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  • Subject Contents

    1. Fuel and Combustion

    2. Steam Generator/ Boiler

    3. Nozzles

    4. Steam Turbines

    5. Gas Turbines

    6. Air Compressors

  • Recommended Books

    i. Applied Thermodynamics for Engineering Technologists

    By: T.D. Eastop & A. McConkey

    ii. Basic Thermodynamics

    By: Reynar Jeol

    iii. Thermodynamics An Engineering Approach

    By: Yunus A. Cengel & M.A. Boles

    iv. Thermodynamics for Engineers

    BY: Bhalchandra V. Karlekar

    Reference Books

    i Text book of Thermal Engineering

    By: R.S. Khurmi

    ii Thermal Engineering

    By: Sarao

  • What is a Fuel ?

    Any material that can be burned to release thermal energy is called a Fuel.

    Most familiar fuels consist primarily of hydrogen and carbon.

    They are called hydrocarbon fuels and are denoted by the general formula CnHm.

    Type of Fuels

    i. Liquid (gasoline)

    ii. Solid (coal)

    iii. Gas (natural gas)

  • Liquid Fuels

    Furnace oil

    Light diesel oil

    Petrol / Gasoline

    Kerosene

    Ethanol

    LSHS (low sulphur heavy stock)

    Liquid Fuels and Calorific value

    Fuel Oil Gross Calorific Value (kCal/kg)

    Kerosene 11,100

    Diesel Oil 10,800

    L.D.O 10,700

    Furnace Oil 10,500

    LSHS 10,600

  • Contamination of Liquid Fuel

    1. Sulphur content:

    1. Depends on source of crude oil and less on the refining process

    2. Furnace oil: 2-4 % sulphur

    Effects: Sulphuric acid causes corrosion

    2. Ash content

    Inorganic material in fuel

    Typically 0.03 - 0.07%

    Effects: Corrosion of burner tips and damage to materials /

    equipments at high temperature

  • 3. Carbon residue

    Tendency of oil to deposit a carbonaceous solid residue on a hot

    surface

    Residual oil: >1% carbon residue

    4. Water content

    Normally low in furnace oil supplied (

  • Solid Fuels

    Coal classification

    Anthracite: hard and geologically the oldest

    Bituminous

    Lignite: soft coal

    Further classification:

    semi- anthracite,

    semi-bituminous, and

    sub-bituminous

  • Physical properties

    Heating or calorific value (GCV)

    Moisture content

    Volatile matter

    Ash

    Chemical properties

    Chemical constituents: carbon, hydrogen, oxygen, sulphur

    Solid Fuel Contents

    1. Moisture content

    0.5 to 10% of moisture in fuel

    Effects:

    Reduces heating value of fuel

    Weight loss from heated and then cooled powdered raw coal

  • 2. Volatile matter

    Methane, hydrocarbons, hydrogen, CO, other

    Typically 25-35%

    Easy ignition with high volatile matter

    Weight loss from heated then cooled crushed coal

    3. Ash

    Impurity that will not burn (5-40%)

    Important for design of furnace

    Ash = residue after combustion

    4. Fixed carbon

    Fixed carbon = 100 (moisture + volatile matter + ash)

    Carbon + hydrogen, oxygen, sulphur, nitrogen residues

    Heat generator during combustion

  • Analysis of Coal

    1. Proximate analysis of coal

    Determines only fixed carbon, volatile matter, moisture and ash

    Useful to find out heating value (GCV)

    Simple analysis equipment

    2. Ultimate analysis of coal

    Determines all coal component elements: carbon, hydrogen,

    oxygen, sulphur, other

    Useful for furnace design

    (e.g flame temperature, flue duct design)

    Laboratory analysis

  • Gaseous Fuels

    Classification of gaseous fuels

    1. Fuels naturally found in natureNatural gasMethane from coal mines

    2. Fuel gases made from solid fuelGases derived from coalGases derived from waste and biomassFrom other industrial processes

    3. Gases made from petroleumLiquefied Petroleum gas (LPG)Refinery gasesGases from oil gasification

    4. Gases from some fermentation

  • Comparing of Fuels

    Constituents Fuel Oil Coal Natural Gas

    Carbon 84 41.11 74

    Hydrogen 12 2.76 25

    Sulphur 3 0.41 -

    Oxygen 1 9.89 Trace

    Nitrogen Trace 1.22 0.75

    Ash Trace 38.63 -

    Water Trace 5.98 -

  • Advantages of Gaseous Fuel

    They are free from all solid and liquid impurities.

