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COAL
Chemical Structure of Coal
(Depending upon source, structure may be widely different)




                                            Anthracite Coal
                                            Carbon 92-98%
COAL : DEFINITION
Coal is a stored fossil fuel, occurring in
layers in the earth’s crust, which has
been formed by the partial decay of
plant materials accumulated millions of
years ago and further altered by the
action of heat and pressure.
COAL FORMATION
THEORIES OF COAL FORMATION

 IN SITU THEORY
 DRIFT THEORY - Flood /Tsunami type wave
                               (velocity 800 km/h)
 300 million of years (earth is 4.6 billion years old)
 15-20 m OF PLANT MATERIAL= 1 m OF COAL SEAM
 In INDIA 30 m seam of coal has been found


450-600 m of plant material might have
accumulated at that place.
(Taipei 101:509 m tallest building in world)
COALIFICATION
COAL                     %C C         H      O     Heating
                                                   value
                                                   (MJ/kg)
Cellulose                44.5   100   13.9   111   -
Wood                     50.0   100   12.0   88    19.77
Peat                     59.9   100   10.0   57    18.66
                  Time



Lignite                  61.8   100   7.8    54    20-25
Brown coal               69.5   100   7.9    36    27.20
Bituminous coal          78.7   100   6.0    21    32.10
Anthracite               91.0   100   4.7    5.2   32.56
Graphite                 100    100   0.0    0.0   32.91
COAL RANKS
1.Peat: starting point of coal formation
  does not come in the category of coal
  Carbon: 60-64%; Oxygen:35-30%
2. Lignites: mark the transition of peat to coal
   Carbon: 60-75% ; Oxygen: 30-20%
   Colour: black, brown, earthy
   Disintegrate very easily
   Briquetting is done
  Neyveli Lignite Corporation, Chennai, Tamilnadu
  Possesses largest reserves of Lignite in India
  Electricity generation: 2490 MW
COAL RANKS contd…
3. Bituminous coals
 Sub-bituminous:
 Between lignites and bituminous
 Carbon: 75-83% ; Oxygen: 20-10%
 No caking power (Briquettes can not be made)
Bituminous: black and banded
Industrial and domestic usage
Carbon: 75-90%: Oxygen:10-5%
Semi-bituminous:
Between bituminous and anthracite
Metallurgical coke formation
Carbon: 90-93%; Oxygen:4-1%
COAL RANKS contd…
4. Anthracites
   Highest rank of coal
   Extreme of metamorphosis
   from the original plant material
  Carbon: 93+%: Oxygen: 2-1%
  Caking power zero
Unusual coals
Cannels: found rarely; high hydrogen content: burn
with smoke and bright flame; does not fall in any category.
Torbanites: fine grained coal, named after Torbane Hill
of Scotland, rich in paraffin oil.
Unusual Solid Fuel
         (Methane Clathrate)
 Burning Ice
 1 mole methane in 5.75 mole
  H 2O
 Available in Deep sea (methane
  from trench + cold water + high
  pressure) and at the lower ice
  layer in Antarctica
 It is expected that 15,000 Gt
  (21×1015 m3) of methane is
  available in this form (as
  compared to 1,000 Gt of Coal)
WORLD PRODUCTION OF COAL IN YEAR 2006

                                       % of world production
            Country   Million tonnes

China                     2380                 39.75
USA                       1053.6               17.59

India                     447.3                7.47

Australia                 373.8                6.24

South Africa              256.9                4.29

Canada                     62.9                1.05

United Kingdom             18.6                0.31

Pakistan                   4.3                 0.07

Japan                      1.3                 0.02

Total of the world       5,986.90               100
WORLD PRODUCTION OF COAL IN YEAR 2006

              Canada       United   Pakistan
     South
                          Kingdom
     Africa                               Japan
              Australia



         India

                                                  China




                 USA
WORLD TOP TEN COAL PRODUCING AND
     CONSUMING COUNTRIES




                    1 quadrillion=1000 trillion
                    1 Btu=1.055 kJ
COAL RESERVES OF INDIA
                                                           (As on 1.1.2007
                                                         in billion tonnes)

                 TOTAL         PROVED         INDICATED INFERRED
 Type of coal
                RESERVE        RESERVE         RESERVE   RESERVE

  COKING            32              17             13               2
   NON-
                   223              81            105              36
  COKING
   TOTAL           255              98             118             38

