator, or to output a signal back to control room to signify no coal on the belt. The customer may determine, according to operating system requirements, which of these functions shall be performed. The coal void signal can also deactivate integrated weight and can prevent feeder calibration with coal on the belt. The coal plug-gage signaling device locates at the feeder discharge and is of identical construction to the coal void signaling device. The limit switch outputs signal signifying coal flow plug-gage at discharge and stops the feeder operation.
• The weighing system is located between feeder inlet and drive pulley. All of the three roller surfaces are finely finished, of which two rollers are fixed on the feeder casing to form a weigh span and the third roller hangs on a pair of load cells. Coal weight on the belt acts on load cells to output a signal. Output signal from the calibrated load cells signifies unit length coal weight and frequency signal from the tacho-generator signifies belt speed. The microprocessor controls integrates both signals to obtain the feedrate. Test weights are located below the load cells and the weigh roller. During feeder operation, test weights are supported by the weigh arm and the eccentric disc to part from the weigh roller. On calibration, turn the ratchet handle so that the eccentric disc is turned to make test weights hang on the load cells to check if the weight signal is correct.
• Cleanout conveyor is used to clean off coal accumulated on inner floor of the feeder. During feeder operation, coal adhered on the belt is cleaned off by a scraper and dirt accumulated on inner belt is dropped off from both ends of the self-cleansing type tension roll. As seat air also generates dirt, dirt will deposit on the inner floor to cause self-ignition if it is not timely cleaned off. Cleanout chain is driven by a motor via a reducer, wing type chain scrapes off the dirt to the feeder discharge. It is recommended that the cleanout conveyor is synchronously operated with the feed bell operation so that coal accumulation interior of the feeder is minimized. Furthermore, continue clean off is also of advantage both to reduce feedrate error and to prevent chain pin from adhesion and rustiness. The cleanout conveyor reducer is comprised of cylindrical gears and worm wheel. Electric overload protection is provided for the cleanout conveyor drive motor, when overload the cleanout conveyor motor’s power is automatically turn off by electronic overload relay to stop reducer.
Seal air inlet is located below the feeder inlet with a flange-type connection for the customer to supply seal air into the feeder. Under pressure operation status, the feeder needs sear air to prevent pulverizer heat air from reversing into the feeder through the inlet. The seal air pressure is 60~245 Pa higher than the pulverizer inlet pressure. The required seal air delivery is the sum of air leakage from hopper of downspout and the amount required to form a pressure difference between inlets of the feeder and of the pulverizer. The feeder itself is construed as of reliable sealed with no leak. A threaded hole is provided near the feeder inlet for adapting a pressure gauge to test the feeder internal pressure. The hole must be plugged if a pressure gauge is not equipped. If the seal air pressure is too low, it will cause the pulverizer heat air reverse back to the feeder so that coal dusts will stagnate at the door frames and at protrusion parts to induce self-ignition. If either the seal air pressure or its flow rate is too high, it will blow coal particles off the belt to degrade weighing accuracy and to increase the load on clean out scrapers. 4 Furthermore, if the seal air flow rate is too large, dustiness is prone to be formed interior of the sight glass to hamper observation. Therefore, suitable seal air pressure has to be adjusted.
• Except that the reducer is oil bath lubricated, grease lubrication is used for all other parts. All lubricating points within the feeder are connected with hoses that extend outside the feeder so that, lubrication can be performed without opening doors to the feeder. Flexible tubes are used for electric wiring, cables are led into the feeder through the tubes so that casing seal is kept.
• Control cabinet is installed on the body of the feeder. Power supply switch is located in cabinet. It can turn on or turn off the power.
• Microprocessor control board, power supply board signal converting board, variable frequency driver disconnect switch, transformers, fuses and relays are installed within the microprocessor control cabinet which is mounted on the feeder casing. On the panel of cabinet microprocessor display keyboard and switches SSC and FLS are equipped. For their functions.





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Friday, March 16, 2012

Displacement | Gear | Pumps | Series D/H/HD



Performance Data
Series D Fixed Displacement, Pressure-Loaded Gear Pump
Features
• Pressure-loaded design
• Efficient, simple design - few moving parts
• Exceptionally compact and lightweight for
their capacity
• Efficient at high pressure operation
• Resistant to cavitation effects
• High tolerance to system contamination
• Reliable under cold weather operation
• Sleeve-bearing construction
• Multi-fluid compatibility
Controls
• Optional built-in relief valve
• Consult factory for special controls
Specifications
Flow Ratings:
.5 GPM (1.9 LPM) to 2.7 GPM (10.2 LPM)
(At 1000 RPM) See next page for additional
flow data.
Pressure Ratings:
D05 thru D22 - 2500 PSI (172 Bar) continuous
D27 - 2000 PSI (138 Bar) continuous
Speed Ratings:
D05 thru D22 - 500 to 4000 RPM
D27 - 3000 RPM
Mounting:
SAE-AA - 2-Bolt Flange
4-Bolt Flange
Housing Material:
Die-Cast Aluminum

