BOILER CONTROLS &BOILER CONTROLS & INSTRUMENTATION

1 Your Logo HereBOILER CONTROLS & BOILER CONTROLS &HereBOILER CONTROLS & BOILER CONTROLS & INSTRUMENTATIONINSTRUMENTATIONPRESENTED ATPRESENTED ATPRESENTED AT PRESENTED AT M/S. MAGADI SODA COMPANY , M/S. MAGADI SODA COMPANY , MAGADI KENYAMAGADI KENYAMAGADI , KENYAMAGADI , KENYA24/06/201024/06/2010 THERMODYNE THERMODYNE TECHNOLOGIES PRIVATE TECHNOLOGIES PRIVATE LIMITEDLIMITED11 MAJOR CLOSED LOOP CONTROLS IN BOILERMAJOR CLOSED LOOP CONTROLS IN BOILER DRUM LEVEL CONTROLDRUM LEVEL CONTROL PUMP ONPUMP ON--OFF CONTROL ( USED ON OFF CONTROL ( USED ON ((PACKAGED SATURATED steam BOILERS)PACKAGED SATURATED steam BOILERS)))

2 SINGLE ELEMENT DRUM LEVEL CONTROL SINGLE ELEMENT DRUM LEVEL CONTROL ( USED IN SMALL & PACKAGE BOILERS WITH ( USED IN SMALL & PACKAGE BOILERS WITH ECONOMISERS OPERATING AT LOW ECONOMISERS OPERATING AT LOW PRESSURE)PRESSURE)PRESSURE)PRESSURE) THREE ELEMENT DRUM LEVEL CONTROL ( THREE ELEMENT DRUM LEVEL CONTROL ( USED IN HIGH PRESSURE LARGE CAPACITYUSED IN HIGH PRESSURE LARGE CAPACITYUSED IN HIGH PRESSURE LARGE CAPACITY USED IN HIGH PRESSURE LARGE CAPACITY BOILERS )BOILERS )24/06/201024/06/2010 THERMODYNE THERMODYNE TECHNOLOGIES PRIVATE TECHNOLOGIES PRIVATE LIMITEDLIMITED2224/06/201024/06/2010 THERMODYNE THERMODYNE TECHNOLOGIES PRIVATE TECHNOLOGIES PRIVATE LIMITEDLIMITED33 SINGLE ELEMENT DRUM LEVEL CONTROLSINGLE ELEMENT DRUM LEVEL CONTROL IN A SINGLE ELEMENT CONTROL , THE IN A SINGLE ELEMENT CONTROL , THE LEVEL TRANSMITTER ON THE steam LEVEL TRANSMITTER ON THE steam DRUM WILL TRANSMIT THE LEVEL DRUM WILL TRANSMIT THE LEVEL SIGNAL TO THE CONTROLLER.

3 LEVEL SIGNAL TO THE CONTROLLER. LEVEL CONTROLLER COMPARES THIS SIGNALCONTROLLER COMPARES THIS SIGNALCONTROLLER COMPARES THIS SIGNAL CONTROLLER COMPARES THIS SIGNAL WITH THE SET POINT AND SENDS AN WITH THE SET POINT AND SENDS AN OUTPUT SIGNAL TO THE FEED WATEROUTPUT SIGNAL TO THE FEED WATEROUTPUT SIGNAL TO THE FEED WATER OUTPUT SIGNAL TO THE FEED WATER CONTROL VALVE TO OPEN OR CLOSE CONTROL VALVE TO OPEN OR CLOSE TO INCREASE OR DECREASE THE FEEDTO INCREASE OR DECREASE THE FEEDTO INCREASE OR DECREASE THE FEED TO INCREASE OR DECREASE THE FEED