Years to consume this coal with present rate: 600
            Cokes are the solid carbonaceous material
            derived from destructive distillation of
            low-ash, low-sulfur bituminous coal.          Source: MoC
COAL RESOURCES OF STATES
Proved: boreholes (1200m deep) @ 400 m
                                                IN MILLION TONNES Jan 1, 2007
Indicated & Inferred: boreholes @ 1-2 km
         State       Proved     Indicated   Inferred    Total     % of total
 Jharkhand            36881      31094       6339       74314        29.11
 Orissa               17464      30239       14296      61999        24.29
 Chhattisgarh         10182      26826       4443       41451        16.24
 West Bengal          11454      11810       5071       28335        11.10
 Madhya Pradesh       7584        9259       2934       19777         7.75
 Andhra Pradesh       8475        6328       2658       17461         6.84
 Maharashtra          4856        2822       1992       9670          3.79
 Uttar Pradesh         766         296         0        1062          0.42
 Meghalaya             118         41         301        460          0.18
 Assam                 315         27         34         376          0.15
 Bihar                  0           0         160        160          0.06
 Arunachal Pdesh        31         40         19          90          0.04
 Sikkim                 0          55         18          73          0.03
 Nagaland               3           1         15          19          0.01
 Total                98129      118838      38280     255247         100
GRADING OF INDIAN COAL
   Coking coal (carbon: 81-91%)
   Non-coking coal
  Grades of coking coal
  Grade                Industry             Ash %
  I                    steel                <15
  II                   steel                15-18
  I                    washery*             18-21
  II                   washery*             21-24
  III                  washery*             24-28
  IV                   washery*             28-35
* Washed Coal is used as fuel in thermal power plants
GRADING OF INDIAN COAL
 High ash content (up to 50%)
 Lower heating/calorific value
 Inferior quality but suitable for power gen.
Grades of non-coking coal
Grade        UHV, kcal/kg            Ash %
A             >6200                   <13.56
B             5600-6200              13.56-17.91
C             4940-5600              17.91-22.69
D             4200-4940              22.69-28.06
E             3360-4200              28.06-34.14
F             2400-3360              34.14-41.10
G             1300-2400              41.10-49.07
UHV:Useful Heating Value       Based on 6 % moisture content
=8900-138×[ash% + moisture%]
ROYALTY TO STATES
 Nationalization in 1971
 Coal companies are paying the
  royalty to states
 This varies from Rs 90-250/tonne
 The rate is dependent of coal
   grade
 Rates are 16 August 2002 onwards
IMPORT OF COAL
Coking and non-coking coals being imported
 Year        Coking     Non-coking    Total
 1991/92     5.27       0.66          5.93
 1996/97     10.62      2.56          13.18
 2000/01     11.06      9.87          19.70
 2003/04     12.99      8.69          21.68
 2005/06     16.89      21.70         38.59
 2006/07     22.00      23.00         45.00
                                     In million tonnes
ANALYSIS OF COAL

 Proximate analysis
 Ultimate analysis
 Heating/calorific value
PROXIMATE ANALYSIS
1. Moisture content: 105 -110 oC
2. Volatiles: 925±15 oC for 7 min time (with lid)
3. Fixed carbon: by difference
4. Ash: 800±15 oC (without lid)

REPORTING: AS RECEIVED BASIS, MOISTURE FREE
BASIS/DRY BASIS OR DRY ASH FREE BASIS

IS:1350-I (1984)
EXAMPLE OF PA
A sample of finely ground coal of mass 0.9945 g was
placed in a crucible of 8.5506 g in an oven, maintained at
105 oC for 4.0 ks. The sample was then removed, cooled in
a dessicator and reweighed; the procedure being repeated
until a constant total mass of 9.5340 g was attained. A
second sample, of mass 1.0120 g in a crucible of mass
8.5685 g was heated with a lid in a furnace at 920 oC for
420 s. On cooling and reweighing, the total mass was
9.1921 g. This sample was then heated without a lid in the
same furnace maintained at 725 oC until a constant total
mass of 8.6255 g was attained. Calculate the proximate
analysis of the sample and express the results on “as
sampled” and “dry, ash-free” basis.
EXAMPLE OF PA contd..
MOISTURE (from first sample)
 mass of sample = 0.9945 g
 mass of dry coal = (9.5340-8.5506) = 0.9834 g
 mass of moisture = (0.9945-0.9834) = 0.0111 g
 % moisture       = 0.0111 × 100/0.9945
                  = 1.11 %
 ASH (from second sample)
       Mass of sample = 1.0120 g
       Mass of crucible = 8.5685 g
Heating up to 920ºC in absence of air removes volatile matters,
subsequent heating up to 725ºC in presence of air burns all
fixed carbon of the sample leaving behind ash in the crucible.
       Mass of ash (remnant in crucible) = (8.6255 - 8.5685)
                                         = 0.0570 g
        % ash = 0.0570 × 100/1.0120 = 5.63 %
EXAMPLE OF PA contd..
VOLATILE MATTER
  Initial mass of sample + crucible = 1.0120 + 8.5685 = 9.5805 g
  Final mass after heating up to 920ºC (without air) = 9.1921 g
  Mass of volatile matter + moisture = Initial – Final mass
                            = (9.5805-9.1921) g
                            = 0.3884 g
  % Moisture + Volatiles = 0.3884 x 100/1.0120
                            = 38.3794 %
% VOLATILE MATTER = 38.3794 – 1.11 (% Moisture)
                            = 37.26 %
FIXED CARBON
       % FC = 100 - % VM - % ash - % moisture
             = 100 – 37.26 - 5.53 - 1.11
             = 55.98 %
EXAMPLE OF PA contd..
Proximate analysis as received basis
  Moisture          : 1.11 %
  Ash               : 5.63 %
  Fixed carbon      : 55.99 %
  Volatile matter   : 37.26 %

