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COAL MILL/PULVERIZER
 IN THERMAL POWER PLANTS




         SHIVAJI CHOUDHURY
1.Introduction
   Coal continues to play a predominant role in the
    production of electricity in the world, A very large
    percentage of the total coal is burned in pulverized
    form.
   Pulverized coal achieved its first commercial success
    in the cement industry. At Wisconsin Electric Power
    Company, the use of pulverized coal was also shown
    to be a viable fuel for electrical power production after
    World War I
    Pulverized coal burns like gas, can be easily lighted
    and controlled.
2.Coal pulverizer/mill system
   One of the critical power
    plant components that is
    relied upon to convert
    the energy stored in coal
    into electricity is the coal
    pulverizer or mill.

   The coal flow is
    controlled by the feeder,
    allowing coal to flow into
    the pulverizer mill.

    The pulverized coal and
    air mixture is then
    transport to the boiler
    burner panels.
3.Boiler

           Boiler drum
                                       Reheater
                                          Final Super
     Platen Super                         heater
     heater                               LTSH
                                           Economizer
                                                        Coal bunker
                   Wind Box
                          Secondary
                                         PA duct
                          air duct
             Furnace
                                      Flue gas
                             APH      duct               Coal feeder


                           F D Fan    P A Fan
                                                              Coal
                                                              Pulverizer
4.Pulverizer
    The pulverizer receives the raw coal and
    reduces it to a very fine, specified size
    consist, similar to face powder.
    There are four primary principals involved
    in pulverization:
   • Drying
   • Grinding
   • Circulation
   • Classification
4.1.Drying

   The coal that is passing through a
    pulverizer is entrained by the use of hot air
    usually from the air heater.
    During the pulverization process the
    surface area of the coal particles increases
    dramatically exposing fresh coal to the
    entrainment air.
   The inherent and surface moisture of the
    coal is reduced by the exposure to hot air.
4.2.Grinding
   There are three basic
    types of grinding:

   1. Impaction – where the
    material to be ground is hit
    or impacted by an outside
    force

   2. Crushing – where
    material is forced between
    two fixed objects

   3. Attrition – where material
    is ground by rubbing or
    friction
4.3.Circulation


   The primary air, is the method of
    circulating the coal through the pulverizer.
    Circulating air is also important in allowing
    for the removal of heavy material such as
    pyrites, extraneous metal, etc. by
    centripetal force that otherwise might
    damage the grinding mechanisms.
4.4.Classification
   The circulating air is also
    used to classify the
    pulverized coal product
    prior to carrying it to the
    burners.
    The classifier, located on
    the top of a mill returns the
    over-size material back to
    the pulverizer but allows
    the proper-sized material to
    pass out of the mill to the
    burners. classifiers are
    critical in providing the
    desired quality of pulverized
    coal with the desired
    fineness
5.Types of Pulverizers
Speed      Low         Medium        High
           10 to 20    40 to 70      900 to
           rpm         rpm           1000 rpm
Type       Ball tube   Bowl          Hammer
           mill        Ball & race   mill
                       mill
Dominating Attrition   Crushing      Impact
principle
6.C-E Raymond Bowl Mill




                BOWL MILL
7.Ball and race mill
8.Foster Wheeler MBF Mill
9.Tube Mill
10.Bowl Mill
   Bowl mills are employed to pulverize the pre-crushed
    raw coal to the required fineness before it is admitted
    into the boiler furnace for combustion.
    The mill output can be easily varied, as per the
    turndown ratio from its minimum to maximum load.
   Crushed raw coal at a controlled rate is fed into the
    revolving bowl of the Bowl Mill.
   Centrifugal force feeds the coal uniformly over the
    replaceable grinding ring where independently spun
    rolls exert the required grinding pressure. The rolls do
    not touch the grinding ring even when the mill is
    empty.
10.1.Designation of C-E Bowl Mills
11.Bowl Mill




               Grinding rolls
12.Pulveriser
for 500 MW

1. TYPE-    XRP 1003

2.NO OF MILL-      10

3.CAPACITY -     62.9 T/HR
4.MOTOR –        525 KW

5.SPEED -       600 RPM
13. Mill Performance Criteria
   FINENESS,
   COAL GRINDABILITY,
   CAPACITY,
   REJECTS
13.1.Fineness