Installation Data
Inlet Conditions:
10 in. hg. max. vacuum condition
(At 1800 RPM)
5 in. hg. max. vacuum condition
(At max. RPM)
20 PSI (1.4 Bar) max. positive pressure
Operating Temperature Range:
-40°F to 185°F
(-40°C to 85°C)
Filtration:
Maintain SAE Class 4



A Parker pressure-loaded gear pump consists of two, intermeshing, hardened-steel, precision-ground gear assemblies. These precision gears are enclosed by a high-strength, die-cast aluminum front cover, back cover and a high-yield, strength-extruded aluminum
center section.

Gear assemblies consist of one drive gear, shrinkfitted on a precision-ground and polished drive
shaft. This shaft extends outside the pump to permit coupling to an external prime mover. The second
gear, being the driven gear, is also shrink-fitted on a precision-ground and polished driven shaft. Retaining rings, which are installed in grooves provided on the shaft, ensure that the gears will not move axially, and a key keeps the drive gear from moving radially. A lip-type, shaft seal is provided at the drive shaft to prevent external leakage of pump fluid. The sealing lip in contact with the fluid is spring-loaded. Vent passages within the housings and driven shaft communicate pump inlet pressure to the rotary seal area, thus imposing the lowest possible pressure at the rotary seal for extended seal life.

The phenolic heat shield, backup gasket, and molded rubber seal form chambers behind the steel-backed bronze wearplate. These chambers are connected either to inlet or discharge pressure. Discharge pressure, acting within the chambers, axially loads and deflects the wear plate toward the gear faces to take up gear side clearances. This pressure-loading on the wear plate increases pump efficiency by reducing internal leakage to a minimum, providing longer pump life. Pump rotation is dependent upon the proper orientation of the heat shield, backup gasket, and rubber seal in the front cover housing, the center section and rear cover, respectively. Pumping action is achieved by connecting the pump drive shaft to a prime mover, and rotating the gears away from the inlet port. Rotation causes the gear mesh to increase on the inlet side and decrease on the outlet (pressure) side.



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Wednesday, March 14, 2012

Steam | Turbine | Of Plants



Type Steam Turbine
- Based on the energy transformation process:
- Turbine impulse
- Turbine reaction
- Under pressure steam turbine
- Back pressure
- Condensing.
- Under the pressure of steam into the turbine
- Super critical pressure (225 bar)
- Very high pressure (170 bar and above)
- High pressure (above 40 bar).
- Pressure medium (s / d 40 bar).
- Low pressure (1.2 - 2bar abs)
- Based on the steam setting in.
- Constant pressure with throttle control.
- Constant pressure with Nozzle control.
- Sliding pressure

a) The speed of the steam out nozzle Ct = 192.6 m / s, then the magnitude of thrust force P1 = m (C1t-C2) = 1/9, 81 (196.2-0) = 20kg.
b) P2 = 1/9, 81 (196.2 +196.2) = 40kg
c) P3 = 1/9, 81 (196.2 + cos300
196.2 cos300) = 34.7 kg.
Relative velocity steam strikes the blade because the blade moves C1t w1 =-U, and if U = 98.1 m / s the thrust
a) P1 '= 1/9, 81 (196.2 to 98.1) = 10kg
b) P2 '= 2/9, 81 (196.2 to 98.1) = 20kg
c) P3 '= 2/9, 81 (196.2 cos300 -
98.1 cos300) = 34.7 kg.
Start-up turbine is divided into 3 types:
Cold start-bin that is if the tour has stopped more than 120 hours. To start this kind requires the longest time: 360 minutes
Warm start when the turbine stopped between 24 -72 hours. Start-up time full load: 160 minutes
Start the heat if turbine stopped less than 6 hours. Start time to 30 minutes at full load
Make sure that the temperature and vapor pressure are in accordance with the type of start before the steam is inserted into the turbine.
Slowly open the throttle valve slowly and manually note langkah2 accretion rate and rotation relative to the current state adjusted in accordance with the user expansionnya
Rapidly through the critical rotation.
Do a test protective device when rotation reaches sinkroon round.
Do a test overspeed if the unit runs out overhaul
Immediately add the flow of steam after sinkroon.
Do a manual trip if the unit runs out overhaul.
Loading the next match with the user.