Proximate analysis on dry, ash free basis
  Moisture + ash = 1.11 + 5.63 = 6.74%
  Fixed carbon:     55.99x100/(100-6.74) = 60.04 %
  Volatile matter: 37.26x100/(100-6.74) = 39.95 %
ULTIMATE ANALYSIS
1.   Carbon
2.   Hydrogen
3.   Oxygen
4.   Sulfur          :0.5-2.50 %
5.   Nitrogen        :1.0-2.25 %
6.   Phosphorus      :0.1%;Blast Furnace: <0.01 %
7.   Chlorine
Mercury: A big problem from NTPC plants
(up to 0.3mg/kg)
IS:1350- IV (1974)
HEATING VALUE
1. Calculated from proximate analysis
2. Calculated from ultimate analysis
3. Experimental determination


1. Gross/High heating value
2. Useful/low heating value
      Hydrogen            Water (gas/vapor or liquid phase)
      Carbon              Carbon Dioxide (gas phase)
      Latent heat of vaporization of water: 2.26 MJ/kg
HEATING VALUE
1. Calculated from proximate analysis
TAYLOR AND PATTERSON RELATIONSHIP
HV=4.19 (82FC+ a VM) kJ/kg
Where FC and VM are on dry ash free basis and a is
an empirical constant which depends on the VM
content of coal.                 170
                                 160
                                 150
                                 140
                                 130
                                 120
                                 110
                                 100
                                  90
                                  80
                                       0    10   20   30   40



VM     5   10    15   20   25   30         35    38   40
a     145 130 117 109 103       98         94    85   80
HEATING VALUE

2. Calculated from ultimate analysis


DULONG FORMULA
HV=338.2C+1442.8(H-O/8)+94.2S kJ/kg
Where C, H, O and S are the % of these elements on
dry ash free basis.
HEATING VALUE
3. Experimental determination: Bomb calorimeter
 solid /liquid samples can be analyzed
 1 g air dried sample is burnt in a bomb in oxygen
  atmosphere
 rise in temperature gives the heat liberated and
  heating value is determined after doing the
  corrections for resistance wire and thread.
 microprocessor based bomb calorimeters are now
  available
IS:1350-II (1970)
BOMB OF CALORIEMETER
VARIOUS COMPONENTS OF BOMB
 CALORIMETERIC EQUIPMENT
ROUTES OF GENERATION OF HEAT AND
            POWER FROM COAL
1. Direct use as thermal energy in heating processes,
   furnaces and domestic heating by open fires
2. Transfer of the heat to a thermal fluid and application of
   the latter for heating and power e.g., steam for heating in
   process industry, central heating and electricity
   generation by steam turbines
3. Gas turbine route to electricity generation
4. Conversion to gas/liquid fuels and subsequent usage in
   IC engines/turbines (gas/steam)
ROUTE I (Direct Heating)

 Domestic cooking (Chula at tea stalls, dhaba, bakery)
 Space heating (Fireplace)
 Lime and brick kilns (Direct heating of stack)
 Ceramic industry (Oven/Furnace)
ROUTE II (Thermal Fluid)

   Generation of steam in a boiler
   Space heating by transferring heat of steam to air
   Process industry : Cogeneration is employed
   Utility services : steam turbines used
SUPERCRITICAL BOILERS: A RECENT CONCEPT
Critical pressure: 218 bar (21.8 MPa); Critical temperature: 374oC
Mark Benson; in 1922 Patent was granted
22 MPa pressure ; η= 1-T1/T2 ≈ 0.53

GOVERNMENT ALLOWED ELECTRICITY GENERATION
BY PRIVATE DEVELOPERS
   Tariffing
   Wheeling
   Banking
ROUTE II contd..
                                                                                                  Hot air
                                                                                                  for
                                                                         Heat                     space
  Coal                    Boiler                      Steam
                                                                         exchanger                heating

