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PROJECT REPORT ON
"FULLYAUTOMATED BURNER MANAGEMENT SYSTEM USING PLC"

FACT (THE FERTILIZERS AND CHEMICALS TRAVANCORE LIMITED) was set up in 1944 on the banks of river Periyar at Udyogamandal, Ernakulam. In decades that followed, multistage expansion programming was undertaken bringing in the latest technology of the days, which were quickly mastered and I successfully implemented.
In 1962, FACT came under the government of India. A second fertilizers production unit called Cochin Division (CD) at Ambalamughal and two Engineering divisions FACT Engineering and Design Organization (FEDO) and FACT Engineering Works (FEW) were established. FACT; a government of India enterprise has business interests in manufacturing and fabrication of equipments.
The company has also interests in fields like Petrochemical, Hydro metallurgy, Chemical and Pharmaceuticals etc. Products like Factmfos, Urea gained wide popularity. Next hosting point came with setting up of international standards and is mainly used in production of Nylon. FACT'S next endeavor was 900 TDP ammonia complex, which was set up in Udyogamandal Division (UD) with Japanese collaboration. Now despite a few financial problems, FACT is still growing.
FACT has capital employed of Rs 650 crores and its turnover around Rs 1210.04 crores. FACT has three manufacturing divisions, two at Udyogamandal, Eloor, one at Ambalamedu near to Cochin Refineries. The overall production is in the range of 2.85 lakh tonnes of nitrogen, 1.5 lakh tonnes of Phosphate and 50000 tonnes of Caprolactum. It has wide range of fertilizers from straight fertilizers like Ammonium Sulphate and Urea to Complex fertilizers. It has successfully branched out into the field
| of Chemicals and Fertilizer Technology Engineering and Design capabilities, R&D and

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Guided by,
Sri. SajiP Varghese Dy. Chief Engineer of Utility Dept. of FACT Udyogamandal Division
Submitted by,
Gibin George Liju P Muttath Ratheesh T R Syam Mohan Alphonsa Roslin Paul

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I Fabrication Engineering Services.
Dept. of Electrical & Electronics
POWER DISTRIBUTION IN FACT
FACT Udyogamandal is getting power supply through two 110KV feeders, from the 220KV substation, Kalamassery. Normally one feeder will meet the full demand of the Udyogamandal complex and the other feeder will always be spare, kept isolated in FACT 110KV yard.
Two transformers 1&2 of AEI England make of 15MVA Capacities and other two 3&4 of TELK make of 12.5/20MVA rating. All the four transformers step down the 110K.V voltage to 11KV. The 11KV secondaries of the 1&2 transformers feed JYOTHY Panel and secondaries of 3&4 transformers feed ALIND Panel. Transformers 1&2 are provided with off-load tap changing system, where as 3&4 are provided with on-load tap changing system. All the transformers can be isolated on load at 110KV side by outdoor 110KV SF6 circuit breakers. For the improvement of system power factor two capacitor banks of 1940KVAR and 970KVAR capacities are provided in the 110KV substation. One 970KVAR capacitor is connected at 11KV substation and one 500KVAR bank at S02 acid substation.
There are two outdoor transformers of 5MVA capacity in the 110KV substation, of TELK make which step down 11 KV to 3.3KV to feed NGEF/TMG, 3.3KV panel in the substation. 11KV outgoing feeders from the Jyothy Panel feed the primary sides of six 5MVA transformers in the intermediate 11KV substation.
Demand for the total Udyogamandal complex including Petrochemical division and new 900TPD Ammonia plant is met through separate duplicate 11KV feeders from the Alind Panel. The station low tension demand of the 110KV substation is met by one 750KVA indoor station transformer. The 110KV control panel facilitates remote control of 110KV breakers, the necessary metering and all the
protective relays. TOD meter installed in the 110KV control panel measures various parameters for both recording and billing purpose.
Power is received at the 11OKV substation in FACT Udyogamandal division and distributed to various plants in Udyogamandal division, apart from sending power to FACT Petrochemical division and new Ammonia plant. Besides the KSEB supply, power is generated in the complex by two Turbogenerator units. They are of 6MW capacity in Ammonia plant and 16MW capacity in Petrochemical division. Power can be received and sent from the 11 OKV substation through interconnecting feeders.
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Figower Distribution in FACT
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The present average energy demand of Udyogamandal division is about 2.85 Lakh units per day with a maximum contract demand of 16MVA.
Running load of various plants in FACT Udyogamandal division is;
DCDA acid plant - 1.5MW
S02 Oleum plant - 1.2MW
Ammophos 300 TPD plant - 0.63MW
Ammophos 150 TPD plant - 0.48MW
Phosphoric acid plant - 0.83MW
Ammonium Sulphate plant - 1.10MW
Filter Bed - 0.83MW
Township and Miscellaneous - 1.04MW
SYNOPSIS
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This project titled "FULLY AUTOMATED BURNER MANAGEMENT SYSTEM USING PLC" is almost entirely centered on the boiler plant |t Ammonia complex of "THE FERTILIZERS AND AGRO-CHEMICALS Ltd, T.RAVANCORE (FACT) unit located at Udyogamandal, Kalamasserry, Ernakulam, Kerala. The plant is equipped with most modern electronic system and hence our exposure to them provide truly beneficial. We begin our work with the study of boilers |hd boiler controls implemented at the plant making use of PLC programmers and. Literatures.
The project aims at different objectives such as automation of plant and energy saving by continuous operation by PLC control, reduction of capital cost and time lost. A programmable logic controller is proposed to be incorporated for the Automation part of project. PLCs have short period of time played a major role in the (evolution of automation both in discrete and process application in industrial control. iPLCs are being used extensively in control system now, where electromechanical relays were in use formerly. The introduction of PLC will make the system more flexible, easy up-gradable and maintenance-friendly.
The project deals with burner management system using ^PLC in boiler process which supervises the control of the fuel burning equipment and :provides all monitoring facility for safe and smooth startup and shut down of boiler.
OBJECTIVES OF PROJECT
Complete automation of burner operations by controlling fuel and steam inputs to the burners.
To meet safety requirements of boiler process control systems.
To provide reliable and efficient operation of system by modifying
interlocks/protection using PLC.
To reduce initial cost & maintenance cost by reducing hardware circuits with relay.
PLCs are programmable according to the requirement.
Application of PLCs ensures continuous operation and there by we can
avoid increased rate of Energy consumption due to frequent starting &
tripping.
PLC ensures the proper burning of fuel in the boiler.
CAPTIVE POWER PLANT
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¢ INTRODUCTION
Captive Power Plant (CPP) is the power generating unit of Replacement Ammonia Plant (RAP). Main objective of CPP is to provide steady and continuous power. In CPP, steam is produced and using this steam Six Megawatt of electric power is generated. It supplies electric power to all processes equipments in Ammonia complex and also supplies steam to the main steam line to cater to the entire process steam requirement.