4 WATER FLOW TO THE FLOW TO THE THERMODYNE TECHNOLOGIES PRIVATE TECHNOLOGIES PRIVATE LIMITEDLIMITED44 SINGLE ELEMENT DRUM LEVEL CONTROLSINGLE ELEMENT DRUM LEVEL CONTROL24/06/201024/06/2010 THERMODYNE THERMODYNE TECHNOLOGIES PRIVATE TECHNOLOGIES PRIVATE LIMITEDLIMITED55 WHY THREE ELEMENT CONTROL ?WHY THREE ELEMENT CONTROL ? IN HIGH PRESSURE BOILERS , WHEN THE IN HIGH PRESSURE BOILERS , WHEN THE ,, steam DEMAND OF THE BOILER INCREASES steam DEMAND OF THE BOILER INCREASES SUDDENLY , THE WITHDRAWAL OF steam SUDDENLY.

5 THE WITHDRAWAL OF steam FROM THE steam DRUM WILL BE HIGHERFROM THE steam DRUM WILL BE HIGHERFROM THE steam DRUM WILL BE HIGHER FROM THE steam DRUM WILL BE HIGHER THAN THE steam GENERATION AS THAN THE steam GENERATION AS COMBUSTION CONTROL WILL TAKE SOME COMBUSTION CONTROL WILL TAKE SOME TIME TO REACT AND INCREASE THE FUEL TIME TO REACT AND INCREASE THE FUEL HEAT INPUT TO THE WILL HEAT INPUT TO THE WILL RESULT IN DRUM PRESSURE FALLINGRESULT IN DRUM PRESSURE FALLINGRESULT IN DRUM PRESSURE FALLING RESULT IN DRUM PRESSURE FALLING TEMPORARILY.

6 THIS LOSS OF PRESSURE TEMPORARILY. THIS LOSS OF PRESSURE WILL RESULT IN THE FORMATION OF steam WILL RESULT IN THE FORMATION OF steam BUBBLES IN THE DRUM WATER DUE TO THE BUBBLES IN THE DRUM WATER DUE TO THE ENTHAPHY DIFFERENCE BETWEEN THE TWO ENTHAPHY DIFFERENCE BETWEEN THE TWO PRESSURE LEVELSPRESSURE LEVELS24/06/201024/06/2010 THERMODYNE THERMODYNE TECHNOLOGIES PRIVATE TECHNOLOGIES PRIVATE LIMITEDLIMITED66 PRESSURE THREE ELEMENT CONTROL ?WHY THREE ELEMENT CONTROL ?CONTINUEDCONTINUED THIS BUBBLING IN THE DRUM WATER WILL THIS BUBBLING IN THE DRUM WATER WILL RESULT IN THE FOAMING AND INCREASE IN RESULT IN THE FOAMING AND INCREASE IN THE VOLUME LEADING TO THE LEVEL GOINGTHE VOLUME LEADING TO THE LEVEL GOINGTHE VOLUME LEADING TO THE LEVEL GOING THE VOLUME LEADING TO THE LEVEL GOING UP SPURIOUSLY.

7 THE LEVEL TRANSMITTER UP SPURIOUSLY. THE LEVEL TRANSMITTER WILL TRANSMIT THIS INCREASE IN DRUMWILL TRANSMIT THIS INCREASE IN DRUMWILL TRANSMIT THIS INCREASE IN DRUM WILL TRANSMIT THIS INCREASE IN DRUM LEVEL TO THE CONTROLLER LEADING TO LEVEL TO THE CONTROLLER LEADING TO REDUCTION IN FEED WATER FLOW INSTEAD REDUCTION IN FEED WATER FLOW INSTEAD OF INCREASING THE FEED WATER FLOW OF INCREASING THE FEED WATER FLOW DUE TO HIGHER DEAMND ON BOILER . TO DUE TO HIGHER DEAMND ON BOILER . TO AVOID SUCH A WRONG CONTROL 3 ELEMENTAVOID SUCH A WRONG CONTROL 3 ELEMENTAVOID SUCH A WRONG CONTROL 3 ELEMENT AVOID SUCH A WRONG CONTROL 3 ELEMENT DRUM LEVEL CONTROL IS REQUIREDDRUM LEVEL CONTROL IS REQUIRED24/06/201024/06/2010 THERMODYNE THERMODYNE TECHNOLOGIES PRIVATE TECHNOLOGIES PRIVATE LIMITEDLIMITED77 THREE ELEMENT DRUM LEVEL CONTROLTHREE ELEMENT DRUM LEVEL CONTROL IN THIS THE DRUM LEVEL CONTROLLER IN IN THIS THE DRUM LEVEL CONTROLLER IN ADDITION TO RECEIVING THE DRUM LEVEL ADDITION TO RECEIVING THE

