fcc trouble shooting trg by spalit
TRANSCRIPT
FCC FUNDAMENTALS : OPERATIONS
& TROUBLESHOOTING
PRESENTED BY : S PALIT (DMPN)
CONCERNS IN FCC
•CATALYST LOSS
•COKING / FOULING
• FLOW REVERSAL
•CATALYST CIRCULATION
•HIGH REGEN TEMPERATURE
•AFTER BURNING
•AMOUNT & QUALITY OF PRODUCTS.
MAJOR PROBLEM
AREAS
CATALYST LOSS
CATALYST LOSS SYMPTOMS
MECHANICAL CONDITION
CHANGES IN
OPERATING CONDITION
CATALYST PROPERTIES
CAUSES OF CATALYST LOSS
MECHANICAL CAUSES
TRICKLE VALVES ARE STUCK CLOSE OR OPEN
DEFORMATION OF TRICKLE VALVE
FLAPPER OR TRICKLE VALVES DISENGAGED
TRICKLE VALVE & SPLASH PLATE
MECHANICAL CAUSES (CONTD)
SPALLED COKE OR REFRACTORY IN DIP LEG CAUSING RESTRICTION
HOLES ON CYCLONES
CRACKS ON PLENUM CHAMBER
DETACHED DIPLEG
A TYPICAL CYCLONE
MECHANICAL CAUSES (CONTD)
IMPROPER STEAM / AIR RESTRICTION ORIFICES ON PURGES CAN LEAD TO CATALYST ATTRITION, THEREBY GENERATING FINES
CATALYST LOSS DUE TO OPERATIONS
INCREASE IN
CATALYST
CIRCULATION
INCREASE IN
STEAM TO
REACTOR
AIR TO
REGENERATOR
LOWERING OF
OPERATING
PRESSURE
INCREASE OF CATALYST
LOADING TO CYCLONES
CATALYST LOSS DUT TO CATALYST
TROUBLESHOOTING
TROUBLESHOOTING
OPERATIONAL
VERIFY THE CATALYST LEVELS
IN REACTOR AND REGENERATOR
CHECK THE CYCLONE VELOCITIES
AND COMPARE WITH THE DESIGN
REDUCE CAT-OIL RATIO
CHECK PURGE POINT ROV
COKING / FOULING PROBLEM
FREQUENT CAVITATION AND LOSS OF SUCTION OF
BOTTOM PUMP
INCREASED
PRESSURE DROP
IN MCB
EXCHANGERS
HIGH PRESSURE
DROP ACROSS Rx
VAPOUR LINE
POOR HEAT TRANSFER IN
MCB PUMPAROUND
CIRCUIT
REASONS FOR COKING / FOULING
CATALYST PROPERTIES RESPONSIBLE
FOR COKING
OPERATIONAL CONDITIONS
RESPONSIBLE FOR COKING
HIGH MCB
LEVEL
LONG
RESIDENCE
TIME
LOW WASH
LIQUID FLOW
LOW ROT
LONG RESIDENCE
TIME IN VAPOUR
LINE
FEED PROPERTIES LEADING TO
COKING
ASPHALTENES AND RESID IF
NOT CONVERTED IN RISER,
LEADS TO COKING
MECHANICAL CONDITIONS LEADING
TO COKING
TROUBLE SHOOTING
TROUBLESHOOTING
IMPROVE FEED ATOMISATION
INTRODUCE FEED WHEN REACTOR IS ADEQAUTELY HEATED DURING UNIT START UP
KEEP THE VELOCITY IN MCB EXCHANGER > 2.1 m/s
TROUBLESHOOTING
MAINTAIN MCB TEMP < 360 deg C