CPP consist of two boilers which are capable of producing 60 tones of superheated steam per hour with a temperature of 520 degree Celsius and a pressure of 110 ata, this steam is supplied to all major steam line.
In CPP mainly four steam lines are used. They are classified as follows;
1) High pressure steam lines -110 ata
2) Medium pressure steam lines-42 ata
3) Low pressure steam lines-12 ata
4) Exhaust steam line-3.5 ata
Steams thus obtained are used for driving turbines, chemical process requirements, heating purposes etc.
In CPP nine turbines are used. Steam inlet of 110 ata (HP) is used for driving Turbo Generator (TG), which generates Six Megawatt of electric power. All other turbines are used as prime movers for the pumps. Steam inlet of 42 ata is used for driving these pumps.
¢ BOILER FEED WATER SYSTEMS
In water management system, which supplies pure water for the jproduction of steam, the water provided should be de-mineralized and de-oxygenated .The pH level is maintained at 9. Boiler feed water system includes:
1) De-Mineralized Water Tank (DM Water Tank)
The DM water supplied from the DM plant is stored in the DM tank. The water for the boiler is stored in this DM tank. A constant water level is maintained in this. A steam driven pump and a motor driven pump are used for pumping the DM water from tank to the next stage, which is de-aerator
2)Deaerator
Before the water is supplied to the boiler, the oxygen content should be removed. This is done in this equipment. The temperature of the water is raised 110 degree Celsius. The level control valve is used to control the water level in the deaerator. Level switches for high and low levels are also incorporated in the deaerator. The water is pumped from the deaerator to the next stage.
3) Dosing
Dosing is a process which is done to maintain a constant pH of 9 in water before it is supplied to the boiler. This process has been undertaken along with the suction of the pump. Ammonia is used for this purpose. The dissolved oxygen is removed by dosing Hydrazine. Both Hydrazine and Ammonia are added to suction input of boiler feed water pump.
¢ BOILER AUXILIARIES
1) Economizer
Water from the boiler feed water pump reaches the economizer. Here the temperature is raised to about 210 Degree Celsius. This is done to enhance the Bteam generation. The economizer inlet is connected to feed pump and the out let is connected to steam drum.
2) Boiler Drums
Boilers consist of two cylindrical drums which are placed one above the other which are separated by tube lines. The upper drum is called Steam drum and the lower one is called Mud drum. The super heated steam of 110 ATA is obtained from the steam drum. Heat exchangers are used for the exchanging flue gas temperature to the steam. Heat exchangers are connected to the steam drum
3) Flue Gas Exhaust System
This system provides a negative pressure inside the furnace. It is [provided before the stack. The flue gas is expelled through the stack using Induced Draft
(ID) fan. Rate of removal of flue gas is controlled by using ID fan, so as to provide a t negative pressure. The negative pressure concentrates the flame throughout the furnace. | The burned fuel is removed from the furnace using ID fan through stack. The harmful
gases are reduced and exhausted through the stack to the atmosphere.
. 4) Super Heater
The saturated steam from the steam drum flows to Low Temperature Super Heater (LTSH) located in the duct connected between boiler banks and economizer, then to platen super heater or directly from drums to platen super heater located in the upper furnace area. The steam then flows to final super heater through a spray type de super heater and then passes on to the main steam line. In case of single
stage super heater, steam from the drum flows to super heater. The steam then flows to
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plain steam line through spray type de super heater
^ 5) De Super heater
De super heaters are provided in the steam line between super heaters or between super heater and main steam line to permit reduction of steam temperature when necessary and to maintain the temperature at designed values with in the limits. Temperature reduction is.accomplished by injecting spray water in to the path of steam through a nozzle. The spray source is from the boiler feed water system. It is essential that the spray water be chemically pure and free of suspended and dissolved solids, containing only approved volatile treatment material in order to prevent chemical ¦deposition in the super heater
I
,6) Combustion
The furnace oil is the fuel used for the combustion. Oxygen needed for burning the fuel is delivered by FD fan in to furnace from atmosphere. The air is pre heated using steam coil air preheater. The air is further heated by the heat of exhaust flue gas in the tubular air pre heater. The fuel for combustion is injected into the furnace by using oil burner. Four oil burners are provided to get a uniform flame distribution inside the furnace. The oil burners use steam at 12 ATA for atomization of the fuel oil. Atomization results in fine spray of oil, which leads to complete combustion.
7) Soot Blowers
Soot coated on the inside parts of the boiler have to be removed periodically. This is done by soot blowers. For this purpose two types of soot blowers are used, rotary soot blowers and long retractable soot blowers.
¢ BOILER STEAM SYSTEM
. Steam of 110ATA with a temperature of 520 Degree Celsius is provided and supplied to the main steam line by the boiler steam system. The feed water enters the economizer and is heated to about 210 Degree Celsius. The water is supplied to
I the boiler at the steam drum. A particular water level was maintained in the steam drum.
i For maintaining the required water level during changed boiler load conditions, a boiler drum level control valve is used. The water reaches the lower mud drum through water wall tube lines. The water changes to steam at these tubes. In the steam drum, this mixture of water and steam gets separated in the steam separator, and the water is again
; fed down through water wall tubes. This process is repeated and constant steam level is maintained at the steam drum by the drum level control scheme. This steam has to be
.superheated. The steam then flows into the Low Temperature Super Heater (LTSH) where the temperature increases and condensates are removed. Further steam is passed through the Platen Super Heater (PSH) where the temperature of steam raises around 600 degree Celsius. This temperature is reduced at the de super heater, where the water is I sprayed for this purpose. The final super heater is used to maintain a temperature of 520 degree Celsius. The superheated steam with temperature of 520 degree Celsius and pressure of 110 ATA is supplied at super heater header.
The water supplied at the steam drum is mixed with the phosphate. This is also a type of dosing for reducing the hardness of water. Tri-Sodium phosphate is used for this purpose. It heaps to increase the pH and make the hard water loft.
PSH - Platan Super Heater FSH - Final Super Heater OBD - Observation Door RSD - Rotary Soot Blower CAD - Circular Access Door IH - Inlet Header OH - Outlet Header
LTSH - Low Temperature Super Heater
El - Economiser 1
E2 - Economiser 2
TAH - tubular Air Preheater
SCAPH - Steam Coil Air Pre Heater
AD - Access Door
LRSB - Long Retractable Soot Blower
¢ BURNER DATA SHEET
Project: 2*60 TPH. Boiler-FACT, Udyogamandal.
\ Boiler Data
Number of boilers -2
Capacity -60 TPH
Furnace Data
Furnace width -4877 mm
Furnace Depth - 6401 mm
Type of furnace operation -Balanced Draft furnace
Burner
Number of burners/boiler - 4
Type of burner -Oil fired burner
Type of fuel - LSHS/furnace oil
Type of atomization - constant pressure steam
atomization.