8 DRUM LEVEL SIGNAL WILL ALSO RECEIVE THE STEAMSIGNAL WILL ALSO RECEIVE THE STEAMSIGNAL , WILL ALSO RECEIVE THE steam SIGNAL , WILL ALSO RECEIVE THE steam FLOW AND FEED WATER FLOW FLOW AND FEED WATER FLOW TRANSMITTER SIGNALS. HENCE WHENEVER TRANSMITTER SIGNALS. HENCE WHENEVER THERE IS A DIFFERENCE BETWEEN THETHERE IS A DIFFERENCE BETWEEN THETHERE IS A DIFFERENCE BETWEEN THE THERE IS A DIFFERENCE BETWEEN THE steam AND WATER FLOW , THE steam AND WATER FLOW , THE CONTROLLER WILL APPLY SUITABLECONTROLLER WILL APPLY SUITABLECONTROLLER WILL APPLY SUITABLE CONTROLLER WILL APPLY SUITABLE CORRECTION TO ITS OUTPUT SIGNAL TO THE CORRECTION TO ITS OUTPUT SIGNAL TO THE FEED CONTROL VALVE.

9 THIS TYPE OF FEED CONTROL VALVE. THIS TYPE OF CONTROL WILL KEEP THE DRUM LEVELCONTROL WILL KEEP THE DRUM LEVELCONTROL WILL KEEP THE DRUM LEVEL CONTROL WILL KEEP THE DRUM LEVEL CONTROL TO FUNCTION CORRECTLY EVEN CONTROL TO FUNCTION CORRECTLY EVEN WHEN THE BOILER LOAD CHANGESWHEN THE BOILER LOAD CHANGES24/06/201024/06/2010 THERMODYNE THERMODYNE TECHNOLOGIES PRIVATE TECHNOLOGIES PRIVATE LIMITEDLIMITED88 OOCGSOOCGS24/06/201024/06/2010 THERMODYNE THERMODYNE TECHNOLOGIES PRIVATE TECHNOLOGIES PRIVATE LIMITEDLIMITED99 FLOW COMPENSATIONSFLOW

10 COMPENSATIONS IN CASE OF FLOW MEASUREMENTS FOR IN CASE OF FLOW MEASUREMENTS FOR COSSS ( SG S )COSSS ( SG S )COMPRESSIBLE FLUIDS ( steam , GAS ) , THE COMPRESSIBLE FLUIDS ( steam , GAS ) , THE DENSITY WILL CHANGE DUE TO CHANGE IN DENSITY WILL CHANGE DUE TO CHANGE IN PRESSURE AND TEMPERATURE OF THE PRESSURE AND TEMPERATURE OF THE MEDIUM. IN SUCH CASES BOTH THE PRESSURE MEDIUM. IN SUCH CASES BOTH THE PRESSURE AND TEMPERATURE OF THE FLUID ALSO SHALL AND TEMPERATURE OF THE FLUID ALSO SHALL BE MEASURED TO APPLY THE DENSITYBE MEASURED TO APPLY THE DENSITYBE MEASURED TO APPLY THE DENSITY BE MEASURED TO APPLY THE DENSITY CORRECTION FOR THE FLOW MEASUREMENTS.