    Simplest burners systems

    Burner systems require least maintenance

    Environmental benefits: lowest GHG and other emissions

    They do not produce smoke and ash.

    They undergo complete combustion with minimum air supply.

  • A good fuel should have:

    Low ignition point

    High calorific value

    Freely burn with high efficiency, once it is ignited

    Not produce harmful gases

    Produce least quantity of smoke and gases

    Economical , easy to store and convenient for transportation

  • Calorific Value of FuelsIt is amount of heat given out by complete combustion of one kg of

    fuel, solid, liquid or gas.

    It is expressed in terms of kJ/kg of fuel.

    Types of calorific value

    i. Gross/higher calorific value (H.C.V)

    ii. Net/lower calorific value (L.C.V)

    i. Gross/higher calorific value:

    Total amount of heat produce by one kg of fuel

    ii. Net/lower calorific value:

    Net amount of heat used to produce steam per kg of heat

    L.C.V = H.C.V Heat of steam formed during combustion

  • What is Combustion ?

    A chemical reaction during which a fuel is oxidized and a large quantityof energy/ heat is released is called combustion .

    Necessary Constituents of Combustion:

    i. Fuel

    ii. Supporter of combustion(Air/oxidizer)

    iii. Ignition / kindling temperature

    Ignition temperature for different fuels

    Fuel Ignition Temperature (oC)

    Gasoline / Petrol 260

    Carbon 400

    Hydrogen 580

    Carbon monoxide 610

    Methane 630

  • The oxidizer most often used in combustion processes is air, which is freeand readily available.

    Pure oxygen O2 is used as an oxidizer only in some specialized applications, such as cutting and welding.

    Oxygen is the key to combustion

    Principle of Combustion

  • Composition of Air

  • Types of combustion Process

    1. Complete combustion

    2. Incomplete combustion

    1. Complete Combustion Process

    A combustion process is complete if all the carbon & hydrogen in

    the fuel burns to form, CO2,& H2O.

    All the sulfur (if any) burns to SO2.

    It means, all the combustible components of a fuel are burned tocompletion during a complete combustion process.

  • 2. Incomplete Combustion Process

    The combustion process is incomplete if the combustion products

    contain any unburned fuel or components such as, C, H2, CO, or OH.

    Insufficient oxygen is an obvious reason for incomplete combustion,but it is not the only one.

    Incomplete combustion occurs even when more oxygen is present inthe combustion chamber than is needed for complete combustion.

    Another cause of incomplete combustion is dissociation, which becomes important at high temperatures.(During adiabatic combustion max. Temp. Lower than the calculatedone)

  • Chemical equations are balanced on the basis of the conservation ofmass principle (or the mass balance),

    Stated as follows: The total mass of each element is conservedduring a chemical reaction.

    That is, the total mass of each element on the right-hand side of thereaction equation (the products) must be equal to the total mass ofthat element on the left-hand side (the reactants).

    Even though the elements exist in different chemical compounds in the reactants and products.

    Example:

    2H2 + O2 2H2OReactants Product

  • Theoretical / Stoichiometric Combustion Process

    The ideal combustion process during which a fuel is burnedcompletely with theoretical air(stoichiometric air) is called thestoichiometric or theoretical combustion process.

    For example,

    the theoretical combustion of methane is notice that theproducts of the theoretical combustion contain no unburned

    methane and no C, H2, CO, OH, or free O2.