Burner Location
Burners are located on the furnace front wall at two elevations with (wo burners in each row. It is proposed to provide common wind box with bottom entry having two burners in each elevation.
The cooling air shall be available at pressure of at least 250mm WG above the maximum surface pressure.
Igniter - 1.20.000 btus/hr LPG(propane) Type of igniter - gas electric with ionic flame monitoring system.
Number of igniters - 1/Burner Igniter capacity -0.038*10A6 LPG pressure at igniter - 0.35 Bar
Scanner
Number of scanners - 1/Burner
Type - I.R.. with self checking feature.
BOILER OPERATION
The boilers installed in CPP of Ammonia Complex are furnace oil fired, balanced draft type with four oil burners in two tier formation. The output steam ¦ parameters are 525 deg. C, 110 kg/sq.cm. The operation of this boiler can be broadly \ divided into:
f Preparation for start-up
¢ Start-up of Boiler (Lighting of Burners)
¢ Pressurization and attaining rated parameters *¢ Loading of Boiler.
Preparation for start-up
Prior to the lighting up of the boiler, the boiler has to be totally, boxed up in the feed water, steam, and air / flue gas sides, i.e., all maintenance work should be made over and all the manholes, etc. should be closed. The boiler drum shall be filled with adequate amount of feed water (de-mineralized water). The ID and FD fans | shall be made run with air flow more than 30% of rated full load value. The steam coil air j pre-heater shall be put in service so that hot air enters the furnace and leaves through the ! stack (chimney). ID fan speed shall be adjusted to get proper negative pressure in the j furnace. All boiler drum and steam line vent valves should be kept open. All the burner j guns should be cleaned and fixed in position. The furnace oil shall be heated up in the oil j pump house and the hot furnace oil shall be circulated upto boiler trip valve and returned j back. This is for maintaining required temperature of Furnace Oil to the burners. Oncej the required temperature of Furnace Oil has been achieved and all other boiler trip conditions have been reset, and the boiler is ready for light-up.
Btart-up of boiler
Once the preparations for start-up are over, Boiler purging start command should be given. This will initiate a 5 minute sequence whereby it is positively (ensured that any unburnt material inside the furnace has been properly evacuated and the furnace is safe for introducing flame. (The steady air flow is maintained during these 5 [minutes by FD/ID fans). Once purging of the boiler is over, the trip valves (Ignitor Gas itrip valve, Atomizing Steam trip valve and Furnace Oil trip valve) are kept opened.
The first step in lighting up the boiler is the lighting up of ignitor. lEach burner gun is provided with a pilot ignitor which uses LPG for burning. Upon giving Ignitor ON command, an electric spark plug initiates the ignitor firing. Upon [successful firing of LPG, the ignitor flame scanner gives positive signal and the electric Ipark is withdrawn and LPG valve of that particular burner stays on. This will facilitate she lighting up of main burner (Furnace Oil burner). The usual practice is to light up any of the two burners in the bottom tier.
Once ignitor flame is established, the burner start command is fgiven. This will initiate a scavenging sequence at first. During scavenging, atomizing feteam is let to both oil path and steam path of the oil burner gun. This will help in heating ^ip of the burner gun internals (so that when furnace oil is let in later, it does not solidify inside the gun) as well as to do a final cleaning. Once the scavenging is over, the ^scavenging valve (which lets atomizing steam in to the furnace oil path of burner gun) jcloses and furnace oil valve (oil burner trip valve) opens. In this condition, at the burner tip, the furnace oil enters the furnace in a fine spray form (due to atomizing effect of isteam) in front of the ignitor flame which is already present there. The furnace oil spray gets lighted up due to the ignitor flame, and the oil flame gets established. This is confirmed by the oil flame scanner and burner ON indication is received. By visually ^.confirming the healthiness of the oil flame (through view glasses provided on the side of jthe boiler), the ignitor flame is stopped. In this condition, the main flame stays lit, and the
heat of the flame starts getting absorbed by the feed water inside the boiler water walls. Due to any reason, if the main flame fails; we have to again start ignitor, do scavenging of the gun, and then light up again. Once all the oil burners come on line, the ignitor trip valve is closed.
Pressurization and attaining of rated parameters
Once the burner is lit up, it can be seen that the boiler temperature starts increasing. This cannot be allowed to rise beyond some safe rate of rise. For the same, the boiler start-up curves are to be followed. For maintaining the required rate of rise of temperature, it will be required to control the oil flow through the burner, taking care not to reduce the oil pressure below the trip value. Start-up curves are designed keeping in view of the allowable thermal stresses on the boiler pressure parts and their expansion, etc.
Once the water temperature exceeds 100 Degree Celsius, steaming starts and steam starts escaping through drum vents. These vents are gradually closed. The steam produced will then flow through the super heater coils and the super heaters start getting heated up. Steam escapes to atmosphere through main steam start-up vent valve. All the while, the boiler start-up curves are to be followed strictly, whereby rate of rise of boiler pressure / temperature is to be maintained. The rate of rise of steam pressure is controlled by a combination of adjusting oil quantity and throttling of main steam vent valve. As the steaming starts and venting of steam occurs, a close watch shall be maintained on the boiler drum level. The drum level drops and the same shall be normalized by giving feed water so that safe level is always maintained in the drum.
Once the boiler attains pressure of around 90 kg/sq. cm, the quantity of steam vented becomes more and it may necessitate lighting up of one more oil burner so that the required rate of rise of steam pressure can be maintained. Once the main steam temperature and pressure reaches rated values, the boiler is ready for loading.
[Loading of boiler
For loading the boiler, the main steam stop valve (which is the main outlet valve) is gradually opened, and the start-up vent is gradually closed. This diverts the steam flow from escaping to atmosphere there by feeding the steam requirement in downstream steam lines. The steam generation will have to match with the steam requirement in real time. Depending upon the need of the downstream steam consuming plants, the flow varies. If the quantity of the oil fired is kept constant, this will lead to fluctuation in steam pressure, and it may lead to even tripping of the boiler. It is here that the boiler load control comes into action. A closed loop controller always monitors the main steam pressure and sends corrective signals to the oil / air flow controllers. Oil flow is controlled by oil flow control valve and air flow by varying the FD fan speed. As the FD fan speed varies, ID fan also varies automatically so as to maintain safe negative pressure in the furnace. The steam coil air pre-heater is isolated once the exit flue gas temperature goes above 135 Degree Celsius which is the acid dew ipoint.
The oil flow is always limited to the lowest of two values: oil flow permissible for the present air flow or signal from main steam pressure controller. Similarly, air flow is always maintained as highest of the following two values: air flow permissible for the present oil flow or signal from main steam pressure controller. This logic is followed, so that the furnace is never starved for air, which is a potentially dangerous condition. So, while the boiler main steam pressure control system is on auto mode, it can be seen that when steam pressure goes up, the oil flow reduces first, then followed by air flow. And when steam pressure goes down, the air flow increases first, followed by oil flow. For safe operation, it is normal practice to monitor the oxygen [content in flue gas, which indicates the quantity of excess air fed to furnace.