 internal losses are losses associated with making the steam in the turbine.
• Losses in the valve pe-
ngatur steam turbine entry ΔH
• Losses in the nozzle or
fixed blade hn
• Losses didlm blade path hb
• Losses due to increased steam
hl blade left behind
• Losses due to friction steam
with disc blade holder
• Losses in sealing an-
tar levels of blade (labirint).
• Losses caused by wet steam

 external losses are losses that are not related to the course of the steam in the turbine as mechanical losses and losses in the steam turbine shaft sealing.
Lubrication of turbine generator system it functions:
 Establish intermediate layer (with a certain thickness) so that no direct contact between the shaft and bearings, and dirt do not hurt the oil carried by the bearing surface.
 Throw away the heat arising from friction in the bearings or the other.
Condition so that the lubricant must be guaranteed not to damage the parts in its path, because it is equipped with a turbine lubrication system cleaning system known as the "oil condtioner"
Wet steam or vapor containing water will cause erosion on turbine blades, because the grain must be removed from the grains of water vapor passes through the extraction channel and especially in the last fixed blades pengkap given channel and waster water.



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Lubrication | for Industrial | Plants

Making Lubricants
Lubricating oil used in generating engines lubricant is mineral oil. Manufacture of mineral lubricating oils made ​​in oil mills by the fractionation of raw material (crude oil). Lubricating oil can also be made from a variety of basic materials such as:
- Lubricating oils made ​​from plants and from animals
such as castor oil (Castrol Oil), use as seed
the base material. Vaseline, using animal fat as an ingredient
basically.
- Synthetic lubricating oils. Derived from synthetic materials (eg Polyqlycols,
basic zdi Acid esters, Fluoroesters, Polyphenil esters, a Novel Synthetic, Lubricants, etc.)


Capabilities and advantages of this mineral include:
- Temperature operating range is quite large
- Easily mixed with chemicals to increase
- Ability to work
- Nature of Physical and Chemical Properties easily controlled
Material wear can be reduced by reducing the magnitude of the force due to friction is by avoiding the direct contact between two surfaces rub against each other. One way to avoid direct contact between two objects rub against each other is to "insert" the lubricating oil between the two objects. This method is called "lubricate" or provide lubrication.
Lubrication principles can be divided into two kinds:
Boundary Lubrication.
Lubrication where the surfaces are the two objects rub against each separated by a very thin layer of lubricant so that in some locations is still friction between the two objects. See Fig.
• Lubrication Film.
By providing a layer of lubricating oil that is thicker (a film) between the two objects rub together, no longer the case friction between two objects. Principles of good lubrication is the lubrication film.
The main function of lubricating oil is for lubrication, while other functions are equally important for cooling, sealing, reduce corrosion, shock absorbers and control.
• As a coolant.
Friction will cause excessive heat can cause damage if material. Lubricating oil will absorb the heat is to be taken and disposed in the lubricating oil or cooling system to the outside air.
• As the seals.
Seals can be used as a lubricant, such as to prevent leakage of hydrogen from the alternator shaft to the outside air.
• To reduce corrosion.
Lubricants can reduce the rate of corrosion because it forms a protective layer on the metal surface so that direct contact between the substance causes corrosion of metal surfaces can be avoided or reduced.
• As shock absorbers.
Shock loads on engine components can occur, including the gears. Lubricant layer will lessen the impact between the gear surfaces intersect each other, so as to reduce vibration and noise.
Additives to improve the characteristics of lubricants, to suit their usage requirements. Additive: Chemicals that have received "Patent" from the factory.
 Detergent: to clean machinery
 Dispersant: to keep all the dirt floats / float in the lubricating oil
 Antioxdant: to prevent the process
 Anticorrosive: prevent kososi
 Antifrezing: to prevent freezing
 Increasing the viscosity index: to keep the lubricants remain fluid in cold temperatures
 Antifoam: to prevent foam
 Extreme Presure: to form a thin layer of strong, resistant to pressure
 antirust: to prevent the formation of rust due to the deviation of pressure





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Cycle of | Basic | Feed | Water | Heater


The main function of the Feed Water Heater is increasing efficiency in power plant steam cycle. Extraction steam from the turbine used to heat the feed water so that the Final Feed Water Temperature had passed (from point A to M). Feed Water Heater is basically a heat exchanger (heat exchanger). Power plant has 7 units of Feed Water Heater is 3 units of Low Pressure Heater (LPH 1, 2 and 3), 3 units of High Pressure Heater (HPH 5, 6 and 7) and the Open Feed Water Heater is Daerator. For LPH and HPH 5,6,7 1,2,3 is Close Feed Water Heater with shell and tube type heat exchanger.