    Stoichiometric air:

    Minimum mass / volume of air required for completedcombustion of 1kg of fuel is known as Stoichiometric air.

  • Actual combustion process

    In actual combustion processes, it is common practice to use

    more air than the stoichiometric amount to increase the chances

    of complete combustion or to control the temperature of the

    combustion chamber.

  • Excess Air

    The amount of air in excess of the stoichiometric amount is called

    excess air.

    The amount of excess air is usually expressed in terms of thestoichiometric air as percent excess air or percent theoretical air.

    For example,50 percent excess air is equivalent to 150 percent theoretical air,

    200 percent excess air is equivalent to 300 percent theoretical air.

    Deficiency of Air

    Amounts of air less than the stoichiometric amount are called

    deficiency of air and are often expressed as percent deficiency of air. For example, 90 percent theoretical air is equivalent to 10 percent deficiency of

    air.

  • Air-Fuel RatioA frequently used quantity in the analysis of combustion processes

    to quantify the amounts of fuel and air is the airfuel ratio (AF).

    AF represents the amount of air used per unit mass of fuel during acombustion process

    It is usually expressed on a mass basis and is defined as,

    The mass m of a substance is related to the number of moles N through the relation m= NM, where M is the molar mass.

    Example:

    The airfuel ratio can also be expressed on a mole basis as the ratioof the mole numbers of air to the mole numbers of fuel. But we willuse the former definition.

    The reciprocal of airfuel ratio is called the fuelair ratio.

  • Example:One k mol of octane (C8H18) is burned with air that contains 20 kmol of O2.Assuming the products contain only CO2, H2O, O2, and N2, determine themole number of each gas in the products and the airfuel ratio for thiscombustion process. Assume the molar mass of air is 29.0 kg/kmol.

    The chemical equation for this combustion process,

    X, y,z and w represent the unknown mole numbers of the product, theseunknowns are determined by applying the mass balance to each of theelements.

    For Carbon(C): 8 = x x = 8For Hydrogen (H): 18 =2y y = 9For Oxygen (O) 20x2=2x+ y+2z z =7.5For Nitrogen (N2): (20)(3.76) =w w = 75.2

  • Now, substitute the values and yields

    Note that the coefficient 20 in the balanced equation above represents the Number of moles of Oxygen, not the number of moles of air.

    The latter is obtained by

    20x3.76 =75.2 moles of nitrogen to the 20 moles of oxygen.

    Therefore, total moles of air is 95.2

    The air-fuel ratio (AF) is determine by

    AF = 24.2 kg air / kg fuel

    It mean 24.2 kg of air is required to burn each kilogram of fuel during thisCombustion process.

  • Combustion Equations of Solid Fuels

    When carbon burns in sufficient quantity of oxygen and produced carbon dioxide along with large amount of heat.

    C + O2 = CO2+Heat

    1mol + 1mol =1mol

    12kg + 32kg = 44kg

    1kg + 8/3kg = 11/3

    It means that 1kg of carbon requires 8/3 kg of oxygen for its complete combustion and produces 11/3 kg of carbon dioxide gas.

  • If sufficient oxygen is not available, then combustion process is not complete and produces carbon monoxide instead of carbon dioxide.

    2C + O2 = 2CO

    2mol + 1mol =2mol (by volume)

    2x12kg + 2x16kg =2x28kg (by mass)

    1kg + 4/3kg = 7/3

    It means that 1kg of carbon requires 4/3 kg of oxygen and produces 7/3 kg of carbon monoxide.

    If carbon monoxide burn further and produces carbon dioxide

    2CO + O2 = 2CO2

    2mol + 1mol =2mol (by volume)

    2x28kg + 2x16kg =2x44kg (by mass)

    1kg + 4/7kg = 11/7

    It means that 1kg of carbon monoxide requires 4/7 kg of oxygen and

    produces 11/7 kg of carbon dioxide.

  • When sulphur (if any) burns with oxygen and produced sulphur dioxide.