The boiler can be loaded upto around 35 T/hr. with two oil ' burners. Beyond that, the top tier oil burners are also lighted up. To have a uniform
j|jii||iiM«»js^^ ¦ -
heating up, usually all four burners are lighted up beyond 20-22 T/hr. boiler load. For maintaining steam temperature at higher loads, de-superheater water spray is given between platen super heater and final super heater. This is called attemperation. A closed loop control monitors the main steam temperature and adjusts the feed water spray (attemperator water flow) so as to maintain the main steam temperature.
BOILER PROCESS CONTROL SYSTEM o INTRODUCTION
The boiler plant installed at Ammonia Complex, Fact, Udyogamandal is mainly meant for producing steam to run the turbine which in turn generates the power required to run the various plants which produces chemicals to be 'used in fertilizers.
Boiler requires special treatment in their control because of the complexity of their numerous controllable parameters and control actions. The requirement for the reliable and efficient operation of the boilers coupled with those of the steam consumers makes the problem of boiler control sufficiently complicated. The consumer consumes steam at specified pressure and temperature and by a specified (amount per unit time.
Basically the boiler plant consists of a furnace process and a steam vessel that handles the pressure and the temperature. For the boiler plant to operate well the furnace process should have maximum efficiency-this in relation to fuel and air inlet supplies as also the furnace pressure. The general types of boilers are drum type ones and the water level in the drum should be with in the prescribed tolerance limit. Thus the variables that need to be controlled for operation of boiler plant are fuel, air, feed water, fuel suction and draught, coolant supply for temperature control of de super heaters etc.
Boiler control is accomplished by means of two systems:-
1) The burner management system
2) The combustion control system
3) Programmable Logic Controller (PLC) based Burner management system which supervises the control of the fuel burning equipment and provides all the monitoring facility for safe and smooth startup and shutdown of the boiler. '
4) Distributed Control System (DCS) based combustion control system, designed to maintain the header steam pressure constant under any boiler load. Flow of fuel and combustion air is controlled by master steam pressure controller. Air rich conditions are maintained to ensure optimum combustion under any load change. After through and exhaustive study of these two systems, we suggested a few modifications aimed at better more efficient and safer operation of the plant. We brought about changes in the program and advised practical circuits for implementation in the plant, for this purpose.
o BURNER MANAGEMENT SYSTEM
The burner management system must essentially provide automatic sequence of operation of connected boilers during start up and its shutdown. It should also indicate the operator the existing states of various elements of fuel burning equipment. The system must indicate safe shutdown procedures as and when an unsafe operating condition is detected.
o COMBUSTION CONTROL SYSTEM
The combustion control system is designed to feed the fuel and air to the furnace to produce the system at a given constant pressure depending on the requirement of boiler load. The set point of the fuel and air controllers is adjusted and a corrective output signal is produced.
Ultimate aim of combustion control system is to deliver steam at constant pressure as per demand economically by effective utilization of fuel. Optimal combustion
takes place in slightly excess of air and also there exists a definite ratio between air and fuel in a combustion system. Thus the four inputs to combustion control system are:
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1) Fuel flow
2) Air flow
3) Present steam pressure
4) Percentage of oxygen
There are two outputs:-one for opening of fuel flow control valve and another for forced draught fan. These then form the set point of fuel and air controllers and a corrective signal is produced.
¦ THE BURNER MANAGEMENT SYSTEM
> START UP SEQUENCE )
The BMS supervises the admission of fuel and air into the boiler ,
..and it also provides all the ON/OFF control and monitoring necessary for safe and
[smooth start up and shut down for the boiler. The start up and shut down is done in a
sequential order. The sequence is as follows;
Furnace Purge
Before any fuel firing can take place (initially or) after a Master
Fuel Trip, a satisfactory furnace purge cycle must first be completed. For a satisfactory
furnace purge, the following are essential.
\ 1} Establish Logic power and power for Ignitor, Scanner and illumination to
BMS.
2) Establish proper drum level ;
3) Put ID fan into service ¦
4) Put FD fan into service !
5) Establish proper purge air flow by manually increasing the air flow until a
minimum of 30% of full load air flow is established
6) Ensure scanner shows no flame
7) Start furnace purge cycle by depressing the "Purge Start" push button
after "Purge Ready" light comes on indicating that all the purge
requirements are satisfied
._.
Note : 1
The "Purge Ready" light will not come on unless all the following requirements are satisfied.
1) ID Fan is operating
2) FD Fan is operating
3) Air Flow greater than 30%
4) Drum level is not very low
5) Furnace pressure not very high
6) Emergency trip push button not depressed
7) All scanners Show no flame
8) HOTV closed
9) All OBTV closed
10) Any Burner Air damper Open
11) Furnace pressure not very low
12) IGTV closed
When the flame purge cycle is started, "Purging" light comes on and remains on during the entire five minutes of purging cycle.
Note: 2
At the end of furnace purge cycle(five minutes)
. 1) The Boiler Trip (or Master Fuel Trip) and purging light goes out 2) The "Purge Complete" light comes on
Ignition Start
After purge complete, any ignitor can started provided "Ignitor start Permit" light is ON. The ignitor start permit light is on when the following requirements are satisfied.
1) NoMFT
2) Ignitor Gas Pressure is not low
3) IGTV open PB is depressed
4) Burner Air Damper open
Pressing the IGTV open push button Ignitor Start Permit light comes on and will open the Ignitor Gas Trip valve.
After the Ignitor Gas Trip valve is opened when the Ignitor proves no flame, the "Ignitor ON" push button is pressed energizing the mixer block (Air & Gas) solenoid valve for 10 seconds allowing the mixed gas flows through the Ignitor. Now the Spark Plug produces spark and mixed gas fired by the sparks.
During the Ignitor trial time of 10 seconds, if the Ignitor flame is not established, then the Ignitor Gas valves closes and Ignitor has to be re-started.
Heavy Oil Start
For the "Heavy Oil Trip Valve" does not open, check to see that;
1) Oil Pressure is OK
2) NoMFT
3) Oil Pressure not very low
4) Atomizing Steam Pressure not very low
tOil re-circulation must be done before opening the HO Trip Valve.
Oil Firing
Once the Ignitor is in service, and the Heavy Oil Trip valve is opened. Oil firing can be started by opening the "Oil Burner Trip Valve", proceed as follows;
1) Oil Gun to be Engaged
2) Burner Air Damper to be Opened
3) Atomizing Steam Manual valve opened
4) "Oil Start Permif light is on, indicating that permissives are satisfied to open the Burner Trip valve by depressing oil burner on push button (ie OBTV 1 is ON). Similarly for other three Burners.