MAINTAIN 1ST TRAY IN THE BOTTOM TEMP < 420°C BY PROVIDE ADEQUATE WASHING LIQUID TO MCB
MAINTAIN HIGH REACTOR TEMPERATURE IF POSSIBLE
FLOW REVERSAL
REGENERATOR
REACTOR
REGENERATOR
NORMAL CATALYST FLOW PATH
PROPER PRESSURE
BALANCE ACROSS
REACTOR AND
REGENERATOR
AIDS CATALYST
MOVEMENT
FLOW REVERSAL
PHENOMENON OF FLOW REVERSAL
THE HOT FLUE GAS FLOW TO
REACTOR AND TO COLUMN IF THE
PRESSURE DIFFERENTIAL ACROSS SPENT
CATALYST SLIDE VALVE BECOMES
NEGATIVE
OIL SOAKED CATALYST TO FLOW
REVERSE FROM RISER TO
REGENERATOR IN CASE THE
DIFFERENTIAL PRESSURE ACROSS
REGENERATED CATALYST SLIDE VALVE BECOMES
NEGATIVE
CAUSES OF FLOW REVERSALS
MAB TRIPPING
PRESENCE OF WATER IN FEED
HIGH OPENING OF SLIDE VALVES
SUDDEN LOSS OF REACTOR / REGENERATOR LEVELS
FAILURE OF REACTOR TEMP / LEVEL CONTROL
PROTECTION FROM FLOW REVERSAL
• INDEPENDENT LOW DIFFERNTIAL PRESSURE OVERRIDE CONTROL FOR SLIDE VALVES
• CHECKING OF FEED TANK HEATING COIL OUTLET AND REGULAR DRAINING OF FEED SURGE DRUM
• EMERGENCY SHUT DOWN
HIGH REGENERATOR TEMPERATUR
HIGH REGENERATOR TEMPERATURE
HIGH REGENERATOR TEMPERATURE
HIGH REGENERATOR TEMPERATURE
HIGH REGENERATOR TEMPERATURE
HIGH REGENERATOR TEMPERATURE
RAISE CAT / OIL RATIO
IMPROVE FEED ATOMISATION
IMPROVE STRIPPING IN
REACTOR
USE METAL PASSIVATOR
REMEDIES
AFTER BURNING
CAUSES OF AFTER BURN
POOR AIR / CATALYST
DISTRIBUTION
LIFT LINE WITH AIR RING AIR
DISTRIBUTION PROBLEM
CAUSES OF AFTER BURN
LIFT LINE WITH AIR RING CAT
DISTRIBUTION PROBLEM
CHANNELING OF CATALYST
IN CURVED LIFT LINE
CAUSES OF AFTER BURN
REGEN INTERNALS CREATE
TWO STAGE REGENERATION
CATALYST ENTERS ONE SIDE
OF REGENERATOR
CAUSES OF AFTER BURN
EFFECT OF HIGH DENSITY CATALYST ON
AIR DISTRIBUTION
REASONS OF AFTERBURNS
OPERATING CAUSES
EXCESS AIR
LOW CATALYST
RESIDENCE TIME
MECHANICAL
CAUSES
DAMAGED AIR RING
DAMAGED CATALYST
DISTRIBUTOR
AFTER BURN REMEDIES
INCREASE STRIPPING STEAM RATE.
INCREASE THE CATALYST RESIDENCE TIME : RAISE THE REGENERATOR CATALYST BED LEVEL.
REDUCE FEED CCR
INCREASE CAT / OIL BY QUENCHING
CATALYST CIRCULATION
THE LIMITATION IN CATALYST CIRCULATION
WILL LIMIT THE T’PUT OF THE UNIT.
