CHECAL2
Dr. Susan A. Roces INTRODUCTION
1
Combustion:
 unit process in which oxidation reaction takes place.
 accompanied by evolution of light and heat, and thus the
industries used in the generation of heat to supply energy
to the process industries.
 chemical reaction in which one of the reactants is oxygen
from the air and the other is a fuel (gaseous, liquid, solid).
Air
HC Fuel Stack Gas/Flue Gas
Complete Combustion:
The complete combustion of a fuel means that all of its
combustible components are gasified: all of the carbon is burned
to carbon dioxide, all of the hydrogen is converted to water and
all sulfur to sulfur dioxide.
C + O2 CO2
H2 +
2
1
O2 H2O
S + O2 SO2
The complete combustion of any organic fuel is represented by:
CwHxOySz +
2
1
[ 2w +
2
x
+ 2z - y ]O2
w CO2 +
2
x
H2O + z SO2
CHECAL2
Dr. Susan A. Roces INTRODUCTION
2
Theoretical Oxygen:
 Theoretical oxygen is the oxygen required to be brought
into the process for complete combustion.
 Sometimes this quantity is called the required oxygen.
Two methods in solving theoretical oxygen:
Method 1:
The individual balanced equation for the oxidation of each
combustible is written. The theoretical oxygen is the sum of all
the oxygen used in each complete combustion.
Theo O2 = ∑ (moles)i (Coefficient of O2)i
Example:
Determine the theoretical moles of dry air required for the
combustion of one mole of refinery gases containing 6 % H2S,
5 % H2, 57 % C3H8, 2 % CO2, and 30 % C4H10.
Basis: 1 mole of gaseous fuel
H2S +
2
3
O2 = SO2 + H2O
(0.06)
H2 +
2
1
O2 = H2O
(0.05)
C3H8 + 5 O2 = 3 CO2 + 4H2O
(0.57)
C4H10 +
2
13
O2 = 4 CO2 + 5 H2O
(0.3)
CHECAL2
Dr. Susan A. Roces INTRODUCTION
3
Theoretical O2:
=
2
3
(0.06) +
2
1
(0.05) + 5 (0.57) +
2
13
(0.3) = 4.915
Method 2:
The components of the fuel are broken down into corresponding
atoms of carbon, sulfur, hydrogen and moles of oxygen present.
Note:
1. For complete combustion, each atom C requires 1 mole O2;
each atom sulfur requires 1 mole O2; each atom H requires
1/4 mole O2;
2. The total moles of O2 in the fuel is subtracted from the O2
requirements to give the theoretical O2 from air.
3. The rational behind this is that before any amount of O2 is
taken from the air, the fuel first utilizes the O2 together
with it.
Therefore:
Theo O2 = at C + at S + at
4
H
- moles O2
Solving the above example by Method 2:
Gas Mole At S At C At H Moles O2
H2S 0.06 0.06 - 0.12 -
H2 0.05 - - 0.1 -
C3H8 0.57 - 1.71 4.56 -
CO2 0.02 - 0.02 - 0.02
C4H10 0.30 - 1.2 3.00 -
1.0 0.06 2.93 7.78 0.02
CHECAL2
Dr. Susan A. Roces INTRODUCTION
4
Theo O2 = 2.93 + 0.06 +
4
78.7
- 0.02
= 4.915
Theoretical Air for Combustion:
Theoretical air is air that contains the exact amount of
theoretical O2. Air for combustion calculations is assumed to be
21 % O2 and 79 % N2. N2 in air is non-combustible and acts as
a diluent to the O2 in the air.
Example:
A furnace is fired with petroleum oil containing 80 % C, 13 % H,
3 % S, 1 % N and 3 % O. Determine the moles theoretical air
required for the combustion of one kg of oil.
Basis: 1 kg of fuel oil
Theo O2 =
12
80.0
+
32
03.0
+
4
13.0
-
32
03.0
= 0.09917
kg moles of Theo air =
21.0
09917.0
= 0.4722
Incomplete Combustion:
Incomplete combustion of fuel represents a loss of heat since
this should have been given off for additional power use had the
fuel been completely burnt.