Note : 4
If the "Oil Start Permit" light does not come on, check to see that;
1) HOTV opened
2) Atomizing Steam Pressure not low
3) HO Manual valve is opened
4) Atomizing Manual valve is opened
5) HO temperature is not very low
6) Scavenge valve closed
7) Ignitor is ON
When Oil Burner on push button is depressed the Atomizing Steam valve is opened first. Then, Oil Burner Trip valve will be opened and indicated by the light coming on.
The first scanner must prove flame at this time. If the flame is not proven with in 10 seconds of the opening of the Oil Burner trip valve, then the OBTV will be closed and the scavenging to be started by depressing scavenging valve open PB
and automatically stopped after 3 minutes . if the scanner proves flame, then OBTV-remains open. Similarly for OBTV-2, OBTV-3& OBTV-4.
Note : 5
The Burner should remain in the " Low Fire Start" position until steam is delivered to the system.
Any one of the following conditions will cause a Master Fuel Trip to occur and results in the immediate shut down of all fuel in service, which necessitates a Furnace Purge Cycle completion before any fuel firing may be re-instated.
1) Furnace Pressure very high
2) Drum level very low
3) ID Fan not operating
4) FD Fan not operating
5) Emergency Push Button initiated
6) Air flow less than 30% of full load
7) All scanners show no flame
The flow chart for the whole sequence is given below;
FLOW CHART
START
Close HOTV and IGTV if Open
STOP
Indicate Purge Ready
Press Purge Start Push Button
O
Indicate Purging
Purge Complete Permanently
Indicate Igniti an Start Ready
Press Ignition Start Push Button
Indicate HOTV Open Permit
Indicate Ignition Established Signals
Press HOTV Open Push Button
Indicate HOTV Open Permanently
Press OBTV Open Push Button
Press IGTV Open Push Button
Indicate OBTV Open Permanently

Burner on Indication

Close IGTV
STOP
> CONTROL SEQUENCE
Burner management is the control of fuel burning equipment required on steam generator for safety operation. In the early days of burner management, it was carried out by field wiring of various devices in series and parallel to perform the required logic sequence and safety interlocks.
The burner management system provides proper sequence of equipment during the normal startup, operating and shutdown procedures. In addition, it provides for a fuel trip during adverse boiler or burner operating condition. This is accomplished through the use of programmable logic and various interlocks.
In the boiler system installed at FACT, Udyogamandal, the burner management system serves the boiler to fire through four independent burners. Each burner is equipped with main oil gun for firing steam atomized heavy oil. It is also provided with a gas ignitor, flame scanner for scanning the flame.
The burner management includes different controls, following below;
¢ Purge Control
¢ Ignition Gas Trip Valve Control
¢ Ignitor 1,2,3,4 Controls
¢ Heavy Oil Trip Valve Control
¢ Oil burner Trip Valve 1,2,3,4 Controls
. ¢ Scavenging Trip Vah e 1,2,3,4 Controls
Each of these controls is maintained by certain conditions. So this gives the complete management of the burner. This is carried out by means of the programmable logic controller. If any one of these condition is wrong the PLC can take the necessary action according to the software installed on it.
The conditions for each section are given below.
Purge Control
Before a fuel firing; after a master boiler trip, a satisfactory
furnace purge cycle must be completed. Purging is nothing but a cleaning of the furnace. During these cycles all the fuel valves are closed, only the FD and ID fans are operated, so the ID fan takes away all the air (and possible unburnt / combustible gases) from the furnace through the stack. For a satisfactory furnace purge, the following are essential:
¢ ID fan is ON
¢ FD fan is ON
¢ Air Flow greater than 30%
¢ Drum Level is not very low
¢ Furnace Pressure is not very high
¢ Establish proper drum level
¢ All scanners show no flame
¢ All Oil Trip Valve are closed
¢ Heavy Oil Trip Valve is closed
¢ Ignition Gas Trip Valve is closed
¢ Furnace Pressure not very low
When the furnace purge cycle is started, "purging" light comes ON and remains on during the entire five minute of purging cycle. After this five minute the "purge complete" light comes ON.
Ignitor Start
After purge is completed, any ignitor can be started, provided "ignitor start permit" light is ON. The ignitor start permit light is ON when the following requirements are satisfied:
¢ No Master Fuel Trip(MFT)
¢ Ignitor Gas Pressure is not low
¢ IGTV open press button depressed
¢ Burner Air Damper open
Pressing the IGTV open push button"Ignitor Start" permit light comes ON and will open the Ignitor Gas Trip Valve (IGTV). After the IGTV is opened when the ignitor provides no flame, the "Ignitor ON" push button is pressed thus energizing the mixer block solenoid valve for 10 sec allowing the mixed gas flow through the Ignitor. Now the spark plug produces spark and mixed gas fired by the spark. During the ignitor trial time of 10 sec, if the ignitor flame is not established, then the ignitor gas valves closes and ignitor has to be restarted. When ignitor flame is established, "Ignitor ON" lamp gets lighted up and further oil burner starting permissive is given.
Heavy Oil Control
By this section we can control the flow of furnace oil to the burner. For opening the heavy oil trip valve some conditions must be satisfied as given below:
¢ Oil pressure is in the required range
¢ No MFT
¢ Atomizing steam pressure not very low
¢ Oil temperature is in the required level
The oil must be recirculated before the opening of the heavy oil trip valve
Oil Firing or OBTV Control
Once ignitor comes into service, and the heavy oil trip valve is opened, oil firing can be started by opening the "Oil Burner Trip Valve" which gives oil to the individual burners. The conditions for oil firing are given below:
¢ Oil gun to be engaged
¢ Burner air damper to be opened
¢ Atomizing steam manual valve opened
¢ Corresponding Ignitor is ON.
"OiJ Start Permit" light is on, indicating that conditions are satisfied to open the Burner Trip Valve by depressing "OBTV 1 ON" push button, similarly for all other three burners. If the "Oil Start Permit" light does not come ON, check the following:
¢ HOTV opened
¢ Atomizing Steam Pressure not low
¢ Heavy Oil manual valve is opened
¢ Atomizing manual valve is opened
¢ Heavy Oil Temperature is not very low
¢ Scavenge Valves are closed
¢ Ignitor is ON
When "Oil Burner ON" push button is depressed, the atomizing steam valve is opened first. Then oil burner trip valve will be opened indicated by the light coming ON. The flame scanner must prove flame at this time. If the flame is not proven with in 10 sec of the opening of the oil burner trip valve, then the OBTV will! rbe closed and the scavenging to be started by depressing "scavenging valve open" Push
button and automatically stopped after 3 minutes. If the scanner shows flame, then OBTV 1 remains open. All the OBTV's are operated in the same way.