   Fineness is an indicator of the quality of the pulverizer
    action. Specifically, fineness is a measurement of the
    percentage of a coal sample that passes through a set of
    test sieves usually designated at 50, 100, and 200 mesh
   A 70% coal sample passing through a 200 mesh screen
    indicates optimum mill performance.
   The mill wear and the power consumption are increased if
    the 70% value is exceeded.
    Values lower than 70% mean higher carbon loss and
    increased fuel consumption.
   In addition, coal retained on the 50 mesh screen should be
    in the 1–2% range. Higher values indicate worn internals or
    improper settings. Also, the higher percentages can cause
    boiler slagging and high unburned carbon.
13.2.Sieve distribution chart & Fineness testing
screen




 - Plot of coal fineness on   Fineness testing screen
    Rosin and Rammler
13.3.Mill capacity vs Grindability

                      Figure shows the
                       effect of coal
                       grindability (HGI)
                       and desired
                       fineness (percent
                       passing a 200
                       mesh screen) on
                       the mill capacity.
13.4.Moisture and grindability
effects on mill capacity
                     Figure demonstrates how
                      moisture and grindability
                      affect pulverizer capacity.
                     The dashed line estimates
                      the increase in mill capacity
                      in going from a high-volatile
                      B bituminous coal with a 55
                      HGI, 12% moisture and a
                      desired mill output of 70%
                      through a 200 mesh screen
                      to a highvolatile B bituminous
                      coal with an HGI value of 60,
                      a moisture content of 14%
                      and the same fineness.
13.5.Mill Rejects

   The amount of pulverizer
    rejects is one indication
    of mill performance.
   Pyrites are the common
    mineral iron disulfide
    (FeS2) that has a pale
    brass-yellow color and
    metallic luster.
    However, it is not
    economical to attempt to
    grind and burn pyrites &    Pyrite Scraper and Guard Assembly

    rock.
13.6. Grindability Index, Moisture, Fineness vs mill
           capacity (XRP 883 Bowl mill)




                              Design parameters
                              Mill capacity- 42.48 T/HR
                              Total moisture-10%
                               HGI -50
13.7.Logic tree – Mill Fineness


                       Decrease
                         in mill
                       fineness
                             SIEVE TEST RESULTS
                             70% THRU 200 MESH
                             99.2% THRU 50 MESH


Classifier   Loss of    Ring or    Classifier Exceeding
  Vane        Roller     Roller      Vane        Mill
position     tension     wear        wear      capacity
14.Abrasion in pulverizer
   In coal pulverization,
    5–20% of the material
    being crushed is abrasive
    mineral. Coal is not
    abrasive by itself. The
    minerals in coal that are the
    most abrasive are quartz
    and pyrite, which cause a
    abrasion or severe wear.
    carbides in the metal part,
    High chromium cast iron
    materials are used for
    improved abrasion
    resistance.



                                    Worn Journal Roll
14.1.CHEMICAL COMPOSITION OF THE
INSERTS GRINDING ROLLS

   This specification of high chrome white cast iron
    inserts for making Insert Grinding Rolls.

    CHEMICAL COMPOSITION OF THE INSERTS:
   C = 2.6 – 3.0 %
   Cr = 15.0 – 22.0 %
   Mo = 1.0 – 2.0 %
   W = 1.0 – 2.0%
   Mn = 1.0 – 2.0 %
   Si = 0.5 – 1.0 %
   S = 0.1 % max
   P = 0.1 % max
15.Erosion in Pulverizer
   Erosion by mineral
    particles picked up in the
    air stream carrying
    pulverized coal through
    the mill, classifier,
    exhauster, and transport
    pipe is a recognized
    problem.
   Erosion can produce
    holes in steel liners and
    deep depressions in large
    section cast parts.
    There has been success
    in the industry using
    ceramic materials.
                                 Classifier cone with ceramic
16.Startup Procedures
   The startup procedures, in addition
    to the controls and interlocks,
    should follow the requirements of
    NFPA 85.
17.Condition Monitoring

   The main technologies used in
    condition monitoring are:
   Vibration analysis ,
   Lubricant Oil analysis
     Particle count
     Viscosity
     Total acid measure
     Condition of oil additives
     Sediment in Lubricating Oils
   Any other test recommended by OEM.
18.Inspection
   Following inspection parameters are critical for bowl
    mill performance:
   • Classifier internal condition
   • Deflector ring length
   • Inverted cone clearance
   • Journal assembly condition
   • Grinding roll-to-bowl clearance
   • Spring pressure for rolls
   • Pyrite scraper clearance
   • Pyrite rejects chute and/or damper condition
   • Feeder settings
   • Air in-leakage sources
19.Test code of Pulverizer:
:ASME PTC 4.2
   The purpose of this code is to establish
    procedures for conducting performance
    tests to determine:
   Capacity, Fineness of product, Raw coal feed,
    Grindability, Moisture, Sizing, Power consumption and
    Effect of changes in raw coal Characteristics on
    product fineness, pulverizer capacity, and power
    consumption.
   Effect of changes in pulverizer component settings on
    product fineness, pulverizer capacity, and power
    consumption.
THANKING YOU
Logic tree – Mill Fineness


