Created by Ankur Sharma,
Created by Ankur Sharma, Gurudayal Srivastava, Vikram Singh, Sanket Gurudayal Srivastava, Vikram Singh, Sanket TaTamhanemhane 1. WHAT ARE CENTRIFUGES?
1. WHAT ARE CENTRIFUGES?
•
• THESE ARE THESE ARE THE DEVICES THE DEVICES USED FOR SEUSED FOR SEPPARAARATING IMPURITIES FRTING IMPURITIES FROM FUEL OIL & LOM FUEL OIL & LUBE OILUBE OIL •
• IMPURITIES CAN BE SOLID (ASH,IMPURITIES CAN BE SOLID (ASH,METMETAL PARAL PARTICLE ETC) OR TICLE ETC) OR LIQUID (CHEMILIQUID (CHEMICALS & WCALS & WAATER)TER)
2. WHAT IS THE PRINCIPLE ON WHICH PURIFIER WORKS? 2. WHAT IS THE PRINCIPLE ON WHICH PURIFIER WORKS?
•
• WHEN BOWL/TANK IS ROTATED, CENTRIFUGAL FORCE WILL THROW ANY PARTICLE WITHWHEN BOWL/TANK IS ROTATED, CENTRIFUGAL FORCE WILL THROW ANY PARTICLE WITH
DENSITY GREATER THAN THE OIL TO THE PERIPHERY OF BOWL. DENSITY GREATER THAN THE OIL TO THE PERIPHERY OF BOWL.
•
• FORCE OF SEPFORCE OF SEPARAARATION CAN BE GIVEN BTION CAN BE GIVEN BY THE STOKE’S FORMULY THE STOKE’S FORMULA A I.E.,I.E., •
• F F !/" # !/" # D$ ( D$ ( % ' % ' % ) % ) * ++++++++++++()* ++++++++++++()
WHERE D DIAMETER OF IMPURITY PARTICLE/OIL GLOBULE WHERE D DIAMETER OF IMPURITY PARTICLE/OIL GLOBULE ( % ' % ) DENSITY DIFFERENCE BETWEEN WATER & OIL. ( % ' % ) DENSITY DIFFERENCE BETWEEN WATER & OIL. W ANGULAR VELOCITY OF THE DISC.
W ANGULAR VELOCITY OF THE DISC.
R EFFECTIVE RADIUS/ DISTANCE OF IMPURITY PARTICLE FROM BOWL CENTRE. FOR THIS R EFFECTIVE RADIUS/ DISTANCE OF IMPURITY PARTICLE FROM BOWL CENTRE. FOR THIS DIAMETER OF BOWL TO BE INCREASED. BUT THERE IS LIMITATION BECAUSE OF
DIAMETER OF BOWL TO BE INCREASED. BUT THERE IS LIMITATION BECAUSE OF BALANCING PROBLEM.
BALANCING PROBLEM. 3. WHAT IS I
3. WHAT IS INTERFNTERFACE?ACE?
•
• WHEN SEPARATION STARTS BY CENTRIFUGAL FORCE, IT FORMS THREE ONES I.E.WHEN SEPARATION STARTS BY CENTRIFUGAL FORCE, IT FORMS THREE ONES I.E.
-. HEAVIER LIQUID/PARTICLE PHASE NEAR PERIPHERY OF BOWL -. HEAVIER LIQUID/PARTICLE PHASE NEAR PERIPHERY OF BOWL . LIGHT LIQUID/CLEAN OIL PHASE
. LIGHT LIQUID/CLEAN OIL PHASE NEAR CENTER OF THE BOWL. &NEAR CENTER OF THE BOWL. &
$. MIDDLE NEUTRAL PHASE .THIS GRADUALLY BECOMES LESS & EVENTUALLY FORMS THIN $. MIDDLE NEUTRAL PHASE .THIS GRADUALLY BECOMES LESS & EVENTUALLY FORMS THIN DIVIDING LINE BETWEEN THE TWO ONES .THIS DIVIDING LAYER IS CALLED INTERFACE OR DIVIDING LINE BETWEEN THE TWO ONES .THIS DIVIDING LAYER IS CALLED INTERFACE OR E+LINE.
E+LINE.