EXTREME HIGH CAT CIRCULATION PROBLEM
WILL LEAD TO UNIT SHUTDOWN
CATALYST CIRCULATION PROBLEM
SYMPTOM:
SLIDE VALVE FAR TOO OPEN
EVIDNECE:
SLIDE VALVE OPENING INDICATIONS
CAUSES:
GATE OR ORIFICE TOO SMALL FOR FLOW
SOLUTIONS:
REPLACE WITH APPROPRIATE SIZE VALVE
INCREASE REGEN PRESSURE / BED LEVEL
CATALYST CIRCULATION PROBLEM
REASONS:
SYMPTOM: LOW DELTA P ACROSS SLIDE
VALVE
HIGH PRESSURE D/S
OF SLIDE VALVE
LOW PRESSURE U/S
OF SLIDE VALVE
WHEN HIGH PRESSURE D/S
HIGH DP ACROSS RISER
HIGH CAT CIRCULATION
LESS RISER GAS AT RISER
BASE
HIGH DP ACROSS VAP
LINE
VAP LINE COKING
HIGH RXR VAP LOAD
REASONS
CAUSES
WHEN HIGH PRESSURE D/S
HIGH DP ACROSS MF
HIGH VAP / LIQ RATES
PLUGGED TRAYS
HIGH DP ACROSS MF
O/H CIRCUIT
CONDENSER FOULING
HIGHER RATES OF
LIGHTER HC
REASONS
CAUSES
WHEN HIGH PRESSURE D/S
HIGH DP ACROSS
RISER
REPLACE RISER BEND
INCREASE RISER STEAM
HIGH DP ACROSS VAP
LINE
COKING REDUCTION
VAP LINE CLEANING
DURING S/D
PROBLEMS
SOLUTIONS
WHEN HIGH PRESSURE D/S
HIGH DP ACROSS MF
ADJUST PUMP AROUND RATES
ADD TOP OR SIDE PUMP AROUNDS
HIGH DP ACROSS MF O/H
CIRCUIT
CONDENSER CLEANING
INCREASE WATER WASH
TO CONDENSERS
PROBLEMS
SOLUTIONS
WHEN LOW PRESSURE U/S
INSUFFICIENT PRESSURE BUILD
UP IN STAND PIPE
DEFLUIDIZATION IN STAND PIPE
DE-AERATION IN STAND PIPE
LOW CATALYST DENSITY IN STAND PIPE
IMPROPER PLACEMENT OF AERATION TAPS
PLUGGED RO
REASONS
CAUSES
WHEN LOW PRESSURE U/S
DEFLUIDIZATION IN STAND PIPE
CHECK CATALYST PROPERTIES
DE-AERATION IN STAND PIPE
INCREASE AERATION GAS
FLOW TO MAXIMIZE PRESSURE BUILD UP
IMPROPER PLACEMENT OF AERATION TAPS
PLUGGED RO
FLUSH RO
SOLUTIONS
PROBLEMS
LOSS IN PRODUCTS –
PROBLEM INDICATORS
CONVERSION
DRY GAS YIELD
GASOLINE YIELD
PROBLEM AREAS
FEED QUALITY
CATALYST QUALITY
OPERATING CONDITION
MECHANICAL DEFECT
LOW CONVERSION
FEED QUALITY
INCREASE IN METALS
CONTENTS
HIGH FBP FEED
INCREASE IN FEED
AROMATICITY / NAPHTHENECITY
CATALYST PROPERTIES
LOW CATALYST ACTIVITY
LOW SURFACE AREA
HIGH CRC
LOW CONVERSION
OPERATING CONDITIONS
LOW CAT / OIL RATIO
LOW ROT
LOWER RATE OF FEED
ATOMIZING STEAM
LOW F-CAT ADDITION
RATE
MECHANICAL CONDITIONS
PROBLEM IN FEED NOZZLE
PROBLEMS IN REGEN
INTERNALS
TROUBLESHOOTING
CHECK FEED STOCK PROPERTIES
K-FACTORS, ANILINE POINT, SP. GR
CHECK E-CAT PROPERTIES
VERIFY ACCURACY OF INSTRUMENT INDICATIONS
OF RR SECTION
CARRY OUT PRESSURE SURVEY OF FEED NOZZLES,
AIR RINGS, ETC
HIGH DRY GAS YIELD
FEED QUALITY
INCREASE IN METALS
CONTENTS
INCREASE IN FEED
AROMATICITY / NAPHTHENECITY
CATALYST PROPERTIES
LOW CATALYST ACTIVITY
LOW SURFACE AREA
HIGH CRC
HIGH DRY GAS YIELD
OPERATING CONDITIONS
HIGH ROT
LOWER RATE OF FEED
ATOMIZING STEAM
INCREASE IN RECYCLES
MECHANICAL CONDITIONS
PROBLEM IN FEED NOZZLE
PROBLEMS IN REGEN
INTERNALS
DECREASE IN GASOLINE YIELD
FEED QUALITY
HIGH FBP FEED
INCREASE IN FEED
AROMATICITY / NAPHTHENECITY
CATALYST PROPERTIES
LOW RARE EARTH CONTENT
LOW ZEOLITE CONTENT
LOW UNIT CELL SIZE
DECREASE IN GASOLINE YIELD
OPERATING CONDITIONS
LOW / HIGH ROT
DECREASE CAT / OIL
RATIO
HIGH DOSING
OF ZSM -5
MECHANICAL CONDITIONS
PROBLEM IN FEED NOZZLE
PROBLEMS IN REGEN
INTERNALS