    S + O2 = SO2

    1mol + 1mol =1mol (by volume)

    32kg + 2x16kg = 64kg (by mass)

    1kg + 1kg = 2kg

    It means that 1kg of sulphur requires 1 kg of oxygen for its complete combustion and produces 2 kg of sulphur dioxide gas.

  • Combustion Equations of Gaseous Fuels

    Gaseous fuels are generally measured by volume (m3) than by mass

    When carbon monoxide burns with oxygen and produced carbon dioxide.By Volume:

    2CO + O2 = 2CO2

    2volumes + 1vol =2vol

    2m3 + 1m3 = 2m3

    By mass:

    2CO + O2 = 2CO2

    2x28kg + 1x32kg= 2x44kg

    1kg + 4/7 kg = 11/7kg

    It means that 1kg of carbon monoxide requires 4/7 kg of oxygen and produces 11/7 kg of carbon dioxide gas.

  • When hydrogen burns with oxygen produces:By Volume:

    2H2 + O2 = 2H2O

    2volumes + 1vol =2vol

    2m3 + 1m3 = 2m3

    By mass:

    2H2 + O2 = 2H2O

    2x2kg + 1x32kg= 2x18kg

    1kg + 8 kg = 9 kg

    It means that 1kg hydrogen requires 8 kg of oxygen and produces 9 kg of water or steam.

    For burning of CH4 with O2,

    CH4 + 2O2 =CO2 + 2H2O

    16kg + 2x32kg =44kg + 2x18kg

    1kg + 4 kg = 11/4 kg +9/4kg

  • Now, consider 1kg of a Fuel, which contains C,H and S

    Let, Mass of Carbon = C kg

    Mass of Hydrogen = H kgMass of Sulphur = S kg

    We know that for the complete combustion of fuel requires sufficient Oxygen for constituent element such as,

    1kg Carbon (C) 8/3 kg of Oxygen

    1kg Hydrogen (H) 8 kg of Oxygen

    1kg Sulphur (S) 1 kg of Oxygen

    Therefore, total oxygen required for complete combustion of 1 kg of fuel

    = 8/3 C +8 H2 +1 S kg

    If some quantity of oxygen is already present in the fuel, then

    =[8/3 C +8 H2 + S kg]- O2 kg

  • We know that oxygen is obtained from the atmospheric air for the combustionWhich mainly consists of Nitrogen, Oxygen and negligible quantity ofCarbon dioxide and inert gases (Neon, Argon and Krypton).

    For the calculations these negligible quantities are not considered.Therefore,

    N2 = 77% and O2 = 23% By massN2 = 79% and O2 = 21% By volume

    It is obvious that for obtaining 1kg of oxygen, amount of air req.

    =100/23=4.35kg

    =100/23[(8/3 C+8H2+S)-O2]

  • Example:A fuel has the following composition by mass,Carbon 86%, Hydrogen 11.75% and Oxygen 2.25%.Calculate the theoretical air supply per kg of fuel and the mass ofproducts of combustion per kg of fuel.

    Solution:

    C=0.86 kg, H2 = 0.1175kg, O2 = 0.0225kg

    (i) Theoretical air supply per kgwe know that

    Airtheo = 100/23[(8/3C+8 H2 +S)- O2] kg

    Substitute the values Airtheo = 100/23[(8/3x0.86+8 x0.1175 +0)- 0.0225] kg

    Airtheo = 13.96 14kg

  • (ii) Mass of products of combustion

    We know that,

    C+O2 =CO22H2 + O2 = 2H2O

    We know that 1kg of carbon produces 11/3 kg of carbon dioxide and 1kg of hydrogen produces 9 kg of water.

    Therefore, total mass of the products of combustion,

    =11/3xC+9H2kg

    = 11/3x0.86+9x0.1175= 4.21 kg

  • Example:Calculate the stoichiometric A/F ratio for the combustion of a sample of dry Anthracite of the following composition by massC90% ;H 3%; O2 2.5% ; N1% ; S 0.5% and ash 3%Determine the A/F ratio and the dry and wet analysis of products of combustionBy volume, when 20% excess air is supplied.