Scavenging
It is the process of firing out the heavy oil inside the burner gun after a main flame trips. The furnace starts by firing LPG and goes on working by firing the heavy oil. So after a main flame trip the furnace starts with LPG, before this all the heavy oil must be fired.
When "scavenging valve ON" Push button is pressed it check for the following:
¢ Ignition start command
¢ All the OBTV's are closed
¢ All the scanners shows flame
The logic diagrams for all these sections are given below which shows the exact location of the various burners in the two boilers, position of various valves etc.
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> VERBOSE LISTING
BOILER LOGICS
1. Boiler Trip Settings
The following conditions will bring about a 'Boiler Trip', which logically means that Purging is required before re-starting.
Drum Level Very Low Drum Level Very High Furnace Pressure Very Low Furnace Pressure Very High Air Flow < 30 % ID Fan Trip FD Fan Trip
: 20 %( at rated pressure) : 80 %
: -250mmwc, 3sec. : +330mmwc : 26 T/Hr, 5sec.
2. HOTV Trip Settings
HOTV Trip will also physically bring about a Boiler Trip, but logically this does not demand a Purging before starting up again.
HO Pressure Very Low : 2.3 Kg/cm2
HO Temp Very Low : 80 deg. C
Atomizing Steam Pressure Very Low : 4 Kg/cm2
3. Burner Trip
This is for individual burner trip. However incase all four burners, trip, it will be physically a Boiler Trip but logically a Burner Trip only.
Flame Intensity : 60 %
4. 'Purge Ready'Permits
All 'Boiler Trip' conditions reset All Main Flames off All OBTVs close HOTV close IGTV close
5. IGTV ODen Permit
Purge Complete
Ign. Gas Pressure Very Low
6. HOTV Open Permit
Purge Complete
All 'HOTV Trip' Conditions reset
j 7. OBTV Open Permit
Purge Complete HOTV Open Ignition On
Oil Manual Valve Open Scavenging Valve Close Atomizing Steam Manual Valve Open Atomizing Steam Pressure not Low
8. OBTV / ATV Open Command Sequence
OBTV Open Permit | ; Oil Gun Engaged ->ATV Open Command OBTV Open PB Operated |
j ATV Open Command |->OBTV Open Command \ ATV Feedback |
9. Scavenging Valve Open Permit
OBTV Close Ignition On
BOILER AUXILIARIES LOGIC
1. Trip Settings of all Auxiliary Turbine
All these trips are operated through the local control panel. Turbine Oil Pressure Very Low : 2.5 Kg/cm2 Gear Box Oil Pressure Very Low : 0.8 Kg/cm2 Oil Temperature Very High deg. C : In the range
57-65 .
Over Speed : Approximately
+ 10%
2. Trip Settings of Boiler Feed Pumps
Deaerator Level Very Low : 17 % (approx)
Suction DP Very High : 0.8 Kg/cm2
Bearing Temperatures Very High : 80 deg. C
This trip is implemented through the local control panel for Turbo Driven Pumps and through PLC for Motor driven Pump.
Additionally, for BFP-3 (motor driven), Lube Oil Pressure Very Low trip is provided.
3. Deaerator Level Alarms
Deaerator Level Low Deaerator Level High Deaerator Level Very High
18 %(apporox) 85 %(apporox) 94 %(apporox)
4. Auto-Starting of Standby Equipments
i. Boiler Feed Pump
Pump will start automatically when the following conditions are satisfied:
a. Local/Remote Switch in Utility Desk is in
'Remote'
b. Auto/Manual Switch in Utility Desk is in 'Auto'
c. Local Control Switch is in 'Auto'
d. 'Ready for Start' indication is available at LCS
e. Pump Discharge common header pressure
is < 120Kg/cm2 or both turbo driven pumps are tripped / not running.
ii. Fuel Oil Pump
Pump will start automatically when the following conditions are satisfied:
a. Local/Remote Switch in Utility Desk is in
'Remote'
b. Auto/Manual Switch in Utility Desk is in
'Auto'
c. Local Control Switch is in 'Auto'
d. 'Ready for Start' indication is available at LCS
e. Any one of the turbo driven pumps is tripped / not running.
iii. DM Water Pump
Pump will start automatically when the following conditions are satisfied:
a. Local/Remote Switch in Utility Desk is in
'Remote'
b. Auto/Manual Switch in Utility Desk is in
'Auto'
c. Local Control Switch is in 'Auto'
d. 'Ready for Start' indication is available at LCS
e. Turbo Driven DM Water Pump is not /tripped.
> PRESENT IMPLEMENTATION OF INTERLOCKS & PROTECTION
In the existing control systems, the interlocks and protections are realized by means of electromagnetic relay based system. Here abnormal plant parameters are sensed by pressure switches / temperature switches / limit switches / flame scanners, etc. and reliable contacts are fed to the relays. The relay contacts are wired according to the above logics to derive certain output contacts. These relay output contacts in turn drive the various systems to allow starting the turbine, trip the running turbine, start auxiliary equipments etc. as per the logic.
The electro magnetic relay based system has the following drawbacks;
1. Since entire logic is hard wired between different relays, the reliability is low.
2. The probability of plant getting affected due to relay failure is more.
3. The relay, interconnecting wiring etc. takes up more space and also makes trouble-shooting difficult.
4. If any change in logic is required, it is very difficult to implement since lot of wiring will have to be changed physically.
> PROPOSED MODIFICATIONS OF THE INTERLOCKS & PROTECTION OF THE SYSTEM
In the view of inherent drawbacks of electromagnetic relay based system, it is proposed to replace the logic implementation using PLC's.The PLC programming based on the ladder diagram & details explained later.
After careful study and analysis of the boiler process control system installed at Ammonia Complex, FACT, Udyogamandal, we suggested a few modifications for better and more efficient operation of the plant. Some of the suggested modifications were very simple and did not require much attention while some others needed immediate attention.
Some modifications suggested include;
1. FD fan trip subsequent to ID fan trip.
2. Intercoupling of PLC & DCS.
3. Ratio bias controller.
(1) FD Fan Trip Subsequent to ID Fan Trip
A rather simplified arrangement of the boiler process control system is as shown
Stack
ID Fan
Air
Reg
ister
Furnace
FD Fan
Air from Atmosphere
Here, air required for combustion is forced into the boiler from the atmosphere by the Forced Draught (FD) Fan. After combustion, the flue gases are thrown out to the atmosphere through the stack, by Induced Draught (ID) Fan.
Now suppose, due to some reason, the ID fan gets tripped while the FD fan goes on working. Then, the gases accumulate with in the boiler developing very high positive pressures, which may damage the boiler and, eventually, lead to the collapse of the whole system. So for proper working of the boiler, it is essential that the FD fan gets tripped subsequent to ID fan trip. Also ID fan should run subsequent to FD fan start-up.
