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    12/13/2010 Dr P B Dwivedi, NMIMSUniversity, Mumbai

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    CHEMISTRY OF FUELS

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    Fuels: substances which undergo combustion in

    the presence of air to produce a large amount of

    heat that can be used economically for domestic

    and industrial purpose.

    This definition does not include nuclear fuel because

    it cannot be used easily by a common man.

    The various fuels used economically are wood, coal,

    kerosene, petrol, diesel gasoline, coal gas, producer

    gas, water gas, natural gas (LPG) etc.

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    Classifications

    Fuels can be broadly classified by origin as,

    (i)Primary or natural fuels: coal, wood etc

    (ii)Secondary or artificial or derived fuels: petrol, diesel

    On the basis of physical state, as :

    (i) Solid fuels

    (ii) Liquid fuels

    (iii) Gaseous fuels

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    Basis Origin Physical

    State

    Source Natural or primary Artificial or Secondary or

    Derived

    Wood, peat, lignite,

    coal

    Semi coke, charcoal Solid fuels

    Petroleum Petrol, kerosene,

    gas oil, coal tar,

    etc.

    Liquid

    fuels

    Producer gas, coke-

    oven gas, water

    gas, blast furnace

    gas, compressed

    butane gas.

    Gaseous

    fuels

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    Characteristics of Fuels

    The physical properties for which fuels are tested and

    their ideal requirements are listed below :

    (i) Calorific value or specific heat of combustion.(ii) Ignition temperature

    (iii) Flame temperature

    (iv) Flash and Fire point.

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    (v) Aniline point

    (vi) Knocking.

    (vii) Specific gravity

    (viii) Cloud and Pour point

    (ix) Viscosity

    (x) Coke number.

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    The chemical properties include the compositional

    analysis of fuel.

    For solid and liquids fuels :

    (i) Percentage of various elements such as C, H, O,

    N, S, etc.

    (ii) Percentage of moisture

    (iii) Percentage of volatile matter

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    For gaseous fuels :

    (i) Percentage of combustible gases e.g. CO, H2,

    CH4, C2H4, C2H6, C4H10, H2S etc.

    (ii) Percentage of non-combustible gases e.g. N2,

    CO2 etc.

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    Calorific Value

    number of units of heat evolved during complete

    combustion of unit weight of the fuel.

    A British Thermal Unit: the heat required to raisethe temperature of one pound of water from 60r F to

    61r F.

    The Calorie: the heat required to raise the temperatureof one kg of water from 15rC to 16rC.

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    High and Low Calorific Values

    Calorific values are of two types as,

    (i)High or Gross Calorific Value (H.C.V. or G.C.V.)

    (ii)Low or Net Calorific Value (L.C.V. or N.C.V.)

    High calorific value may be defined as, the total

    amount of heat produce when one unit of the fuel has

    been burnt completely and the combustion productshave been cooled to 16rC or 60rF.

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    LCV: is the net heatproduced when unit mass or

    volume of fuel is completely burnt and products are

    allowed to escape.

    Net or lower C.V.= Gross C.V. Latent heat of

    water formed

    Or Gross C.V Mass of hydrogen v 9v Latent heat

    of steam (587 cal/g)

    (Because 1 part by weight of hydrogen produces 9

    parts (1 + 8) by mass of water)

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    The calorific value of fuels (e.g. Coal) is determined

    theoretically by Dulong formula, or I.A. Daviesformula.

    Dulong formula can be expressed as,

    HCV = 1/100 [8,080 C+ 34,500(H- O/8)+ 2240 S]

    Where C = % Carbon, H = % Hydrogen, O = %

    Oxygen, S = % Sulphur

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    Oxygen in fuel (coal) is in combined state as

    water and hence it does not contribute to

    heating value of fuel.

    LCV = [HCV 0.09 H(%) 587] cal/g

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    Sr.

    No.

    Property Solid Fuels Liquid Fuels Gaseous Fuels

    1. Calorific value Low Higher Highest

    2. Specific gravity Highest Medium Lowest

    3. Ignition point High Low Lowest

    4. Efficiency Poor Good Best

    5. Air required for

    combustion

    Large and excess

    of air

    Less excess of air Slight excess of air

    6. Use in I.C. engine Cannot be used Already in use Can be used

    7. Mode of supply Cannot be piped Can be piped Can be piped

    8. Space for storage Large 50% less than

    solid fuel

    Very high space

    9. Relative cost Cheaper Costly More costly than

    other two

    10. Care in storage and

    transport

    Less care required Care is necessary Great care required

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    Sr

    No

    Types

    of Coal

    Moisture

    of Air

    Dried At

    40rC

    C

    %

    H

    %

    O

    %

    Ash

    %

    Calorific

    Value

    (kcal/kg)

    Uses

    1. Peat 25 57 6 35 2 5400 Power generation and

    domestic purpose.

    2. Lignite 20 67 5 20 8 6500 Manufacture of

    producer gas, thermal

    power plants.

    3. Bitumi

    nous

    4 83 5 15 7 8000 For metallurgical

    coke, coal gas, boiler,domestic purpose

    4. Anthra

    cite

    2 92 3 2 3 8600 Boilers, metallurgical

    fuel, domestic

    Classification of Coal

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    Analysis of Coal

    The proximate analysis is easy and quicker and it gives a fair

    idea of the quality of coal.

    The ultimate analysis is essential for calculating heat

    balances in any process for which coal is employed as a fuel.