                                          Steam
                                                                                                  Air
             Condensate
                          Steam



                                                        Cogeneration
                                                  Steam
                                                  turbine           Alternator                 to grid
Alternator




                                                                                 Electricity
                                  Condensate




          Steam
                                                            Steam
          turbine


Electricity to grid                                     Process plant
ROUTE III
Coal                                        Vent
                          Preheated air
Pulverizer                                  Heat
                                          exchanger




                          Turbine
                          exhaust
       Combustion
       chamber
                    Gas turbine     Compressor      Alternator




                                    Air            Electricity
                                                     to grid
ROUTE III
                                                     Vent
                                   Preheated air
                                                     Heat
                                                   exchanger




                                   Turbine
                                   exhaust
       Combustion
       chamber
                          Gas turbine        Compressor      Alternator


Coal


                                             Air            Electricity
                Gasifier and gas                              to grid
                cleaning unit
ROUTE IV (Pyrolysis / Gasification)

1. Partial Gasification or Pyrolysis /coking
   /carbonization / destructive distillation
   (heating in the absence of air)
   • Solid
   • Liquid
   • Gas

2. Complete gasification with air/oxygen
   •   Gas
PYROLYSIS

Low temperature carbonization                   500-700 oC
     Coke (solid fuel) maximum; classical domestic smokeless fuel
     production


Medium temperature carbonization               700-900 oC
     Liquid fraction for chemicals recovery/liquid fuel


High temperature carbonization                   >900 oC
     Coke for metallurgical furnaces; gas yield high; liquid low
PYROLYSIS
     Coal   Pretreatment
                 unit
                                         Water in     Gas
Flue gas                                              for IC engines/
                                                      Gas turbines/
            Pyrolyser            Condenser            thermal
                                                      applications
                             Water out

             Coke                          Liquid        Coal tar
                                           fraction      Liquid fuels
                                                         Chemicals
                    Gas for heating of pyrolyser
GASIFICATION




 3




             1k mole
12x3=36 kg                      ≈18 Liter
             =1000.R.T/P (m3)
             =22.41 Nm3
(Air Separation
     Unit)
ROUTE IV BERGIUS PROCESS
Coal is hydrogen starved/hydrogen needs to be added to make it
liquid (directly or indirectly)

1. Bergius process
   Friedrich Karl Rudolf Bergius (Germany) in 1913,
   Nobel Prize in 1931 (Shared with Carl Bosch)
   By end of World war II – most of the fuel for
         German army was produced by this method.
   Hydrogenation of vegetable oils
2. Fischer-Tropsch process
    Franz Fischer and Hans Tropsch in 1926, Germany
BERGIUS PROCESS
Coal     T=400-500 oC         Hydrogen
         P= 20 -70 MPa
         Catalyst=Tin
         Conver.=97%            Fractionating
                                column

        Pulverizer
                                                HCs
                Bergius
                Reactor
         Coal pasting
         unit


                          Heavy fraction
F-T PROCESS
   Coal       T=150-250 oC
              P= 1 -25 Mpa
              Catalysts : Fe, Co
                                        Fractionating
                                        column

           Gasification
           unit                                         HCs
                    F-T
Syn gas
                    Reactor
            Syn gas
            Cleaning


          (Large number of patents worldwide)
F-T PROCESS (COMMERCIAL PLANTS)
                 South Africa Oil and Gas
                  Company
                 1950 established
                 Oldest plant proving the F-T
                  process viability
                 Presently engaged in Qatar,
                  Iran and Nigeria in similar
                   projects
F-T PROCESS (COMMERCIAL PLANTS)
F-T PROCESS(COMMERCIAL PLANTS)
UNDERGROUND/ IN SITU COAL
          GASIFICATION
A process applied to the non-mined coal seams
Injection and production wells are drilled
End gas mix depends on type of coal seam
Air/ oxygen can be used for gasification
Syn gas can be used for power generation in combined cycle
Syn gas can be converted to chemicals/fuel by F-T process
UNDERGROUND/ IN SITU COAL
      GASIFICATION




                Source: World Coal Institute
COAL COMBUSTION AND ENVIORNMENT
 Global warming
 Green house gases: water vapor, carbon dioxide,
  methane, nitrous oxide, HFCs (hydrofluorocarbons),
  PFCs (perfluorocarbons), SF6 (Sulphur Hexafluoride)
 SF6 is 22, 200 more potential than CO2
 Carbon dioxide gas: main culprit from fossil fuels; not
  from biomass
 Intergovernmental Panel on Climate Change (IPCC)
 Nobel Peace Prize 2007 : R. K. Pauchari and Al Gore
 Reduction in Carbon Dioxide emissions
 G8 meeting in Japan in July 2008
COAL COMBUSTION AND ENVIORNMENT




