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8.2 · Calculate theoretical air and excess-air fractions
Learn to calculate theoretical air and excess-air fractions through clear examples and targeted practice.
University of Alberta MEC E 340: Applied Thermodynamics
Chemical Reactions and Combustion
A stoichiometric method for introductory combustion calculations
Consider a steady-flow combustion control volume: fuel and air enter, and combustion products leave. The working substances are the fuel, dry air, and product gases. We label the inlet fuel and air as streams 1 and 2, and the outlet products as stream 3; these labels identify streams, not thermodynamic states. Assume complete combustion, so carbon forms carbon dioxide and hydrogen forms water. For the basic calculations here, treat fuel and air amounts on a molar basis, and model dry air as 21 mol% oxygen and 79 mol% nitrogen. The first-law background is not needed to find theoretical air: the key tool is conservation of atoms. The result is a minimum air requirement for complete combustion under the stated assumptions, not a prediction of how well a real burner mixes or burns.
What you will learn
- Set a fuel basis and balance a complete-combustion reaction.
- Calculate the theoretical oxygen and dry air required for complete combustion.
- Determine actual air supplied and express excess air as a fraction or percentage.
- Check air–fuel calculations using atom balances and clear units.
1. Set the basis and balance complete combustion
A calculation needs a stated basis, such as 1 kmol of fuel. For a gaseous fuel written as , complete combustion sends the carbon to and the hydrogen to . First count the oxygen atoms needed in those products. Carbon requires kmol of oxygen atoms in carbon dioxide; hydrogen requires kmol of oxygen atoms in water. Because each oxygen molecule supplies two oxygen atoms, the oxygen demand is half the total product oxygen-atom count.
The air accompanying that oxygen also brings nitrogen. In this lesson, nitrogen is treated as inert: it passes through the reaction without reacting. The dry-air model gives a nitrogen-to-oxygen molar ratio of , approximately . Include this nitrogen on the product side when writing the reaction, even though it does not affect the oxygen balance.
For a fuel with oxygen already in its formula, count that oxygen as part of the available oxygen before finding the oxygen required from air. For a general fuel containing carbon, hydrogen, and oxygen, written as , the oxygen required from air is kmol per kmol of fuel, provided this value is nonnegative and complete combustion is assumed.
- Choose and state a fuel basis before calculating.
- Balance carbon and hydrogen into and , then balance oxygen.
- Use the stated dry-air composition; do not count air nitrogen as oxygen.
2. Convert oxygen demand to theoretical air
Theoretical air is the exact air amount that supplies the stoichiometric oxygen requirement for complete combustion under the chosen reaction model. It is not a separate kind of air; it is a calculated minimum. With dry air containing 21 mol% oxygen, each kmol of oxygen is accompanied by kmol of nitrogen. Thus, the theoretical air amount per kmol of fuel is the theoretical oxygen amount divided by 0.21.
For a hydrocarbon, the balanced idealized reaction is fuel plus theoretical oxygen and its accompanying nitrogen, producing carbon dioxide, water, and unchanged nitrogen. This reaction is a mole balance. It does not say that the products are at a particular temperature, pressure, or phase. No property-table values are required to calculate the air requirement.
Keep the basis visible in your answer. For example, report kmol dry air per kmol fuel, or kg dry air per kg fuel if you have the required molar masses and convert consistently. Do not mix a molar oxygen demand with a mass-based air–fuel ratio without converting units.
- Theoretical air is based on the oxygen needed for complete combustion.
- The air amount depends on the assumed oxygen fraction in air.
- A molar air–fuel ratio and a mass air–fuel ratio are different quantities.
3. Measure actual air and excess air
When actual air is supplied in excess of the theoretical requirement, the extra amount is measured relative to theoretical air. Use the same fuel basis and the same units for both air quantities. The excess-air fraction is dimensionless; multiplying it by 100 expresses excess air as a percentage.