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    Moisture

    It is determined by heating about one gm. of finely

    powdered coal at 105rC to 110rC for an hour in

    electric oven. The loss in weight is reported as due to

    moisture.

    % Moisture = [loss in wt of sample 100]/wt of coal

    taken

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    Ash

    A known weight of sample is taken in a crucible and

    the coal is burnt completely at 700rC 750rC in

    muffle furnace until a constant weight is obtained.The residue left in the crucible is ash content in coal

    which is calculated as

    % of Ash = [wt of residue left in cruciblev 100]/ wt

    of coal taken

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    Volatile matter

    For determining volatile matter content, a known

    weight of dried sample is taken in a crucible with

    properly fitting lid. It is then heated at9

    50rCs

    20rC

    for exactly seven minutes in previously heated muffle

    furnace. The loss in weight is due to volatile matter

    which is calculated as

    Volatile matter = [loss in wt at 9500C 100]/wt of

    coal sample

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    iv) Fixed carbon :

    % of Fixed carbon = 100 (% of moisture + % of ash +

    % of volatile matter)

    In any good sample of coal, the percentages ofmoisture, ash, volatile matter should be as low as

    possible and thus the percentage of fixed carbon

    should be as high as possible.

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    C + O2 p CO2

    12 parts p 44 parts

    2H2 + O2 p 2H2O

    4 parts p 36 parts

    % of Carbon = [increase in wt of KOH tube 12

    100]/wt of coal taken 44

    % of Hydrogen =[increase in wt of CaCl2 tube 4

    v100]/wt of coal taken 36

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    Nitrogen

    Nitrogen is calculated by Kjehldals Method.

    % N = [vol of acid consumed in neutralizing NH3 N 1.4]/wt

    of coal taken

    % Sulphur: [wt of BaSO4 obtained 32 100]/wt of coal taken

    233

    (v) Oxygen:

    The oxygen is determined indirectly by calculation as

    % of Oxygen = 100 (% of C + % of H + % of N + % of S + %

    of Ash)

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    Bomb Calorimeter

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    Let x = mass in g of fuel taken in crucible

    W = mass of water in calorimeter

    w = water equivalent in g of calorimeter, stirrer, thermometer,

    bomb etc.

    t1 & t2 are initial & final temperatures of water in calorimeter

    L = higher calorific value of fuel in cal/g

    Then heat liberated by buring of fuel = xL

    Heat absorbed by water & apparatus = (W+w)(t2-t1)

    But heat liberated = heat absorbed

    so, xL = (W+w)(t2-t1)

    L = (W+w)(t2-t1)/x cal/g or kcal/kg

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    If H = % of hydrogen in fuel

    9H/100 g = mass of water from 1 g of fuel= 0.09H g

    So heat taken by water in forming steam = 0.09 H

    587 cal

    LCV = HCV - 0.09 H 587 cal/g

    By considering fuse wire correction, acid correction

    & cooling corection

    L = [{(W+w)(t2-t1+ cooling correction)}- {acid +fuse

    correction}]/x cal/g or kcal/kg

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    Combustion

    Combustion is a process in which oxygen from the

    air reacts with the elements or compounds to give

    heat. As the elements or compounds combine in indefinite

    proportions with oxygen, we need to calculate what is

    minimum oxygen or air requiredfor the completecombustion of compounds. The commonly involved

    combustion reactions are :

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    i) C + O2p

    CO2ii) 2H2 + O2p 2H2O OR H2 + (O)p H2O

    iii) S + O2p SO2

    iv) 2CO + O2p 2CO2 OR CO + (O)p

    CO2v) CH4 + 2O2p CO2 + 2H2O

    vi) 2C2H6 + 7O2p 4CO2 + 6H2O

    vii) C2H4 +3O2-p 2CO2 + 2H2O

    viii) 2C2H2 + 5O2p 4CO2 + 2H2O

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    Hint to Solve Problems on Calculation of Quantity of Air

    Required for Combustion of Fuel :

    First write the appropriate chemical reaction with

    oxygen and find their relation between the element or

    compound on weight or volume basis.

    e.g C + O2 p CO2

    (12 gm) + (32 gm)

    2H2 + O2 p 2H2O

    (4 gm) + (32 gm)S + O2 p SO2

    (32 gm) + (32 gm)

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    2) Calculate the oxygen required on the basis of unit quantity of

    fuel.

    3) Calculate the total oxygen required for the combustion and

    subtract the oxygen which is present in the fuel.

    4) The oxygen calculated should be converted into air byknowing that air contains 23 parts by weight of oxygen OR 21

    parts by volume of oxygen.

    5) The average molecular weight of air is 28.94 gm.

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    Weight of

    elements per kg.

    of coal

    Weight of O2 required

    for complete combustion

    in kg.

    C = 0.85 0.85 v32/12 = 2.26 kg.

    H = 0.1 0.1 v 8 = 0.8 kg.

    O = 0.05

    Total oxygen = 3.06 kg.

    Weight of oxygen required

    = Weight of oxygen needed weight of oxygen present

    = 3.06 0.05 = 3.01

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    @ Air required for complete combustion

    = 3.01 v 100/23

    = 13.08 kg. per 1 kg. coal.

    @ Air required for 5 kg. of coal

    = 13.08 v 5 = 65.40 kg.

    Volume of Air@ 28.94 kg. of air = 22,400 ml volume at NTP

    @65.4 kg. of air =22400 65.4/ 28.94

    =50815.8 ml. Air

    =50.8158 litres of air