In the boiler plant at the Ammonia complex, no such
interlock exists to cause the same, at present. Hence operational facilities are to be incorporated for this purpose, as suggested by us, to ensure better safety of the plant. This could be done, by just modifying the PLC program. With a flag which indicates ID fan trip in front panel for PLC.
(2) Intercoupling of PLC & DCS
In the existing system, PLC & DCS are two different
sections, completely independent PLC, which monitors the existence of any unfavorable situation, work with digital values. DCS aims at continuous operation and hence, work with analog quantities. Now these two have to be coupled.
To illustrate the present situation, consider the following
examples. The airflow should always be maintained to some value corresponding to the load required. This value should be >30% for successful working of the boiler. If the airflow becomes <30%, the PLC should operate to trip of boiler. For this purpose, two flow transmitters have been installed FT2157 & FT2158, one for DCS & other for PLC.
FT2157
DCS
\
PLC
A/D Converter
Digital I/P
If air flow becomes < (86.2*30/100) T/Hr the trip amplifier is
activated.
The need for two such transmitters could be well avoided if we have accurate repeater or dual circuit like this.
DCS
Current
Repeater
(Dual)
\
PLC
The current repeater will have two outputs. It just duals the input and this is given to the DCS & PLC circuits, separately. Besides, such an -arrangement leads to reduced costs, eliminating the necessity of two parallel circuits.
An improved version of the circuit is shown below;
Transmitters
Field
Junction
Boxes
Marsha
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Do
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w
FT A (A/D Converter cards
0/
to final actuating device
field termination assembly
(3) Ratio Bias Controller
The existing combustion control system works perfectly, when all the burners in both the boilers are working. But if one or more burners of a boiler trips, when the boiler is in the combustion control loop, immediately, the oil flow controller, FIC2106 and the air flow controller, FIC2107, have to be taken into the manual mode. The output of FIC2106 has to be reduced to maintain higher 02 level in the flue gas. This is because, if the loop is in line, it will try to keep the same total oil flow through the remaining burners, resulting in increased oil flow in these burners, while the air flow remains the same. This would leads to decreased efficiency.
To avoid such a situation, a modification in the combination control loop is essential and the result is the 'Ratio Bias Controller'.
The proposed Ratio Bias Controller (RBC) would divide the air & fuel, equally amongst the presently working burners. This avoids over loading of some of the burners while maintaining higher efficiency, at the same time. Since RBC demands greater attention, it has been dealt separately.
IMPORTANCE OF PROJECT BASED ON ANALYSIS
Steam is mainly required for power generation, driving the turbo generator and heating installation. For the proper operation of plant an uninterruptible supply of steam is required. So a continuous operation of boiler is necessary. The continuous boiler operation provides higher efficiency by proper controlling methods. So the boiler control process is very essential to enhance the smooth start up and shut down and also provides high efficiency.
The main objective of this project is the complete automation of boiler plant based on BMS. Energy saving by proper control or selective switching enhances efficiency of plant and increase economical benefits. These are depends on many parameters included in this operation. The analysis of boiler plant operation gives a detailed study of plant operation and the present implementation. It also provides methods for future improvement. The findings from the project indicates the importance of project that are explained below.
1. Energy Saving by Selective Switching
The boiler process control can be done either manually or automatically. For the continuous operation, it requires periodic examinations of different conditions to be satisfied for switching purpose. So a person has to be appointed just for monitoring the temperature and pressure and do the switching operations. This is cumbersome duty and wastage of labour. These problems can be avoided by automated switching operation using PLC. This will account to saving of annual energy consumption and reduction in laborer.
By automatic combustion control system it is very easy to meet the requirements of steam demand. When the boiler steam demand is decreases oil demand decreases. This is done by reducing speed of the Forced Draught fan (FD fan) which is driven by turbine blades whose rotating speed is set up adjusting steam input.
It is necessary to maintain a constant steam pressure and uniform furnace draught and supply of air or fuel which can be regulated to meet the changes in steam demand. It is very efficiently done by selective switching process. So the boiler operation becomes more flexible.
The speed of fan is regulated with respect to the steam demand. The supply of air is done through FD fan which helps for complete combustion of fuel and thus avoid wastage of fuel. So the steam demand is satisfactorily meet by adjusting speed of fans (directly proportional to demand).
2. Improve Efficiency
In FACT, the boiler produced steam rate is represented as 60TPH, at 520 degree c. and 110kg. It is a high pressure boiler with high capacity. It provided higher efficiency (output/input - steam/fuel) and high steam rate, ie The high pressure and temperature steam has high heat content so less steam is required for meeting the requirement. So less fuel is needed for obtaining some efficiency, ie It provided high efficiency and leads to less wastage of energy.
Boiler efficiency depends on the following factors, air fuel ratio, soot formation and insulation. The efficiency can be increased by maintaining proper air fuel ratio. This leads to reduce excess flue gases and thus heat losses. Soot formed by boiler operation is removed by soot blowing operation which is periodically run for cleaning the internal parts of boiler. The insulation level must be satisfactorily provided for feed water system to avoid heat loss through water tubes.
The boiler efficiency can be increased by reducing heat loss.
This is done in 3 ways;
1. Absorb flue gas temperature by water tubes
2. Soot is removed by soot blowers which is periodically run by steam
3. To reduce flue gases by minimize excess air or maintain proper air/fuel ratio
The steam produced in boiler is saturated, which is not used in turbine because the dryness factor of steam leaving the boiler will be very low. This results in the presence of moisture which causes scaling of turbine blades. To raise the temperature of steam super heaters are used. It supplies steam at constant temperature at different loads. So super heated steam increase efficiency. The proper setting of arrangement of FD and ID fans improve burning of fuel and achieve higher efficiency.
3. Economic Benefits
In the existing control systems, interlocks for tripping are realized by means of electromagnetic relay based system. Its reliability is low and hard wired structures leads to high insulation or capital cost. It has some disadvantages too. Here error detection is difficult due to complexity in configuration. So maintenance cost is high and also time loss is more due to the wastage of time for repairing hardwire parts. It require more space for installation.
This is avoided by using PLC control. It provides continuous operation and avoid increased rate of energy consumption due to frequent starting and tripping. PLC are programmable according to requirement. So configuration do not affect according to demand. It give reliable and efficient operation for long life time and also provides safety requirements. This automatic control reduces the labour. Recirculation of DM water reduces running cost. By proper controlling of speed of fans and the combustion of fuel, wastage of fuel is avoided. There by expenses reduces and operation is economically beneficial.
AUTOMATION OF OPERATION OF BOILER PLANT USING PLC
Today, automation is moving rapidly towards a true point of central control that resides in the system operator's office. It is becoming increasingly necessary for the system operators to have finger tip control of the process. This has been greatly fulfilled by the use of programming device.
