Library / Aerospace / AER-49
Aerospace
Combustor fuel-to-air mass ratio
Mass of fuel burned per mass of air from an energy balance, in the constant-specific-heat model.
- Ref
- AER-49
- Rev
- v1
- Field
- Aerospace
- Result
- f
An energy balance on the combustor sets the fuel needed to raise the gas from Tt3 to Tt4: f·ηb·QLHV + cpa·Tt3 = (1 + f)·cpg·Tt4, which gives f = (cpg Tt4 − cpa Tt3)/(ηb QLHV − cpg Tt4). The specific heats are chosen so that the sensible enthalpies refer to a common datum. For a turbine inlet temperature of 1400 K and a compressor exit of 600 K, f is about 2.3 %.
Mass of fuel burned per mass of air from an energy balance, in the constant-specific-heat model. cpa and cpg are chosen consistently so that sensible enthalpies refer to a common datum. T3 and T4 are total temperatures, ηb is combustion efficiency and Q the fuel lower heating value. Fuel sensible enthalpy and bleed are ignored.
Calculator
- Fuel energy per kg of air, f·ηb·Q975,700 J/kg
- Total temperature rise, Tt4 − Tt3800 K
- Fuel flow for 20 kg/s of air0.4631 kg/s
What drives the result
Each variable is moved across its typical range while the others stay at the values above. The longest bar is the key driver.
- The combustor burns 0.02315 kg of fuel per kg of air (2.315 %) to raise the gas by 800 K, so 0.4631 kg/s of fuel for a 20 kg/s core.
- The air is far leaner than stoichiometric (about 0.068), which is why jet engines carry large excess air for cooling and dilution.
Chart data as tables
Ranked variables
| Variable | Typical range | Lowest result | Highest result | Swing () | Local step | Change in result |
|---|---|---|---|---|---|---|
| Tt4 Combustor exit total temperature | 900 to 2,000 K | 0.009478 | 0.04006 | 0.03058 | +10% | +16.8 % |
| Tt3 Combustor inlet total temperature | 400 to 900 K | 0.01576 | 0.02808 | 0.01232 | +10% | −6.38 % |
| cp,g Specific heat of the hot gas | 1,050 to 1,250 J/(kg·K) | 0.02139 | 0.02847 | 0.007081 | +10% | +16.8 % |
| QLHV Fuel lower heating value | 4e7 to 5e7 J/kg | 0.01981 | 0.02496 | 0.005154 | +10% | −9.4 % |
| ηb Combustion efficiency | 0.9 to 1 | 0.02267 | 0.0253 | 0.002624 | +10% | −9.4 % |
| cp,a Specific heat of the compressed air | 950 to 1,100 J/(kg·K) | 0.02167 | 0.02389 | 0.002217 | +10% | −6.38 % |
Sweep of Combustor exit total temperature
| Combustor exit total temperature (K) | Fuel-to-air ratio |
|---|---|
| 900 | 0.009478 |
| 1,038 | 0.0132 |
| 1,175 | 0.01695 |
| 1,313 | 0.02073 |
| 1,450 | 0.02454 |
| 1,588 | 0.02838 |
| 1,725 | 0.03224 |
| 1,863 | 0.03614 |
| 2,000 | 0.04006 |
Sweep one variable
Variables and how each one contributes
Fuel-to-air ratio
What the equation gives you. Everything else feeds it.
Specific heat of the hot gas
The specific heat of the hot gas, in J/(kg·K). Raises the fuel needed to heat the gas. Raising it by 10 % (to 1,210) moves the result by +16.8 %, from 0.02315 to 0.02705.
Combustor exit total temperature
The combustor exit total temperature, in K. Raises the fuel-air ratio, steeply at high temperatures. Raising it by 10 % (to 1,540) moves the result by +16.8 %, from 0.02315 to 0.02705.
Specific heat of the compressed air
The specific heat of the compressed air, in J/(kg·K). A higher value lowers the fuel needed, since the air carries more sensible enthalpy in. Raising it by 10 % (to 1,100) moves the result by −6.38 %, from 0.02315 to 0.02167.
Combustor inlet total temperature
The combustor inlet total temperature, in K. A hotter inlet air lowers the fuel needed. Raising it by 10 % (to 660) moves the result by −6.38 %, from 0.02315 to 0.02167.
Combustion efficiency
The combustion efficiency. A lower efficiency raises the fuel needed in inverse proportion. Raising it by 10 % (to 1.078) moves the result by −9.4 %, from 0.02315 to 0.02098.
Fuel lower heating value
The fuel lower heating value, in J/kg. A higher heating value lowers the fuel needed. Raising it by 10 % (to 4.73×107) moves the result by −9.4 %, from 0.02315 to 0.02098.
Worked example with the values above
- Heat to be added: cpg Tt4 − cpa Tt3 = 1,540,000 − 600,000 = 940,000 J/kg.
- Available: ηb Q − cpg Tt4 = 4.214×107 − 1,540,000 = 4.06×107 J/kg.
- f = 940,000 / 4.06×107 = 0.0231527 kg fuel/kg air.
Assumptions and limits
- Constant specific heats in each stream, adiabatic components and total-to-total efficiencies.
- Steady operation at one operating point, with no bleed and no leakage unless the page says so.
Common mistakes
- Mixing total and static states.
- Using a total-to-static efficiency where a total-to-total one is needed.
- Forgetting the fuel added to the turbine mass flow.
Statistics and uncertainty
Constant-cp cycle calculations are rough: cp rises from 1005 J/(kg·K) in cold air to about 1150 J/(kg·K) in hot gas, which shifts results by 5 % to 10 %. Component efficiencies from maps are good to 1 % to 2 % at design and worse off design.
Where it is used
- Matching compressors, combustors and turbines and finding fuel flow and power.
- Sizing engines and checking cycle designs.
Maths you need
- Isentropic efficiency: ideal work divided by actual work (or the reverse for a turbine)
- Total temperature: the temperature the gas would reach at rest
- Brayton cycle: compression, heat addition, expansion