             Present CO2 level:483 PPM




Carbon Dioxide Emissions and Carbon Dioxide Concentrations (1751-2004)
COAL COMBUSTION AND ENVIORNMENT




 Global Carbon Cycle (Billion Metric Tons Carbon)
COAL COMBUSTION AND ENVIORNMENT




U.S. Anthropogenic Greenhouse Gas Emissions by Gas,
2006 (Million Metric Tons of Carbon Dioxide Equivalent)
ULTIMATE SOLUTIONS



Solar: photovoltaic




Fuel cells: Chemical to electrical conversion




Hybrid vehicles: Honda introduced in India

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Ch 20102 coal

  • 2. Chemical Structure of Coal (Depending upon source, structure may be widely different) Anthracite Coal Carbon 92-98%
  • 3. COAL : DEFINITION Coal is a stored fossil fuel, occurring in layers in the earth’s crust, which has been formed by the partial decay of plant materials accumulated millions of years ago and further altered by the action of heat and pressure.
  • 5. THEORIES OF COAL FORMATION  IN SITU THEORY  DRIFT THEORY - Flood /Tsunami type wave (velocity 800 km/h)  300 million of years (earth is 4.6 billion years old)  15-20 m OF PLANT MATERIAL= 1 m OF COAL SEAM  In INDIA 30 m seam of coal has been found 450-600 m of plant material might have accumulated at that place. (Taipei 101:509 m tallest building in world)
  • 6. COALIFICATION COAL %C C H O Heating value (MJ/kg) Cellulose 44.5 100 13.9 111 - Wood 50.0 100 12.0 88 19.77 Peat 59.9 100 10.0 57 18.66 Time Lignite 61.8 100 7.8 54 20-25 Brown coal 69.5 100 7.9 36 27.20 Bituminous coal 78.7 100 6.0 21 32.10 Anthracite 91.0 100 4.7 5.2 32.56 Graphite 100 100 0.0 0.0 32.91
  • 7. COAL RANKS 1.Peat: starting point of coal formation does not come in the category of coal Carbon: 60-64%; Oxygen:35-30% 2. Lignites: mark the transition of peat to coal Carbon: 60-75% ; Oxygen: 30-20% Colour: black, brown, earthy Disintegrate very easily Briquetting is done Neyveli Lignite Corporation, Chennai, Tamilnadu Possesses largest reserves of Lignite in India Electricity generation: 2490 MW
  • 8. COAL RANKS contd… 3. Bituminous coals Sub-bituminous: Between lignites and bituminous Carbon: 75-83% ; Oxygen: 20-10% No caking power (Briquettes can not be made) Bituminous: black and banded Industrial and domestic usage Carbon: 75-90%: Oxygen:10-5% Semi-bituminous: Between bituminous and anthracite Metallurgical coke formation Carbon: 90-93%; Oxygen:4-1%
  • 9. COAL RANKS contd… 4. Anthracites Highest rank of coal Extreme of metamorphosis from the original plant material Carbon: 93+%: Oxygen: 2-1% Caking power zero Unusual coals Cannels: found rarely; high hydrogen content: burn with smoke and bright flame; does not fall in any category. Torbanites: fine grained coal, named after Torbane Hill of Scotland, rich in paraffin oil.
  • 10. Unusual Solid Fuel (Methane Clathrate)  Burning Ice  1 mole methane in 5.75 mole H 2O  Available in Deep sea (methane from trench + cold water + high pressure) and at the lower ice layer in Antarctica  It is expected that 15,000 Gt (21×1015 m3) of methane is available in this form (as compared to 1,000 Gt of Coal)
  • 11. WORLD PRODUCTION OF COAL IN YEAR 2006 % of world production Country Million tonnes China 2380 39.75 USA 1053.6 17.59 India 447.3 7.47 Australia 373.8 6.24 South Africa 256.9 4.29 Canada 62.9 1.05 United Kingdom 18.6 0.31 Pakistan 4.3 0.07 Japan 1.3 0.02 Total of the world 5,986.90 100
  • 12. WORLD PRODUCTION OF COAL IN YEAR 2006 Canada United Pakistan South Kingdom Africa Japan Australia India China USA
  • 13. WORLD TOP TEN COAL PRODUCING AND CONSUMING COUNTRIES 1 quadrillion=1000 trillion 1 Btu=1.055 kJ
