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WELCOMEWELCOME TO TO
THE PRESENTATIONTHE PRESENTATION ONON
MILLING SYSTEMMILLING SYSTEM
NTPC - SIMHADRINTPC - SIMHADRI
MILLING PLANT SPECIFICATIONMILLING PLANT SPECIFICATION• TYPE OF MILL XRP 1003 (MPSP)• NO OF MILLS PER BOILER 9• NO OF MILLS REQUIRE FOR 6
FULL LOAD• MILL CAPACITY 66.2 TPH• PF FINENESS 70% THROUGH -200
MESH• MILL SPEED 42 RPM• MILL MOTOR RATING 525 KW, 3.3 KV, 589
RPM • MILL INLET AIR TEMP 230 °C• PA FANS (COMMON) 2 NOS• SEAL AIR FANS (COMMON) 2 NOS
COAL CHARACTERISTICS
• GCV 3450 – 3600 KCAL/KG
• ASH > 40 %
• VM 20 – 24 %
• CARBON 20 – 33 %
• MOISTURE 12 – 16 %
• HGI 55
CONSTRUCTION & DESIGN FEATURESCONSTRUCTION & DESIGN FEATURES• SIMHADRI IS THE FIRST COASTAL BASED COAL FIRED
THERMAL POWER PROJECT OF NTPC
• BHEL HAS PROVIDED MILLS WITH MPSP (MILL PLANT SUPER PERFORMANCE) SYSTEM AT DESIGN STAGE, FIRST TIME IN NTPC
• TALL TOP CLASSIFIER• MODIFIED VENTURI ( ALSO CERAMIC LINED)• FLAP TYPE MILL DISCHARGE VALVE (CERAMIC LINED)• BEARINGLESS SPRING LOADING• DOUBLE BEARING JOURNALS• MODIFIED VANE WHEEL ASSEMBLY• CERAMIC LINED BENDS, INNER CONE, ORIFICES• CERAMIC CARBIDE DUO CAST GRINDING ROLLS
• SPRING LOADED FLOATING FOUNDATION• HIGH CHROME BULL RING SEGMENTS• BURNER INLET ISOLATION VALVES• FEEDER DISCHARGE ISOLATION VALVE• DUST GAURD SEAL• JOURNAL TILTING
CONSTRUCTION & DESIGN FEATURESCONSTRUCTION & DESIGN FEATURES
CE VS MPSP DESIGNCE VS MPSP DESIGN
S.NO PARAMETERS CE MPSP
1 GRINDING ROLL (GR) NI-HARD DUO CAST WITH CERAMIC CARBIDE
INSERTS
2 BULL RING SEGMENT (BRS) NI-HARD HIGH CHROME
3 VANE WHEEL 45 ° 30 °
4 EXPECTED RUNNING HOURS 3000 11000
5 PM SCHEDULE BI-WEEKLY FOUR WEEKLY
6 COST OF GRINDING ELEMENTS (GR + BRS)
~ 3 LACS ~ 13 LACS
MILL MAINTENANCE PRACTICES & STRATEGIES
• REGULAR AND PERIODIC PREVENTIVE MAINTENANCE
• CONDITION / WALKDOWN BASED MAINTENANCE
• PLANNED MAINTENANCE (MAJOR)
• BREAKDOWN MAINTENANCE
• TIMELY PLANNING OF SPARES AND CONTRACTS
• OPTIMIZATION / MODIFICATIONS
MILL MAINTENANCE PRACTICES & STRATEGIES
• REGULAR AND PERIODIC PREVENTIVE MAINTENANCE
• CONDITION / WALKDOWN BASED MAINTENANCE
• PLANNED MAINTENANCE (MAJOR)
• BREAKDOWN MAINTENANCE
• TIMELY PLANNING OF SPARES AND CONTRACTS
• OPTIMIZATION / MODIFICATIONS
MILL PERFORMANCE FACTORSMILL PERFORMANCE FACTORS
• MILL CAPACITY• PF FINENESS• MILL REJECTS• MILL OUTLET TEMPERATURE• MILL BOWL DP• MILL POWER CONSUMPTION
• MILL CAPACITY DEPENDS UPON FOLLOWING FACTORS
HARD GROOVE INDEXHARD GROOVE INDEX
TOTAL MOISTURE CONTENTTOTAL MOISTURE CONTENT
AIR FLOWAIR FLOW
PF COAL FINENESSPF COAL FINENESS
MILL PERFORMANCE FACTORSMILL PERFORMANCE FACTORS
• PULVERISED COAL FINENESS
THE RECOMMENDED PF COAL FINENESS IS ABOVE 70% AND 98.0 % THROUGH 200 MESH AND 50 MESH
RESPECTIVELY
INITIAL FINENESS ACHIEVED : 60 TO 70% THROUGH INITIAL FINENESS ACHIEVED : 60 TO 70% THROUGH 200 MESH 200 MESH &MORE THAN 2% RETENTION ON 50 MESH&MORE THAN 2% RETENTION ON 50 MESH
ADJUSTMENTS DONE DURING PG TEST:ADJUSTMENTS DONE DURING PG TEST:
• INCREASE IN SPRING COMPRESSION : 9.5 TO 11.5 TONS• INCREASE IN VENTURY COLLOR HEIGHT : 50 MM • REDUCTION IN INVERTED CONE CLEARANCE : 30 MM• REMOVAL OF AIR RESTRICTION PLATE • CLASSIFIER SETTING : FROM 3 TO 5