    Constituent Mass/kg Combust:Equation

    Oxygen (O2) req./ kg

    Products / kg

    C 0.9 C+O2 CO212kg+32 44 kg

    0.9x 32/12= 2.4kg

    0.9x 44/12 =3.3kg of CO2

    H 0.03 2H2+O2 2H2O1kg + 8kg 9kg

    0.03x8=0.24kg

    0.03x9 =0.27 kg H2O

    O 0.025 0.025kg -0.025kg

    N 0.01 0.01kg N2

    S 0.005 S+O2 SO232kg+32kg=64kg

    0.005x32/32=0.005kg

    0.005x64/32=0.01kg SO2

    Ash 0.03

    Total 1.0 2.62kg

  • From table O2 required per kg of coal =2.62 kg

    Therefore,

    (i) Air required per kg of coal = 2.62/0.233= 11.25kg

    (Assume 23.3% O2 by mass)

    (ii) N2 associated with this air =0.767x11.25 =8.63kg

    Total N2 in product =8.63+0.01=8.64kg

    The stoichiometric A/F ratio = 11.25/1

    For an air supply which is 20% excess

    We know that % excess air = A/F(Actual)- A/F(Stioch)/ A/F (Stioch)

    A/F(Actual)=11.25+20/100x11.25=1.2x11.25

    A/F(Actual)=13.5/1

  • Therefore,

    N2 supplied =0.767x13.5=10.36kg

    O2 supplied =0.233x13.5=3.144kg

    In the products, we have

    N2 =10.36+0.01= 10.37kg

    and excess oxygen

    O2 =3.144-2.62=0.524kg

  • Example:The volumetric analysis of a flue gas is CO214% ,CO 1%, O2 5% and N280%Calculate the flue gas composition by mass. Solution:By volumeCO2= 0.14m

    3 ,CO=0.01m3 , O2 =0.05m3 and N2= 0.8m

    3

    The volumetric analysis may be converted into mass analysis by Completing following table

    Constituent Volume of gas (m3)

    (a)

    Molecular mass

    (b)

    ProportionalMassc=axb

    Mass in/kgd=c/c

    %by massdx100

    CO2 0.14 44 6.16 6.16/30.44=0.202

    20.2%

    CO 0.01 28 0.28 0.28/30.44=0.009

    0.9%

    O2 0.05 32 1.60 1.60/30.44=0.053

    5.3%

    N2 0.80 28 22.40 22.40/30.44=0.736

    73.6%

    Total 1.00 c=30.44 1.00 100

  • The flue gas composition by mass is given in the last column

    CO2=20.2%CO = 0.9%O2 =5.3%

    N2 = 73.6%

  • Example:A flue gas has the following percentage composition by massCO213.3% ,CO 0.95%, O2 8.35% and N277.4%

    Calculate the flue gas composition by volume. Solution:By volumeCO2= 13.3% ,CO=0.95% , O2 = 8.35% and N2= 77.4%The mass analysis may be converted into volumetric analysis by Completingfollowing table

    Constituent % mass analysis

    (a)

    Molecular mass

    (b)

    Proportionalvolumec=a/b

    Volume in (m3)

    d=c/c

    %volumetricdx100

    CO2 13.3 44 13.3/44=0.302

    0.302/3.357=0.090

    9.0

    CO 0.95 28 0.95/28=0.034

    0.034/3.357=0.010

    1.0

    O2 8.35 32 8.35/32=0.261

    0.261/3.357=0.078

    7.8

    N2 77.4 28 77.4/28=2.76

    2.76/3.357=0.822

    82.2

    Total 100.0 c=3.357 1.00 100

  • The flue gas composition by volume is given in the last column

    CO2=9%CO = 1%O2 =7.8%

    N2 = 82.2% Ans