Two obvious phenomenon of incomplete or partial combustion:
1. CO and H2 formation in the flue gas
2. Presence of unburned combustibles in the refuse for solid
fuels.
CHECAL2
Dr. Susan A. Roces INTRODUCTION
5
In actual practice, theoretical air is not sufficient to get complete
combustion.
Excess Air (excess O2):
 Amount of air (excess O2) in excess of that is required for
complete combustion
 Does not depend on how much material is actually burned
but what can be burned.
 The percent excess air is identical to the percent excess O2
Percent Excess Air:
Excess air supply or excess O2 supply is a must for complete
combustion.
Excess O2 = Actual O2 supply - Theo O2
% Excess Air = 100
2
2
x
OlTheoretica
OExcess
= 100
2
22
x
OlTheoretica
OTheoOSupplied 
= 100
22
2
x
OExcessOSupplied
OExcess

The actual Percentage Excess Air depends on the fuel used for
combustion:
 Gaseous fuels require very little excess O2
 Liquid fuels require somewhat more % excess O2 depending
on their characteristics
 Solid fuels require maximum excess O2
CHECAL2
Dr. Susan A. Roces INTRODUCTION
6
If the percent excess air and the chemical equation are specified
in a problem, you will know how much air enters with the fuel.
Flue or stack gas:
All the gases resulting from combustion process including the
water vapor, sometimes known as a wet basis.
Orsat Analysis or dry basis:
 All the gases resulting from a combustion process not
including the water vapor
 Refers to a type of gas analysis apparatus in which the
volumes of the respective gases are measured over and in
equilibrium with water; hence each component is saturated
with water vapor.
Comparison of gas analysis on different bases:
CO2 Dry Flue
CO Gas on Orsat Analysis
Flue Gas O2 Free Dry Basis
Stack Gas N2 SO2 Basis
Wet Basis SO2
H2O

Introduction combustion

  • 1.
    CHECAL2 Dr. Susan A.Roces INTRODUCTION 1 Combustion:  unit process in which oxidation reaction takes place.  accompanied by evolution of light and heat, and thus the industries used in the generation of heat to supply energy to the process industries.  chemical reaction in which one of the reactants is oxygen from the air and the other is a fuel (gaseous, liquid, solid). Air HC Fuel Stack Gas/Flue Gas Complete Combustion: The complete combustion of a fuel means that all of its combustible components are gasified: all of the carbon is burned to carbon dioxide, all of the hydrogen is converted to water and all sulfur to sulfur dioxide. C + O2 CO2 H2 + 2 1 O2 H2O S + O2 SO2 The complete combustion of any organic fuel is represented by: CwHxOySz + 2 1 [ 2w + 2 x + 2z - y ]O2 w CO2 + 2 x H2O + z SO2
  • 2.
    CHECAL2 Dr. Susan A.Roces INTRODUCTION 2 Theoretical Oxygen:  Theoretical oxygen is the oxygen required to be brought into the process for complete combustion.  Sometimes this quantity is called the required oxygen. Two methods in solving theoretical oxygen: Method 1: The individual balanced equation for the oxidation of each combustible is written. The theoretical oxygen is the sum of all the oxygen used in each complete combustion. Theo O2 = ∑ (moles)i (Coefficient of O2)i Example: Determine the theoretical moles of dry air required for the combustion of one mole of refinery gases containing 6 % H2S, 5 % H2, 57 % C3H8, 2 % CO2, and 30 % C4H10. Basis: 1 mole of gaseous fuel H2S + 2 3 O2 = SO2 + H2O (0.06) H2 + 2 1 O2 = H2O (0.05) C3H8 + 5 O2 = 3 CO2 + 4H2O (0.57) C4H10 + 2 13 O2 = 4 CO2 + 5 H2O (0.3)
  • 3.