A related phrase is “percent theoretical air.” It compares actual air supplied with theoretical air. For example, 120% theoretical air means the actual supply is 1.20 times the theoretical amount, which corresponds to 20% excess air. This distinction prevents the common mistake of reporting 120% excess air for a supply that is only 120% of theoretical.
If the actual amount is below theoretical, the computed excess-air fraction is negative. That result means a deficiency of air relative to the complete-combustion requirement; it does not justify calling the negative value a positive excess-air percentage. Whether combustion is incomplete then depends on actual conditions and is outside the complete-combustion model used for the theoretical requirement.
- Compare actual and theoretical air on identical bases.
- Excess-air fraction uses theoretical air in the denominator.
- State whether a result is a fraction, a percentage, or percent theoretical air.
4. A reliable calculation and its checks
For each problem, list the fuel formula and amount, the air composition, and the actual-air information supplied. Choose a basis, balance the reaction for theoretical oxygen, and convert oxygen to theoretical air. Then use the problem’s actual-air amount to calculate the excess-air fraction. If the problem gives percent theoretical air instead, divide that percentage by 100 to find the actual-to-theoretical ratio before calculating excess air.
Check the result in two ways. First, verify that the theoretical reaction balances carbon, hydrogen, and oxygen; nitrogen must also be carried through consistently. Second, test the comparison: actual air equal to theoretical air gives zero excess, while actual air greater than theoretical air gives a positive fraction. A result must also retain consistent units and fuel basis.
These are material-balance calculations. The first-law energy balance would be needed for quantities such as heat transfer or product temperature, but it is not required to determine theoretical air or the excess-air fraction from air-supply data.
- Balance atoms before comparing actual with theoretical air.
- Use one consistent fuel basis and one consistent air basis.
- Do not infer product temperature or combustion performance from excess air alone.
Worked example
Theoretical air for methane
Find the theoretical oxygen and dry-air requirements for 1 kmol of methane. Use dry air as 21 mol% oxygen and 79 mol% nitrogen.
- Choose the basisUse 1 kmol of fuel, so all calculated amounts are per kmol of methane. Assume complete combustion and the stated dry-air composition.
- Balance the reactionOne carbon atom forms one carbon dioxide molecule, and four hydrogen atoms form two water molecules. These products need four oxygen atoms, or two oxygen molecules.
- Find theoretical airFor each kmol of oxygen, the dry air contains kmol of nitrogen. Divide the oxygen requirement by the oxygen mole fraction to obtain total theoretical air.
Answer: Theoretical oxygen is 2.00 kmol per kmol . Theoretical dry air is 9.52 kmol air per kmol .
Check: The reaction has 1 carbon atom and 4 hydrogen atoms on each side. Its 2 kmol of oxygen supplies the 4 oxygen atoms in the products. The air amount is greater than the oxygen amount because air is only 21 mol% oxygen.
Worked example
Excess air for propane
Propane is burned with 30.0 kmol of dry air per kmol of fuel. Calculate theoretical air and the excess-air fraction and percentage. Use complete combustion and dry air containing 21 mol% oxygen.
- Balance complete combustionOn a 1 kmol propane basis, three carbon atoms form three carbon dioxide molecules and eight hydrogen atoms form four water molecules. The products require ten oxygen atoms, or five oxygen molecules.
- Calculate theoretical airThe given dry-air oxygen fraction converts the 5 kmol oxygen requirement to the theoretical air supply.
- Compare actual and theoretical airBoth air amounts are on the same basis. Subtract the theoretical amount from the actual amount and divide by theoretical air; multiply by 100 to report a percentage.
Answer: Theoretical air is 23.81 kmol per kmol propane. The excess-air fraction is 0.260, or 26.0%.
Check: Actual air exceeds theoretical air, so a positive result is appropriate. The supplied amount is about 126% of theoretical, consistent with about 26% excess air.
Worked example
Convert percent theoretical air to excess-air fraction
A fuel requires 8.00 kmol theoretical dry air per kmol fuel. The actual supply is 115% theoretical air. Find actual air and the excess-air fraction.