MILL PERFORMANCE FACTORSMILL PERFORMANCE FACTORS
• MILL REJECTS
DENSITY BASED SEPARATION ON THE BOWL LEADS TO DENSITY BASED SEPARATION ON THE BOWL LEADS TO MILL REJECTS MILL REJECTS
AT SIMHADRI, THE MILLS ARE REJECTING THE AT SIMHADRI, THE MILLS ARE REJECTING THE MATERIALS WHICH ARE DIFFICULT TO GRIND LIKE MATERIALS WHICH ARE DIFFICULT TO GRIND LIKE STONES STONES AND PYRITES. THE TOTAL MILL REJECTS ARE AND PYRITES. THE TOTAL MILL REJECTS ARE AROUND 2-10 AROUND 2-10 KG PER HOURKG PER HOUR
STONE IS VERY LESS IN RAW COALSTONE IS VERY LESS IN RAW COAL
MILL PERFORMANCE FACTORSMILL PERFORMANCE FACTORS
• MILL OUTLET TEMPERATURE
GENERALLY THE RECOMMENDED VALUE OF MILL GENERALLY THE RECOMMENDED VALUE OF MILL OUTLET TEMPERATURE IS 100-X (X = % OF OUTLET TEMPERATURE IS 100-X (X = % OF VOLATILE VOLATILE MATTER IN THE COAL)MATTER IN THE COAL)
AT SIMHADRI WE ARE MAINTAINING THE MILL AT SIMHADRI WE ARE MAINTAINING THE MILL OUTLET TEMP AT 75 TO 85°C AS THE VOLATILE OUTLET TEMP AT 75 TO 85°C AS THE VOLATILE MATTER IN MATTER IN OUR COAL IS LESS AND THE MOISTURE OUR COAL IS LESS AND THE MOISTURE IS HIGHIS HIGH
MILL PERFORMANCE FACTORSMILL PERFORMANCE FACTORS
• MILL BOWL DIFFERENTIAL PRESSURE
THE RECOMMENDED VALUE BOWL DP IS 300 MMWC THE RECOMMENDED VALUE BOWL DP IS 300 MMWC AT FULL LOAD AT FULL LOAD
HIGHER ASH CONTENT, HIGHER REJECTION, LOW AIR HIGHER ASH CONTENT, HIGHER REJECTION, LOW AIR FLOW, EXCESS FINENESS AND ERODED MILL FLOW, EXCESS FINENESS AND ERODED MILL
INTERNALS INTERNALS LEAD TO HIGHER BOWL DPLEAD TO HIGHER BOWL DP
• POWER CONSUMPTION
THE POWER CONSUMED BYTHE POWER CONSUMED BY THE MILL MOTOR THE MILL MOTOR SHOULD NOT EXCEED THE SHOULD NOT EXCEED THE RATED CAPACITY. AT RATED CAPACITY. AT SIMHADRI THE CURRENT DRAWN BY MILL MOTOR AT SIMHADRI THE CURRENT DRAWN BY MILL MOTOR AT FULL LOAD IS WELL WITHIN THE LIMITSFULL LOAD IS WELL WITHIN THE LIMITS
MILL PERFORMANCE FACTORSMILL PERFORMANCE FACTORS
IT IS ALWAYS SUGGESTED THAT BOWL MILL PARAMETERS SHOULD BE OPTIMIZED FOR SATISFACTORY PERFORMANCE OF THE MILLS AND TO IMPROVE THE LIFE OF MILL COMPONENTS
AT SIMHADRI PG TEST IS JUST COMPLETED. OPTIMIZATION OF SPRING COMPRESSION IS IN PROGRESS
OPTIMISATION OF BOWL MILL PARAMTERS
THE FOLLOWING MODIFICATIONS WERE DONE WITHOUT AFFECTING THE MILL DESIGN/FLOW CONDITIONS (DURING ERECTION & COMMISSIONING) :
LUBE OIL SKID RELOCATION
INCREASE OF DISCHARGE PIPE DIA OF LUBE OIL SYSTEM FRO ¾” TO 1”DURING COMMISSIONING
LOCKING SYSTEM MODIFICATION OF JOURNAL STOP BOLT
EXTENSION OF SPRING SHAFT
PROVISION OF ON-LINE MILL REJECT CHOKING REMOVAL PORT
MODIFICATIONS
DATA FOR MILL PERFORMANCE FACTORS AT SIMHADRI
S.NO. DESCRIPTIOIN RATED PARAMETERSACTUAL PARAMETERS
1 ) Capacity66.3 tph 65
02)Fineness X Passing through200 mesh) >70% >80%
Retention on 50 mesh 2.00% <1%
03) Mill outlet Temp. 87 deg c 80-85 deg c
04) Bowl DP Maxm 300 mm WC 300 to 340 mmWC
05) Mill Amperage Mill 137A 120-125A
06) Rejects Low
07) OTHERS,
Volatile matter 22min <22%
Moisture 12.00% .12-14 %
Mill air inlet temp. 265 deg c 250 -270 deg c
PA Flow 95 tph 90-105 tph
HGI 55 >55
GCV 3300 Kcal/kg ~3300 k cal/kg
Ash ~40 >40
THANK YOUTHANK YOU