•
• THE POSITION OF I THE POSITION OF INTERFNTERFACE DECIDACE DECIDES THE DEGREES THE DEGREE OF PURIFICE OF PURIFICAATIONTION •
• THE OPTIMUM POSI THE OPTIMUM POSITION OF INTERFTION OF INTERFACE IS BETACE IS BETWEEN EDGE WEEN EDGE OF DISC STOF DISC STACK & THE OUACK & THE OUT SIDET SIDE
EDGE OF THE TOP DISC. EDGE OF THE TOP DISC.
•
• POSITION OF INTERFACE CAN BE FI#ED BY USING CORRECT SIE OF GRAVITY DISC.POSITION OF INTERFACE CAN BE FI#ED BY USING CORRECT SIE OF GRAVITY DISC.
4. WHAT IS GRAVITY DISC? 4. WHAT IS GRAVITY DISC?
•
• GRAVITY DISC IS A RING FITTED AT THE TOP OF DISC STACK FROM WHERE WATERGRAVITY DISC IS A RING FITTED AT THE TOP OF DISC STACK FROM WHERE WATER
(HEAVIER PHASE) IS PASSING OUT. (HEAVIER PHASE) IS PASSING OUT.
•
• OUTSIDE DIAMETER OF GRAVITY DISC IS FI#ED & INSIDE DIAMETER CAN VARY DEPENDINGOUTSIDE DIAMETER OF GRAVITY DISC IS FI#ED & INSIDE DIAMETER CAN VARY DEPENDING
UPON SPECIFIC GRAVITY OF THE OIL TO BE PURIFIED. FOR THIS PURPOSE DIFFERENT SETS UPON SPECIFIC GRAVITY OF THE OIL TO BE PURIFIED. FOR THIS PURPOSE DIFFERENT SETS OF GRAVITY DISCS ARE SUPPLIED WITH EVERY CENTRIFUGE.
OF GRAVITY DISCS ARE SUPPLIED WITH EVERY CENTRIFUGE.
•
A) VISCOSITY OF THE OIL. B) SPECIFIC GRAVITY OF THE OIL. C) TEMPERATURE OF THE OIL. D) TEMPERATURE OF WATER. 5. METHODS TO SELECT CORRECT SIZE OF GRAVITY DISC?
-. USING THE MONOGRAMS GIVEN IN MANUAL WHICH IS BASED ON OIL DENSITY & SEPARATING TEMP.
. BY USING THE FORMULA. $. BY TRIAL & ERROR METHOD.
6. WHAT IS TRIAL ERROR METHOD?
• IF THE GRAVITY DISC (INSIDE DIAMETER) IS CORRECT SIE , INTERFACE WILL BE FORMED
BETWEEN EDGE OF DISC STACK & OUTSIDE EDGE OF THE TOP MOST DISC . WITH THIS CLEAN OIL OUTLET IS CLEAR OF WATER & WATER DISCHARGE IS CLEAR OF OIL .
• IF INSIDE DIAMETER IS TOO LARGE, THE INTERFACE WILL BE FORMED OUTSIDE THE TOP
DISC EDGE. CLEAN OIL WILL PASS TO THE WASTE THROUGH WATER OUTLET & CLEAN OIL OUTLET WILL BE CLEAR OF WATER.
• IF INSIDE DIAMETER IS TOO SMALL, THE INTERFACE WILL BE FORMED WITHIN THE DISC
STACK & SEPARATING EFFICIENCY WILL REDUCE. WITH THIS CLEAN OIL WILL CONTAIN WATER & THE WATER DISCHARGE WILL BE CLEAR OF OIL.
!. HOW ARE THE FOLLOWING FACTORS AFFECT INTERFACE?
#. WHAT IS THE DIFFERENCE $ETWEEN PURIFIER AND CLARIFIER? PURIFIER
• THE LOWER DISC HAS HOLES
• SEPARATES WATER & HEAVY SOLID IMPURITIES • TWO OUTLETS ON TOP, EACH FOR WATER & OIL • TOP DISC WITH NECK.
• GRAVITY DISC ON TOP OF DISC STACK.
• REQUIRE SEALING WATER WHILE STARTING.
• PROVIDED WITH AUTOMATIC CLEANING ARRANGING.
CLARIFIER
• THE LOWER DISC HAS NO HOLES. • SEPARATES ONLY FINER PARTICLES. • THERE IS ONLY ONE OUTLET ON TOP. • DISC WITHOUT NECK
• CLARIFIER DISC WITH SMALLER NECK • DOES REQUIRE SEALING WATER.