                       Decrease
                         in mill
                       fineness
                            SIEVE TEST RESULTS




Classifier   Loss of    Ring or    Classifier Exceeding
  Vane        Roller     Roller      Vane        Mill
position     tension     wear        wear      capacity

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Coal mill pulverizer in thermal power plants

  • 1. COAL MILL/PULVERIZER IN THERMAL POWER PLANTS SHIVAJI CHOUDHURY
  • 2. 1.Introduction  Coal continues to play a predominant role in the production of electricity in the world, A very large percentage of the total coal is burned in pulverized form.  Pulverized coal achieved its first commercial success in the cement industry. At Wisconsin Electric Power Company, the use of pulverized coal was also shown to be a viable fuel for electrical power production after World War I  Pulverized coal burns like gas, can be easily lighted and controlled.
  • 3. 2.Coal pulverizer/mill system  One of the critical power plant components that is relied upon to convert the energy stored in coal into electricity is the coal pulverizer or mill.  The coal flow is controlled by the feeder, allowing coal to flow into the pulverizer mill.  The pulverized coal and air mixture is then transport to the boiler burner panels.
  • 4. 3.Boiler Boiler drum Reheater Final Super Platen Super heater heater LTSH Economizer Coal bunker Wind Box Secondary PA duct air duct Furnace Flue gas APH duct Coal feeder F D Fan P A Fan Coal Pulverizer
  • 5. 4.Pulverizer  The pulverizer receives the raw coal and reduces it to a very fine, specified size consist, similar to face powder.  There are four primary principals involved in pulverization:  • Drying  • Grinding  • Circulation  • Classification
  • 6. 4.1.Drying  The coal that is passing through a pulverizer is entrained by the use of hot air usually from the air heater.  During the pulverization process the surface area of the coal particles increases dramatically exposing fresh coal to the entrainment air.  The inherent and surface moisture of the coal is reduced by the exposure to hot air.
  • 7. 4.2.Grinding  There are three basic types of grinding:  1. Impaction – where the material to be ground is hit or impacted by an outside force  2. Crushing – where material is forced between two fixed objects  3. Attrition – where material is ground by rubbing or friction
  • 8. 4.3.Circulation  The primary air, is the method of circulating the coal through the pulverizer. Circulating air is also important in allowing for the removal of heavy material such as pyrites, extraneous metal, etc. by centripetal force that otherwise might damage the grinding mechanisms.
  • 9. 4.4.Classification  The circulating air is also used to classify the pulverized coal product prior to carrying it to the burners.  The classifier, located on the top of a mill returns the over-size material back to the pulverizer but allows the proper-sized material to pass out of the mill to the burners. classifiers are critical in providing the desired quality of pulverized coal with the desired fineness
  • 10. 5.Types of Pulverizers Speed Low Medium High 10 to 20 40 to 70 900 to rpm rpm 1000 rpm Type Ball tube Bowl Hammer mill Ball & race mill mill Dominating Attrition Crushing Impact principle
  • 11. 6.C-E Raymond Bowl Mill BOWL MILL
  • 15. 10.Bowl Mill  Bowl mills are employed to pulverize the pre-crushed raw coal to the required fineness before it is admitted into the boiler furnace for combustion.  The mill output can be easily varied, as per the turndown ratio from its minimum to maximum load.  Crushed raw coal at a controlled rate is fed into the revolving bowl of the Bowl Mill.  Centrifugal force feeds the coal uniformly over the replaceable grinding ring where independently spun rolls exert the required grinding pressure. The rolls do not touch the grinding ring even when the mill is empty.
  • 17. 11.Bowl Mill Grinding rolls
  • 18. 12.Pulveriser for 500 MW 1. TYPE- XRP 1003 2.NO OF MILL- 10 3.CAPACITY - 62.9 T/HR 4.MOTOR – 525 KW 5.SPEED - 600 RPM
  • 19. 13. Mill Performance Criteria  FINENESS,  COAL GRINDABILITY,  CAPACITY,  REJECTS
