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MAE 5310: COMBUSTION FUNDAMENTALS

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Known Stoichiometry 1st Law (Energy Balance) Adiabatic Flame Temperature. Problems 1-4. Known P and T 2nd Law (Equilibrium Relations) Stoichiometry. Problems 5-9 ... – PowerPoint PPT presentation

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Title: MAE 5310: COMBUSTION FUNDAMENTALS


1
MAE 5310 COMBUSTION FUNDAMENTALS
  • Lecture 7 Adiabatic Combustion Equilibrium
    Examples
  • September 8, 2009
  • Mechanical and Aerospace Engineering Department
  • Florida Institute of Technology
  • D. R. Kirk

2
ADIABATIC COMBUSTION EQUILIBRIUM
  • Previously we have considered
  • Known Stoichiometry 1st Law (Energy Balance) ?
    Adiabatic Flame Temperature
  • Problems 1-4
  • Known P and T 2nd Law (Equilibrium Relations) ?
    Stoichiometry
  • Problems 5-9
  • Now we can combine these
  • 1st Law (Energy Balance) 2nd Law (Equilibrium
    Relations) ? Adiabatic Flame Temperature
    Stoichiometry
  • Problems 10-14
  • Solution Scheme
  • Guess a TTguess
  • Do equilibrium calculation to solve for species
    concentrations at Tguess
  • Plug into 1st Law
  • We want F(Tguess)0
  • If F(Tguess) gt 0, then initial guess was too high
  • If F(Tguess) lt 0, then initial guess was too low
  • Increment Tguess

3
PRACTICAL APPLICATION RECUPERATION
  • A recuperator is a heat exchanger in which energy
    from a steady flow of hot combustion products,
    called flue gases, is transferred to the air
    supplied to the combustion process

4
SOME COMMON TYPES OF RECUPERATORShttp//www.hardt
ech.es/hgg_tt_hrt.0.html
Tubes cage radiation recuperator
Tubes cage radiation recuperator working at
1,200ºC
Double shell radiation recuperator
Installation consisting of a tubes cage
recuperator and a double shell one, series-connect
ed
5
EXAMPLE RECUPERATION (TURNS)
  • A recuperator, as shown in figure, is employed
    in a natural-gas-fired heating-treating furnace.
    The furnace operates at atmospheric pressure with
    an equivalence ratio of 0.9. The fuel gas enters
    the burner at 298 K, while the air is pre-heated.
  • Determine the effect of air preheat on the
    adiabatic flame temperature of the flame zone for
    a range of inlet air temperatures from 298 K to
    1,000 K.
  • What fuel savings result from preheating the air
    from 298 K to 600 K? Assume that temperature of
    flue gases at furnace exit, prior to entering
    recuperator, is 1700 K, both with and without
    preheat.

Radiant-tube burner with coupled Recuperator for
indirect firing. Note that All flue gases pass
through the recuperator Source Turns, An
Introduction to Combustion
6
STANJAN PRACTICE PROBLEM
  • Consider combustion of a methane-air mixture at
    10 atm (both fuel and air are at 10 atm).
  • Plot mole fractions, ci, for the species CO2, CO,
    H2O, H2, OH, O2, N2, NO vs. temperature for f1
    for a temperature range from 1000 to 2500 K.
  • Calculate Tflame and mole fractions as a function
    of f for adiabatic combustion. Plot these results
    vs. f and discuss at what value the peak flame
    temperature occurs. Comment on this value in
    light of the discussion found in Chapter 1, Part
    2 of Glassman.
  • Compare Tflame from part (2) to what would be
    obtained assuming complete oxidation (burning in
    only oxygen) and what would be obtained assuming
    complete combustion (burning in air).
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