• TO BE CLEANED MANUALLY
1%. WHAT IS MANUAL CLEANING AND SELF CLEANING? MANUAL CLEANING
• IN THIS TO CLEAN THE BOWL AND DISC, THE BOWL PART IS TO BE DISMANTLED, AND THE
DISCS ARE TO BE TAKEN OUT.
• THESE ARE TO BE CLEANED WITH DIESEL OIL AND PLAIN CLOTH. THE BOWL IS ALSO TO BE
CLEANED IN A SIMILAR FASHION.
• IN CASE PARTS OF THE BOWL IS CLEANED THOROUGHLY AND THE OTHER PARTS CLEANED
POORLY, CAUSE UNBALANCE OF THE BOWL WHICH FURTHER RESULT IN VIBRATION AND DAMAGE TO THE BEARING.
• ALSO IMPROPER CLEANING RESULTS IN PLUGGING IN SOME PARTS WITH SLUDGE WHICH
FURTHER AFFECTS THE PERFORMANCE OF THE BOWL OPERATIONS. SELF CLEANING
• A SELF CLEANING CENTRIFUGE DOES NOT REQUIRE DISMANTLING. • WATER WASH IS GIVEN DURING RUNNING PERIOD ONLY.
• FOR THIS THE BOWL IS CONSTRUCTED WITH A CONICAL SURFACE AND HYDRAULICALLY
OPERATED OPENING AND CLOSING VALVE MECHANISM.
• THE SLUDGE DISCHARGE TAKES PLACE THROUGH A NUMBER OF SLOTS IN THE BOWL
WALL. DURING NORMAL RUNNING CONDITIONS THESE SLOTS ARE CLOSED BY THE SLIDING BOWL.
• FOR THIS, SLIDING BOWL IS FORCED UPWARDS AGAINST A SEAL RING BY THE PRESSURE
OF THE OPERATING LIQUID CONTAINED IN THE SPACE BELOW IT.
• THIS OPERATING LIQUID OUTER BALANCES THE DOWNWARD PRESSURE FROM THE
PROCESS LIQUID INSIDE THE BOWL.
11. WHAT ARE THE REASONS FOR PURIFIER OVERFLOWING?
-. WRONG SELECTION OF GRAVITY DISC, GRAVITY DISC OF BIGGER SIE. . TOO MUCH RATE OF THROUGHPUT
$. TOO LOW FUEL OIL TEMP
. TOO MUCH SLUDGE INSIDE THE BOWL . LOW SPEED OF BOWL ROTATION
". OIL IS E#CESSIVELY HEATED UP. 0. SEALING RING OF BOWL IS LEAKING 1. OPERATING WATER FAILURE
2. BOWL HAS NOT CLOSED PROPERLY -3.OIL PAIRING DISC ARE WORN OUT
--.OPERATING WATER FLOW IS NOT PROPER
-.HEIGHT OF BOWL IS NOT PROPERLY AD4USTED -$.CLUTCH PADS ARE WORN OUT OR SLIPPING
12. WHAT ARE THE REASONS FOR WATER CARRIED AWAY WITH OIL? -. GRAVITY DISC IS SMALLER.
. INTERFACE WILL SHIFT INWARD $. FEED RATE IS TOO HIGH
. BOWL DISC IS DIRTY
. THROUGHPUT IS TOO HIGH
13. WHAT ARE THE REASONS FOR E&CESSIVE VI$RATION? -. S56789 : ;6<= . F6>7?:@> 7?;9* & *@>8 ?@56*9 $. B9?*@>8 ?@56*9 . W*> 89?* . U>99> 9?* *@<:@>?5 <56:<= ". M:* 997 : =@8= * : 5 0. H9@8=: ?76:;9>: @ >: *9* 1. S=?: @ 9>7 2. F6>7?:@> 5: ?*9 59
14. WHAT ARE THE REASONS IF PURIFIER IS NOT DESLUDGING? -. DOWN BELOW PAIRING DISC AND WATER HOLES ARE CHOCKED. . SLIDING BOWL IS SEIED
$. DESLUDGING WATER PRESSURE IS NOT SUFFICIENT MAY BE FILTER IS CHOCKED OR SOLENOID VALVE IS NOT OPERATING.
15. WHAT ARE THE REASONS IF $OWL IS NOT GETTING CLOSED? -. OPERATING WATER LINE PRESSURE IS NOT BUILT UP.
. SEALING RING IS LEAKING
16. WHAT ARE THE REASONS WHY HAVN'T GET ENOUGH RPM WHEN PURIFIER IS RUNNING?
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1#. HOW TO CHANGE PURIFIER FROM H.O TO D.O.?