Programmable devices eliminate the need of complex components and the discrete components. They are also more reliable, cheaper and it can withstand harsh factory environments, perhaps the biggest advantages of programmable devices is that their functions are easily changeable by merely changing the program stored in them, there by eliminating need for replacing the whole system. Additional changes can be made incrementally. They also allow interaction with other systems and since their outputs are digital, their working can be easily monitored by computers.
In the world of automation, PLC has become a standard for control. It now not only replaces the earlier relay controls but has taken over many additional control functions. PLCs are used to synchronize the flow of inputs from sensors and events with the flow of outputs to actuators and events. This leads to precisely controlled actions that permit a tight control of the process or machine. This project is devoted to the principle upon which PLCs operate.
Until the last decade control were realized through the discrete relays. Relays, though simple, because of these discrete nature and the need for them to be hard-wired for their operation become cumbersome and unfit in cases where a lot of conditions are to be satisfied to achieve automatic control when the system requirements change, the relay wiring has to be changed or modified. In an industrial environment, such modifications are not only time consuming but tedious as well. In extreme cases, such as in auto industry, complete panels have to be replaced as it is not economically feasible to old panels with each model change over.
Bigger the process more is need for a PLC. We can simply program the PLC to count its inputs and turn the solenoids on for specified time. Used in industrial and commercial applications, PLCs act as controllers for machines and processes. They monitor inputs, make decisions and control outputs in order to automatic machines and processes. A PLC is a computer designed for using in machines. Unlike a computer, it has been designed to operate in the industrial environment and is equipped with special inputs or outputs and a control program language. Initially the PLC was used to replace relay logic, but its ever increasing range of function means that it is found in many more complex applications.
As the structure of a PLC is same as those employed in computer architecture, it is capable of performing not only relay switching tasks but also other applications such as counting, calculating, comparing and the processing of analog signals . In this project, automation of boiler process system is done using PLC. The ladder diagram technique of programming PLC has been utilized. The implementation of this system would replace existing permanent hard-wired relay system by programmable system varied according to the requirement make the system more reliable and upgraded in future.
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22. LD 0.07 Heavy oil pressure very low
23. OUT 11.00 Heavy oil pressure very low
24. LD 0.08 Heavy oil temperature very low
25. OUT 11.01 Heavy oil temperature very low
26. LD 0.09 Atomizing steam pressure very low
27. OUT 11.02 Atomizing steam pressure very low
28. LD .0.07 Heavy oil pressure very low
29. OR 0.08 . Heavy oil temp, very low
30. OR 0.09 Atomizing steam pressure very low
31. OUT 11.03 HOTV trip
32. LD 0.10 Burner 1 flame failure
33. OUT 11.04 Burner 1 trip
34. LD 0.11 Burner 2 flame failure
35. OUT 11.05 Burner 2trip
36. LD 1.00 Burner 3 flame failure
37. OUT 11.06 Burner 3 trip
38. LD 1.0.1 Burner 4 flame failure
39. OUT 11.07 Burner 4 trip
40. LD 0.10 Burner 1 flame failure
41. AND 0.11 Burner 2 flame failure
42. AND 1.00 Burner 3 flame failure
43. AND 1.01 Burner 4 flame failure

44. OUT 12.00 All flame fail
45. LD 1.02 OBTV 1 close
46. AND 1.03 OBTV 2close
47. AND 1.04 OBTV 3close
48. AND 1.05 OBTV 4 close
49. OUT 12.01 All OBTV close
50. LD 1.06 HOTV close
51. OUT 12.02 HOTV close
52. LD 1.07 IGTV close
.53. OUT 12.03 IGTV close
54. LDNOT 10.07 Boiler trip
55. AND 12.00 All flame fail
56. AND 12.01 All OBTV close
57. AND 12.02 HOTV close
58. AND 12.03 IGTV close
59. OUT 12.04 Purge Ready Permit
60. LD 1.08 Purge Start command
61. ANDNOT TIM001
62. OUT 12.05 Purge start given
63. LD 12.04 Purge Ready Permit
64. AND 12.05 Purge start given
65. TIM 001 1
66. LD TIM001
67. OUT 12.06 Purge complete
68. LD 1.09 Ignition gas pressure not low
69. OUT 12.07 Ignition gas pressure not low
70. LD 12.06 Purge complete
71. AND 12.07 Ignition gas pressure not low
72. OUT 13.00 IGTV open permit
73. LD 12.06 Purge complete
74. ANDNOT 11.03 HOTV trip
75. OUT 13.01 " HOTV open ON
76. LD 1.10 Ignition ON
77. OUT 13.02 Ignition ON
78. LD 1.11 Oil manual valve open
79. OUT 13.03 Oil manual valve open
80. LD 2.00 Scavenging valve close
8.1. OUT 13.04 Scavenging valve close
82. LDNOT 1.06 HOTV close
83. AND 12.06 Purge complete
84. AND 13.02 Ignition ON
85. AND 13.03 Oil manual valve open
86. OUT 13.05 Out 1
87. LD 13.04 Scavenging valve close
88. AND 2.01 Atomizing steam manual valve open
89.
AND
2.02
Atomizing steam pressure not low
90.
AND
13.05
Out
91.
OUT
13.06
OBTV open permit
92.
LD
2.03
OBTV open Push Button
operated
93.
AND
13.06
OBTV open permit
94.
OUT
13.07
OBTV open PB pressed
95.
LD
13.06
OBTV open permit
96.
AND
2.04
Oil gun Engaged
97.
AND
13.07
OBTV open PB pressed
98.
OUT
14.00
ATV open command
99.
LD
2.05
ATV open feedback
100.
OUT
14.01
ATV opened
101.
LD
14.00
ATV open command
102.
AND
14.01
ATV opened
103.
ANDNOT
14.03
OBTV close command
104.
OUT
14.02
OBTV open command
105.
LD
14.02
OBTV open command
106.
TIM
002 5
107.
LD
TIM002
108.
AND
0.10
Burner 1 flame failure
109.
OUT
14.03
OBTV close command
LD
1.02
OBTV 1 close
111.
OUT
14.04
OBTV 1 close

112. LD 13.02 Ignition ON
113. AND 14.04 OBTV 1 close
114. OUT 14.05 Scavenging Valve open
115. END(OOl) End
17. OUT 10.07 Suction DP very high
18. LD * 0.07 Bearing temperature very high
19. OUT 11.00 Bearing temperature very high
20. LD 0.08 Lube oil pressure very low trip
21. OUT 11.01 Lube oil pressure very low trip
22. LD 0.05 Deaerator level very low
23. OR 0.06 Suction DP very high
24. OR 0.07 Bearing temperature very high
25. OR 0.08 Lube oil pressure very low trip
26. OUT 11.02 Boiler feed pump trip
27. LD 0.09 Deaerator level low
28. OUT 11.03 Alarm
29. LD 0.10 Deaerator level high
30. OUT 11.04 Alarm
31. LD 0.1