  • 14. COAL RESERVES OF INDIA (As on 1.1.2007 in billion tonnes) TOTAL PROVED INDICATED INFERRED Type of coal RESERVE RESERVE RESERVE RESERVE COKING 32 17 13 2 NON- 223 81 105 36 COKING TOTAL 255 98 118 38 Years to consume this coal with present rate: 600 Cokes are the solid carbonaceous material derived from destructive distillation of low-ash, low-sulfur bituminous coal. Source: MoC
  • 15. COAL RESOURCES OF STATES Proved: boreholes (1200m deep) @ 400 m IN MILLION TONNES Jan 1, 2007 Indicated & Inferred: boreholes @ 1-2 km State Proved Indicated Inferred Total % of total Jharkhand 36881 31094 6339 74314 29.11 Orissa 17464 30239 14296 61999 24.29 Chhattisgarh 10182 26826 4443 41451 16.24 West Bengal 11454 11810 5071 28335 11.10 Madhya Pradesh 7584 9259 2934 19777 7.75 Andhra Pradesh 8475 6328 2658 17461 6.84 Maharashtra 4856 2822 1992 9670 3.79 Uttar Pradesh 766 296 0 1062 0.42 Meghalaya 118 41 301 460 0.18 Assam 315 27 34 376 0.15 Bihar 0 0 160 160 0.06 Arunachal Pdesh 31 40 19 90 0.04 Sikkim 0 55 18 73 0.03 Nagaland 3 1 15 19 0.01 Total 98129 118838 38280 255247 100
  • 16. GRADING OF INDIAN COAL  Coking coal (carbon: 81-91%)  Non-coking coal Grades of coking coal Grade Industry Ash % I steel <15 II steel 15-18 I washery* 18-21 II washery* 21-24 III washery* 24-28 IV washery* 28-35 * Washed Coal is used as fuel in thermal power plants
  • 17. GRADING OF INDIAN COAL  High ash content (up to 50%)  Lower heating/calorific value  Inferior quality but suitable for power gen. Grades of non-coking coal Grade UHV, kcal/kg Ash % A >6200 <13.56 B 5600-6200 13.56-17.91 C 4940-5600 17.91-22.69 D 4200-4940 22.69-28.06 E 3360-4200 28.06-34.14 F 2400-3360 34.14-41.10 G 1300-2400 41.10-49.07 UHV:Useful Heating Value Based on 6 % moisture content =8900-138×[ash% + moisture%]
  • 18. ROYALTY TO STATES  Nationalization in 1971  Coal companies are paying the royalty to states  This varies from Rs 90-250/tonne  The rate is dependent of coal grade  Rates are 16 August 2002 onwards
  • 19. IMPORT OF COAL Coking and non-coking coals being imported Year Coking Non-coking Total 1991/92 5.27 0.66 5.93 1996/97 10.62 2.56 13.18 2000/01 11.06 9.87 19.70 2003/04 12.99 8.69 21.68 2005/06 16.89 21.70 38.59 2006/07 22.00 23.00 45.00 In million tonnes
  • 20. ANALYSIS OF COAL  Proximate analysis  Ultimate analysis  Heating/calorific value
  • 21. PROXIMATE ANALYSIS 1. Moisture content: 105 -110 oC 2. Volatiles: 925±15 oC for 7 min time (with lid) 3. Fixed carbon: by difference 4. Ash: 800±15 oC (without lid) REPORTING: AS RECEIVED BASIS, MOISTURE FREE BASIS/DRY BASIS OR DRY ASH FREE BASIS IS:1350-I (1984)
  • 22. EXAMPLE OF PA A sample of finely ground coal of mass 0.9945 g was placed in a crucible of 8.5506 g in an oven, maintained at 105 oC for 4.0 ks. The sample was then removed, cooled in a dessicator and reweighed; the procedure being repeated until a constant total mass of 9.5340 g was attained. A second sample, of mass 1.0120 g in a crucible of mass 8.5685 g was heated with a lid in a furnace at 920 oC for 420 s. On cooling and reweighing, the total mass was 9.1921 g. This sample was then heated without a lid in the same furnace maintained at 725 oC until a constant total mass of 8.6255 g was attained. Calculate the proximate analysis of the sample and express the results on “as sampled” and “dry, ash-free” basis.
  • 23. EXAMPLE OF PA contd.. MOISTURE (from first sample) mass of sample = 0.9945 g mass of dry coal = (9.5340-8.5506) = 0.9834 g mass of moisture = (0.9945-0.9834) = 0.0111 g % moisture = 0.0111 × 100/0.9945 = 1.11 % ASH (from second sample) Mass of sample = 1.0120 g Mass of crucible = 8.5685 g Heating up to 920ºC in absence of air removes volatile matters, subsequent heating up to 725ºC in presence of air burns all fixed carbon of the sample leaving behind ash in the crucible. Mass of ash (remnant in crucible) = (8.6255 - 8.5685) = 0.0570 g % ash = 0.0570 × 100/1.0120 = 5.63 %