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2%. HOW TO CANGE PURIFIER TO CLARIFIER?
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B5?> :=9 9?5@>8 ?:9* @>59: 5@>9. 21. WHAT IS PAIRING DISC?
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22. WHY MULTIDISC PROVIDED?
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23. WHAT ARE ALL TRIPS ALARMS ARE PRESENT IN PURIFIER?
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24. WHAT IS DRIVE OF PURIFIER?
• THE DRIVE FOR THE CENTRIFUGE IS TAKEN FROM A STANDARD CONSTANT SPEED
HORIONTAL SHAFT TYPE ELECTRIC MOTOR RUNNING AT -3+-03 RPM WITH AC SUPPLY OF "3 CYCLE. WITH WORM WHEEL BOWL REVOLVES AT A SPEED OF ABOUT "333 RPM.
• NORMALLY CENTRIFUGAL FRICTION TYPE COUPLING IS USED TO CONNECT THE MOTOR
AND THE PURIFIER CROSS SHAFT WHICH HOUSES THE WORM WHEEL ON IT WITH INBUILT WORM.
• THE MATERIAL USED FOR WORM IS HARDENED STEEL WHERE AS THAT FOR WORM WHEEL
IS PHOSPHOR BRONE.
• THE SPINDLE UNIT WHICH IS VERTICAL IS FITTED WITH BALL BEARINGS AND SLEEVE. THE
TOP PART OF THE SPINDLE CARRIES BOWL AND THE LOWER IS FITTED WITH CYLINDRICAL WORM (REMOVABLE).
• THE SPINDLE IS DRIVEN THROUGH THIS CYLINDRICAL WORM WHICH ITS DRIVE FROM THE
WORM WHEEL. THE WHOLE OF THIS ASSEMBLY IS TOTALLY ENCLOSED IN AN OIL BATH AND LUBRICATION IS THEREFORE AUTOMATIC.
25. WHAT IS AN ALCAP SYSTEM?
THE BASIC ALCAP CLEANING SYSTEM COMPRISES AN FOP# SEPARATOR
A WATER TRANSDUCER WT 33, AN EPC+33 CONTROL UNIT, AND A WATER DRAIN VALVE.
AN OIL FEED PUMP, A STRAINER, AND OIL HEATING SYSTEM ARE SUPPLEMENTARY EQUIPMENT TO THE BASIC CONCEPT.
WORKING*
Changes in refinery techniques are resulting in heavy fuel oils with increased density and usually
contaminated with catalytic fines. These are small particles of the catalysts used in the refining process. They are extremely abrasive and must be removed from the fuel before it enters the engine. The generally accepted maximum density limit for purifier operation is 991 kg/m at 1!"C.
#n the $%C$& separation system the separator has no gravity disc and operates' to some extent' as a clarifier. Clean oil is discharged from the oil outlet and separated sludge and water collect at the periphery of the bowl. (hen the separated water reaches the disc stack' some water will escape with the cleaned oil. The increase in water content is sensed by a water)detecting transducer in the outlet .
The water transducer signal is fed to the *$+,T 1 microprocessor which will discharge the water when a predetermined level is reached which is -. above the reference value. The water will be discharged from sludge ports in the bowl or' if the amount is large' from a water drain valve.
#t can be used for oil whose specific gravity is more than 1.
CONSTANT OPTIMUM SEPARATION EFFICIENCY IS MAINTAINED SINCE SEPARATED WATER DOES NOT ENTER THE DISC STACK.
• SIMPLE OPERATION NO AD4USTMENTS OF THE CLEANING PLANT ARE REQUIRED DUE TO
FLUCTUATIONS IN DENSITY, VISCOSITY, FLOW RATE AND TEMPERATURE.
• SINGLE STAGE OPERATION: ONE ALCAP CLEANING SYSTEM REPLACES ONE PURIFIER/ONE
CLARIFIER IN SERIES.
• VIRTUALLY NO OIL LOSSES.
• WIDE OPERATING RANGE AS ANY FUEL OIL WITH DENSITY UP TO -3-3 KG/M$/-C CAN
BE EFFICIENTLY CLEANED WITH RESPECT TO WATER AND SOLID PARTICLES. SEPARATION EFFICIENCY IS NOT AFFECTED EVEN WHEN CLEANING FUEL OILS WITH A HIGH WATER CONTENT.
SOME POINTS TO REMEM$ER
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