    CHECAL2 Dr. Susan A.Roces INTRODUCTION 3 Theoretical O2: = 2 3 (0.06) + 2 1 (0.05) + 5 (0.57) + 2 13 (0.3) = 4.915 Method 2: The components of the fuel are broken down into corresponding atoms of carbon, sulfur, hydrogen and moles of oxygen present. Note: 1. For complete combustion, each atom C requires 1 mole O2; each atom sulfur requires 1 mole O2; each atom H requires 1/4 mole O2; 2. The total moles of O2 in the fuel is subtracted from the O2 requirements to give the theoretical O2 from air. 3. The rational behind this is that before any amount of O2 is taken from the air, the fuel first utilizes the O2 together with it. Therefore: Theo O2 = at C + at S + at 4 H - moles O2 Solving the above example by Method 2: Gas Mole At S At C At H Moles O2 H2S 0.06 0.06 - 0.12 - H2 0.05 - - 0.1 - C3H8 0.57 - 1.71 4.56 - CO2 0.02 - 0.02 - 0.02 C4H10 0.30 - 1.2 3.00 - 1.0 0.06 2.93 7.78 0.02
  • 4.
    CHECAL2 Dr. Susan A.Roces INTRODUCTION 4 Theo O2 = 2.93 + 0.06 + 4 78.7 - 0.02 = 4.915 Theoretical Air for Combustion: Theoretical air is air that contains the exact amount of theoretical O2. Air for combustion calculations is assumed to be 21 % O2 and 79 % N2. N2 in air is non-combustible and acts as a diluent to the O2 in the air. Example: A furnace is fired with petroleum oil containing 80 % C, 13 % H, 3 % S, 1 % N and 3 % O. Determine the moles theoretical air required for the combustion of one kg of oil. Basis: 1 kg of fuel oil Theo O2 = 12 80.0 + 32 03.0 + 4 13.0 - 32 03.0 = 0.09917 kg moles of Theo air = 21.0 09917.0 = 0.4722 Incomplete Combustion: Incomplete combustion of fuel represents a loss of heat since this should have been given off for additional power use had the fuel been completely burnt. Two obvious phenomenon of incomplete or partial combustion: 1. CO and H2 formation in the flue gas 2. Presence of unburned combustibles in the refuse for solid fuels.
  • 5.
    CHECAL2 Dr. Susan A.Roces INTRODUCTION 5 In actual practice, theoretical air is not sufficient to get complete combustion. Excess Air (excess O2):  Amount of air (excess O2) in excess of that is required for complete combustion  Does not depend on how much material is actually burned but what can be burned.  The percent excess air is identical to the percent excess O2 Percent Excess Air: Excess air supply or excess O2 supply is a must for complete combustion. Excess O2 = Actual O2 supply - Theo O2 % Excess Air = 100 2 2 x OlTheoretica OExcess = 100 2 22 x OlTheoretica OTheoOSupplied  = 100 22 2 x OExcessOSupplied OExcess  The actual Percentage Excess Air depends on the fuel used for combustion:  Gaseous fuels require very little excess O2  Liquid fuels require somewhat more % excess O2 depending on their characteristics  Solid fuels require maximum excess O2
  • 6.
    CHECAL2 Dr. Susan A.Roces INTRODUCTION 6 If the percent excess air and the chemical equation are specified in a problem, you will know how much air enters with the fuel. Flue or stack gas: All the gases resulting from combustion process including the water vapor, sometimes known as a wet basis. Orsat Analysis or dry basis:  All the gases resulting from a combustion process not including the water vapor  Refers to a type of gas analysis apparatus in which the volumes of the respective gases are measured over and in equilibrium with water; hence each component is saturated with water vapor. Comparison of gas analysis on different bases: CO2 Dry Flue CO Gas on Orsat Analysis Flue Gas O2 Free Dry Basis Stack Gas N2 SO2 Basis Wet Basis SO2 H2O