  • 24. EXAMPLE OF PA contd.. VOLATILE MATTER Initial mass of sample + crucible = 1.0120 + 8.5685 = 9.5805 g Final mass after heating up to 920ºC (without air) = 9.1921 g Mass of volatile matter + moisture = Initial – Final mass = (9.5805-9.1921) g = 0.3884 g % Moisture + Volatiles = 0.3884 x 100/1.0120 = 38.3794 % % VOLATILE MATTER = 38.3794 – 1.11 (% Moisture) = 37.26 % FIXED CARBON % FC = 100 - % VM - % ash - % moisture = 100 – 37.26 - 5.53 - 1.11 = 55.98 %
  • 25. EXAMPLE OF PA contd.. Proximate analysis as received basis Moisture : 1.11 % Ash : 5.63 % Fixed carbon : 55.99 % Volatile matter : 37.26 % Proximate analysis on dry, ash free basis Moisture + ash = 1.11 + 5.63 = 6.74% Fixed carbon: 55.99x100/(100-6.74) = 60.04 % Volatile matter: 37.26x100/(100-6.74) = 39.95 %
  • 26. ULTIMATE ANALYSIS 1. Carbon 2. Hydrogen 3. Oxygen 4. Sulfur :0.5-2.50 % 5. Nitrogen :1.0-2.25 % 6. Phosphorus :0.1%;Blast Furnace: <0.01 % 7. Chlorine Mercury: A big problem from NTPC plants (up to 0.3mg/kg) IS:1350- IV (1974)
  • 27. HEATING VALUE 1. Calculated from proximate analysis 2. Calculated from ultimate analysis 3. Experimental determination 1. Gross/High heating value 2. Useful/low heating value Hydrogen Water (gas/vapor or liquid phase) Carbon Carbon Dioxide (gas phase) Latent heat of vaporization of water: 2.26 MJ/kg
  • 28. HEATING VALUE 1. Calculated from proximate analysis TAYLOR AND PATTERSON RELATIONSHIP HV=4.19 (82FC+ a VM) kJ/kg Where FC and VM are on dry ash free basis and a is an empirical constant which depends on the VM content of coal. 170 160 150 140 130 120 110 100 90 80 0 10 20 30 40 VM 5 10 15 20 25 30 35 38 40 a 145 130 117 109 103 98 94 85 80
  • 29. HEATING VALUE 2. Calculated from ultimate analysis DULONG FORMULA HV=338.2C+1442.8(H-O/8)+94.2S kJ/kg Where C, H, O and S are the % of these elements on dry ash free basis.
  • 30. HEATING VALUE 3. Experimental determination: Bomb calorimeter  solid /liquid samples can be analyzed  1 g air dried sample is burnt in a bomb in oxygen atmosphere  rise in temperature gives the heat liberated and heating value is determined after doing the corrections for resistance wire and thread.  microprocessor based bomb calorimeters are now available IS:1350-II (1970)
  • 32. VARIOUS COMPONENTS OF BOMB CALORIMETERIC EQUIPMENT
  • 33. ROUTES OF GENERATION OF HEAT AND POWER FROM COAL 1. Direct use as thermal energy in heating processes, furnaces and domestic heating by open fires 2. Transfer of the heat to a thermal fluid and application of the latter for heating and power e.g., steam for heating in process industry, central heating and electricity generation by steam turbines 3. Gas turbine route to electricity generation 4. Conversion to gas/liquid fuels and subsequent usage in IC engines/turbines (gas/steam)
  • 34. ROUTE I (Direct Heating)  Domestic cooking (Chula at tea stalls, dhaba, bakery)  Space heating (Fireplace)  Lime and brick kilns (Direct heating of stack)  Ceramic industry (Oven/Furnace)
  • 35. ROUTE II (Thermal Fluid)  Generation of steam in a boiler  Space heating by transferring heat of steam to air  Process industry : Cogeneration is employed  Utility services : steam turbines used SUPERCRITICAL BOILERS: A RECENT CONCEPT Critical pressure: 218 bar (21.8 MPa); Critical temperature: 374oC Mark Benson; in 1922 Patent was granted 22 MPa pressure ; η= 1-T1/T2 ≈ 0.53 GOVERNMENT ALLOWED ELECTRICITY GENERATION BY PRIVATE DEVELOPERS Tariffing Wheeling Banking
  • 36. ROUTE II contd.. Hot air for Heat space Coal Boiler Steam exchanger heating Steam Air Condensate Steam Cogeneration Steam turbine Alternator to grid Alternator Electricity Condensate Steam Steam turbine Electricity to grid Process plant