- Interpret the percentage115% theoretical means actual air is 1.15 times the theoretical amount. The excess is the amount above 100% theoretical, not 115% of theoretical.
- Find actual airMultiply the given theoretical air by the actual-to-theoretical ratio, keeping the same fuel basis.
- Calculate excess airThe actual amount is 1.20 kmol above theoretical. Dividing that difference by theoretical air gives the dimensionless excess-air fraction.
Answer: Actual air is 9.20 kmol per kmol fuel. The excess-air fraction is 0.150, or 15.0%.
Check: The answer is consistent because 115% theoretical air equals 100% theoretical plus 15% excess air.
Common mistakes and how to avoid them
Calling actual air equal to 120% of theoretical “120% excess air.”
Correction: It is 20% excess air, because the excess is only the amount above the theoretical requirement.
Using the oxygen amount as though it were the total air amount.
Correction: Divide theoretical oxygen by the oxygen mole fraction in air to obtain theoretical air.
Changing the fuel basis between theoretical and actual air calculations.
Correction: Compare air amounts on the same fuel basis and in the same units.
Leaving nitrogen out of the balanced reaction.
Correction: Carry the nitrogen accompanying air through as an inert product, even though it does not supply oxygen.
Lesson summary
- Balance complete combustion to find theoretical oxygen demand.
- Convert oxygen demand to air using the stated oxygen fraction in dry air.
- Calculate excess-air fraction as actual air minus theoretical air, divided by theoretical air.
- Percent theoretical air equals 100% plus excess-air percentage when actual air exceeds theoretical.
Check your understanding
Question 1
A fuel needs 10.0 kmol theoretical air per kmol fuel and receives 12.5 kmol. What is its excess-air fraction?
- 0.250, or 25.0%
- 0.200, or 20.0%
- 1.25, or 125%
- 0.800, or 80.0%
Show answer and explanation
0.250, or 25.0%
The excess is 2.5 kmol air per kmol fuel. Dividing by the theoretical amount gives 2.5/10.0 = 0.250, or 25.0%.
Question 2
A burner receives 90% theoretical air. What is the excess-air fraction?
- 0.10
- -0.10
- 0.90
- -0.90
Show answer and explanation
-0.10
The actual-to-theoretical ratio is 0.90, so the excess-air fraction is 0.90 - 1.00 = -0.10. This indicates an air deficiency, not positive excess air.
Question 3
For a fuel requiring 3.00 kmol oxygen per kmol fuel, what theoretical dry-air amount follows from an air oxygen fraction of 0.21?
- 0.630 kmol air per kmol fuel
- 3.00 kmol air per kmol fuel
- 14.29 kmol air per kmol fuel
- 63.0 kmol air per kmol fuel
Show answer and explanation
14.29 kmol air per kmol fuel
The theoretical air amount is 3.00/0.21 = 14.29 kmol air per kmol fuel.
Key terms
- Theoretical air
- The amount of air that supplies the stoichiometric oxygen required for complete combustion under stated assumptions.
- Excess-air fraction
- The difference between actual and theoretical air divided by theoretical air.
- Percent theoretical air
- Actual air expressed as a percentage of theoretical air.
- Complete combustion
- The idealized model in which fuel carbon forms carbon dioxide and fuel hydrogen forms water.
Continue through MEC E 340
- 8.1 · Balance complete combustion with air
- 8.3 · Use formation enthalpies in reaction energy balances
- 8.4 · Distinguish higher and lower heating values
- 8.5 · Estimate adiabatic flame temperature under stated assumptions
- 1.1 · Define the system, working fluid, state, and process
- 1.2 · Read property tables and identify phase regions
About this lesson and its review
Published by DoAssignment. This AI-assisted lesson follows University of Alberta MEC E 340: Applied Thermodynamics, study topic 8.2. It is a study resource, not an official curriculum publication.
Before publication, the draft is checked for structure, mathematical or chemical notation, calculations, course boundaries, and readability, and then requires administrator approval. Errors can still occur, so corrections are welcomed.