Heat transfer occurs between the feed water temperature in the tube with extraction steam from the steam turbine and the drain of the Feed Water Heater on the top shell. Condensate Pump Condensate water is pumped by the deaerator through LPH 1, 2 and 3 respectively. Then the feed water is pumped by a Boiler Feed Pump (BFP) to the economizer to advance through the timber 5, 6 and 7. Another function of the heater is to improve the steam quality, which capture some steam at the turbine blade will reduce the wetness of steam, thereby reducing the effect of condensation heat transfer processes Most of the heater on the condensing section occurs. Although superheating made very high temperature, the heat transfer in desuperheating section remains small. Drain the cooling is the smallest part of the process of heat transfer in the heater.

Due to certain reasons such as tube leakage or leakage valve, feed water heater can be out of service (cut heater operation). In Design Manual Book (Hamen-Subelco Vol OI), the operation of the heater cut operation can be done with certain limitations. There are several parameters that must be observed particularly fibrasi problem and the maximum weight allowed when there are concessions in the out of service. However, the operation of the heater cut in a long time is not recommended because it will reduce the life time of the other heater. Turbine has been designed to anticipate the heater cut operation without overstressing the following conditions:
A. A condition
One or more non-contiguous heater (nonadjacent - one chasing turbine) can be out of service from the system.
Example: Heater 7, 5, 3 out of service. Load 100%
2. The condition B
If there is a heater that successive (adjacent) in the out of service then the load can still be maintained as long as there is above all the heater come on out of service.
Example: Heater 7, 6, 5 out of service. Load 100%
3. The condition C
Turbine heater can be operated with the highest in service and a combination heater out of service sequentially below. Load must be reduced 10% when there are 2 consecutive heater out of service, reduced 20% when there are three successive heater out of service. Reduction of the maximum allowable load is 50% of the nameplate. Loading beyond these limits is the responsibility of the owner.
Example: Heater 6, 5 out of service. Load 90%
Heater 6, 5, 3, 2 out of service. Load 90%
Heater 6, 5, 3, 2, 1 out of service. Load 80%







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Tuesday, March 13, 2012

Clarification | of the actual design | and capacity | Condenser


The condenser is a heat exchanger type of contact is not directly aimed at changing the steam from the turbine into the water so it can be re-circulated by the cooling method derived from seawater that is pumped by the CWP (circulating Water Pump).
Expenses received by the condenser can be calculated by the following formula:
P = Pg (HR/3600) - (104/ηm ηg)
where,
P = Load Condensor, kW
Pg = Electrical output, kW
HR = heat rate, kJ / kWh
ηm = Mechanical efficiency turbine-generaztor (approximately 99.5%)
ηg = Generator electrical efficiency (about 99%)
While the heat balance on the condenser can be calculated using the formula
Qcw = P / (cp (θ1 - θ2)
where,
Qcw = flow of cooling water, kg / s
P = load condenser, kW
Cp = specific heat, kJ / kg K
θ1 = temperature of cooling water into the condenser, C
θ2 = temperature of condenser cooling water exit, ° C


To clarify the design of the cooling capacity is needed, we must first know the condenser load (the energy that goes into the condenser) with a simple calculation using the formula: P = Pg (HR/3600) - (104/ηm ηg).
Turbine heat rate (HR) performance of data taken from test unit 2 of 1980 kcal / kWh (Appendix 1) at 300 MW load.
Pg = 300 MW
HR = 1980 kcal / kWh = 8290 kJ / kWh
P = 300 MW ((8290 kJ / kWh) / 3600) - (104 / (99 x 98))
P = 381.62 MW
Condenser load of 381.62 MW obtained. Clarification was required cooling capacity can be calculated using the heat balance in the condenser by the formula:
Qcw = P / (cp (θ1 - θ2)
Clarification of the cooling capacity required by the operational one CWP
θ1 = 26 ° C (temperature into the condenser with a pump CWP)
θ2 = 44 ° C (the temperature of the condenser with one pump out CWP)
cp = 4.08 J / kg K
Qcw = 381.62 MW / ((4:08 J / kg K) (44 oC - 26 oC)
Qcw = 5190 kg / s = 5.06 m3 / s
The actual flow flowing at 5:06 m3 / s flow capacity of the pump close to CWP. This proves that with a CWP able to load the actual unit of 300 MW but the consequences condenser outlet temperature of 44 oC.

Clarification of the required cooling capacity is based on two operational CWP (design)
Calculations can be performed using data from the design of the condenser inlet temperature and outlet temperature of the condenser.
θ1 = 26 ° C (the temperature of the condenser with two pumps into CWP)
θ2 = 34 ° C (the temperature of the condenser with two pumps out CWP)
Qcw = 381.62 MW / ((4:08 J / kg K) (34 oC - 26 oC)
Qcw = 11 678 kg / s = 11:39 m3 / s
Flow calculations for 11:39 m3 / s near the pump flow capacity of 2 CWP. So it is true CWP design 2 x 50% with the condenser inlet temperature of 26 ° C, the condenser outlet temperature is 34 oC.



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