  • 20. 13.1.Fineness  Fineness is an indicator of the quality of the pulverizer action. Specifically, fineness is a measurement of the percentage of a coal sample that passes through a set of test sieves usually designated at 50, 100, and 200 mesh  A 70% coal sample passing through a 200 mesh screen indicates optimum mill performance.  The mill wear and the power consumption are increased if the 70% value is exceeded.  Values lower than 70% mean higher carbon loss and increased fuel consumption.  In addition, coal retained on the 50 mesh screen should be in the 1–2% range. Higher values indicate worn internals or improper settings. Also, the higher percentages can cause boiler slagging and high unburned carbon.
  • 21. 13.2.Sieve distribution chart & Fineness testing screen - Plot of coal fineness on Fineness testing screen Rosin and Rammler
  • 22. 13.3.Mill capacity vs Grindability  Figure shows the effect of coal grindability (HGI) and desired fineness (percent passing a 200 mesh screen) on the mill capacity.
  • 23. 13.4.Moisture and grindability effects on mill capacity  Figure demonstrates how moisture and grindability affect pulverizer capacity.  The dashed line estimates the increase in mill capacity in going from a high-volatile B bituminous coal with a 55 HGI, 12% moisture and a desired mill output of 70% through a 200 mesh screen to a highvolatile B bituminous coal with an HGI value of 60, a moisture content of 14% and the same fineness.
  • 24. 13.5.Mill Rejects  The amount of pulverizer rejects is one indication of mill performance.  Pyrites are the common mineral iron disulfide (FeS2) that has a pale brass-yellow color and metallic luster.  However, it is not economical to attempt to grind and burn pyrites & Pyrite Scraper and Guard Assembly rock.
  • 25. 13.6. Grindability Index, Moisture, Fineness vs mill capacity (XRP 883 Bowl mill) Design parameters Mill capacity- 42.48 T/HR Total moisture-10% HGI -50
  • 26. 13.7.Logic tree – Mill Fineness Decrease in mill fineness SIEVE TEST RESULTS 70% THRU 200 MESH 99.2% THRU 50 MESH Classifier Loss of Ring or Classifier Exceeding Vane Roller Roller Vane Mill position tension wear wear capacity
  • 27. 14.Abrasion in pulverizer  In coal pulverization, 5–20% of the material being crushed is abrasive mineral. Coal is not abrasive by itself. The minerals in coal that are the most abrasive are quartz and pyrite, which cause a abrasion or severe wear.  carbides in the metal part, High chromium cast iron materials are used for improved abrasion resistance. Worn Journal Roll
  • 28. 14.1.CHEMICAL COMPOSITION OF THE INSERTS GRINDING ROLLS  This specification of high chrome white cast iron inserts for making Insert Grinding Rolls.  CHEMICAL COMPOSITION OF THE INSERTS:  C = 2.6 – 3.0 %  Cr = 15.0 – 22.0 %  Mo = 1.0 – 2.0 %  W = 1.0 – 2.0%  Mn = 1.0 – 2.0 %  Si = 0.5 – 1.0 %  S = 0.1 % max  P = 0.1 % max
  • 29. 15.Erosion in Pulverizer  Erosion by mineral particles picked up in the air stream carrying pulverized coal through the mill, classifier, exhauster, and transport pipe is a recognized problem.  Erosion can produce holes in steel liners and deep depressions in large section cast parts.  There has been success in the industry using ceramic materials. Classifier cone with ceramic
  • 30. 16.Startup Procedures  The startup procedures, in addition to the controls and interlocks, should follow the requirements of NFPA 85.
  • 31. 17.Condition Monitoring  The main technologies used in condition monitoring are:  Vibration analysis ,  Lubricant Oil analysis  Particle count  Viscosity  Total acid measure  Condition of oil additives  Sediment in Lubricating Oils  Any other test recommended by OEM.
  • 32. 18.Inspection  Following inspection parameters are critical for bowl mill performance:  • Classifier internal condition  • Deflector ring length  • Inverted cone clearance  • Journal assembly condition  • Grinding roll-to-bowl clearance  • Spring pressure for rolls  • Pyrite scraper clearance  • Pyrite rejects chute and/or damper condition  • Feeder settings  • Air in-leakage sources
  • 33. 19.Test code of Pulverizer: :ASME PTC 4.2  The purpose of this code is to establish procedures for conducting performance tests to determine:  Capacity, Fineness of product, Raw coal feed, Grindability, Moisture, Sizing, Power consumption and Effect of changes in raw coal Characteristics on product fineness, pulverizer capacity, and power consumption.  Effect of changes in pulverizer component settings on product fineness, pulverizer capacity, and power consumption.
  • 35. Logic tree – Mill Fineness Decrease in mill fineness SIEVE TEST RESULTS Classifier Loss of Ring or Classifier Exceeding Vane Roller Roller Vane Mill position tension wear wear capacity