  • 37. ROUTE III Coal Vent Preheated air Pulverizer Heat exchanger Turbine exhaust Combustion chamber Gas turbine Compressor Alternator Air Electricity to grid
  • 38. ROUTE III Vent Preheated air Heat exchanger Turbine exhaust Combustion chamber Gas turbine Compressor Alternator Coal Air Electricity Gasifier and gas to grid cleaning unit
  • 39. ROUTE IV (Pyrolysis / Gasification) 1. Partial Gasification or Pyrolysis /coking /carbonization / destructive distillation (heating in the absence of air) • Solid • Liquid • Gas 2. Complete gasification with air/oxygen • Gas
  • 40. PYROLYSIS Low temperature carbonization 500-700 oC Coke (solid fuel) maximum; classical domestic smokeless fuel production Medium temperature carbonization 700-900 oC Liquid fraction for chemicals recovery/liquid fuel High temperature carbonization >900 oC Coke for metallurgical furnaces; gas yield high; liquid low
  • 41. PYROLYSIS Coal Pretreatment unit Water in Gas Flue gas for IC engines/ Gas turbines/ Pyrolyser Condenser thermal applications Water out Coke Liquid Coal tar fraction Liquid fuels Chemicals Gas for heating of pyrolyser
  • 42. GASIFICATION 3 1k mole 12x3=36 kg ≈18 Liter =1000.R.T/P (m3) =22.41 Nm3
  • 44.
  • 45. ROUTE IV BERGIUS PROCESS Coal is hydrogen starved/hydrogen needs to be added to make it liquid (directly or indirectly) 1. Bergius process Friedrich Karl Rudolf Bergius (Germany) in 1913, Nobel Prize in 1931 (Shared with Carl Bosch) By end of World war II – most of the fuel for German army was produced by this method. Hydrogenation of vegetable oils 2. Fischer-Tropsch process Franz Fischer and Hans Tropsch in 1926, Germany
  • 46. BERGIUS PROCESS Coal T=400-500 oC Hydrogen P= 20 -70 MPa Catalyst=Tin Conver.=97% Fractionating column Pulverizer HCs Bergius Reactor Coal pasting unit Heavy fraction
  • 47. F-T PROCESS Coal T=150-250 oC P= 1 -25 Mpa Catalysts : Fe, Co Fractionating column Gasification unit HCs F-T Syn gas Reactor Syn gas Cleaning (Large number of patents worldwide)
  • 48. F-T PROCESS (COMMERCIAL PLANTS)  South Africa Oil and Gas Company  1950 established  Oldest plant proving the F-T process viability  Presently engaged in Qatar, Iran and Nigeria in similar projects
  • 51. UNDERGROUND/ IN SITU COAL GASIFICATION A process applied to the non-mined coal seams Injection and production wells are drilled End gas mix depends on type of coal seam Air/ oxygen can be used for gasification Syn gas can be used for power generation in combined cycle Syn gas can be converted to chemicals/fuel by F-T process
  • 52. UNDERGROUND/ IN SITU COAL GASIFICATION Source: World Coal Institute
  • 53. COAL COMBUSTION AND ENVIORNMENT  Global warming  Green house gases: water vapor, carbon dioxide, methane, nitrous oxide, HFCs (hydrofluorocarbons), PFCs (perfluorocarbons), SF6 (Sulphur Hexafluoride)  SF6 is 22, 200 more potential than CO2  Carbon dioxide gas: main culprit from fossil fuels; not from biomass  Intergovernmental Panel on Climate Change (IPCC)  Nobel Peace Prize 2007 : R. K. Pauchari and Al Gore  Reduction in Carbon Dioxide emissions  G8 meeting in Japan in July 2008
  • 54. COAL COMBUSTION AND ENVIORNMENT Present CO2 level:483 PPM Carbon Dioxide Emissions and Carbon Dioxide Concentrations (1751-2004)
  • 55. COAL COMBUSTION AND ENVIORNMENT Global Carbon Cycle (Billion Metric Tons Carbon)
  • 56. COAL COMBUSTION AND ENVIORNMENT U.S. Anthropogenic Greenhouse Gas Emissions by Gas, 2006 (Million Metric Tons of Carbon Dioxide Equivalent)
  • 57. ULTIMATE SOLUTIONS Solar: photovoltaic Fuel cells: Chemical to electrical conversion Hybrid vehicles: Honda introduced in India