AME 514 – Applications
of Combustion - Fall 2006
Final Exam 12/11/2006
Time
allowed: 2 hours. Each problem is worth 25 points. Do any 4 of the 5 problems. You can try all of the problems, but turn
in only 4 to be graded. The exam is open book and notes - use
any reference materials you want, but no laptop computers, Pocket PCs, PDAs or
other devices capable of running excel spreadsheets.
1. Anything goes
Planet
X is identical to earth in every way except that the ambient atmospheric pressure on Planet X is twice
that on earth. The ambient air
temperature is still 300K and the atmospheric composition is still 21% O2
and 79% N2 as they are on earth. How would each of the following be different on Planet
X? In particular, does the
property increase, decrease or remain the same, and if it changes, does it
change by more than, less that or exactly a factor of 2? Explain each in 1 or 2 sentences. Each part is worth 3 points, 1 point
is free, do only 8 of 10 parts.
Cross out or donÕt do the 2 parts you donÕt want graded.
a)
The minimum tube
diameter for which a stoichiometric methane-air flame will propagate without
quenching
b)
The amount of
thermal NO emission in a lean premixed fuel-air flame at equivalence ratio 0.9.
c)
The relative
importance of streamwise wall heat conduction compared to convection in a
microscale counter-current (or Swiss roll) heat exchanger and combustor
(assuming the same combustor size, mixture and mass flow rate on earth and on
X).
d)
The NET power output
of the Berkeley micro Wankel engine
e)
The turbulent
burning velocity (ST) of a stoichiometric fuel-air mixture laminar
flamelet regime (assuming GouldinÕs fractal model of ST is the valid
one, and assume uÕ and LI same on earth and on Planet X).
f)
Liftoff height of a
turbulent round jet (same jet diameter do and mass flow rate as
earth-based jet), assuming the scaling given in the lecture notes is correct.
g)
The thrust of a
steady-flow hypersonic propulsion engine with isentropic inlet and
constant-temperature heat addition until the exit pressure equals the ambient
pressure (corresponding to problem 1c-d on HW #4), assuming same flight Mach
number and inlet area (you donÕt have to do all the calculations, just explain
your result.)
h)
The specific impulse
of a pulsed detonation engine
i)
The minimum tube
diameter for which a polymerization front in a fixed composition of acrylic
acid – ammonium persulfate – water can propagate without quenching
j)
The compression
ratio in an HCCI engine where the rapid reaction (call it ÒignitionÓ ÒknockÓ
ÒexplosionÓ or whatever) occurs.
2.
Advanced fundamental topics – flammability, ignition, pollutant
formation
Ronney
Oil and Gas Co. claims to have invented a new fuel additive, called PDR¨,
which increases the fuel heating value (QR) by 10% but has no effect on any other chemical,
thermodynamic or transport property. Estimate by what percent each of the
following combustion properties would increase or decrease by adding PDR¨
to propane (C3H8) in each of the following cases (i.e. is
there less than 10% change, exactly 10% change, or more than 10% change). In some cases there may be no change at
all. (Again, 3 points per part,
1 part free, but do all parts in this case.)
a)
Flame-front
temperature of a non-premixed C3H8-air flame under
diffusion-controlled burning conditions
b)
Extinction stretch
rate of a premixed C3H8-air flame
c)
The burning velocity
at the downward flammability limit
(SL,lim) of a lean premixed C3H8-air flame in
a large diameter tube.
d)
The burning velocity
at the radiation-induced flammability limit (SL,lim) of a lean premixed C3H8-air
flame with negligible buoyancy effects
e)
The adiabatic flame
ball radius in a stoichiometric premixed C3H8-air mixture
f)
The amount of soot
production in a rich premixed C3H8-air flame at
equivalence ratio 1.4
g)
The amount of soot
production in a nonpremixed laminar C3H8 jet flame
h)
Amount of prompt NO
in the products of a rich premixed C3H8-air flame at
equivalence ratio 1.4, far downstream of the flame where chemical equilibrium
is reached, with N2 added to obtain the same adiabatic flame
temperature as a C3H8-air mixture without PDR¨
additive
3.
Microscale combustion
Consider a linear counter-current heat exchanger and
combustor as described in Lecture 4, slides 42 - 48. The temperature profiles for the reactant gas and product
gas (dividing wall temperature profile is excluded for clarity) are shown in
the attached figures for the special case of no heat loss, no streamwise wall
heat conduction and infinitely fast chemical reaction rates. (This is just a reproduction of the top
figure on page 46.) Below is an
expanded diagram just to help refresh your memory about the meaning of this
plot.

Show
modified temperature profiles for each of the following modifications to this
ideal combustor. Explain each
answer in a few sentences. Do only
4 of 5 parts. Be sure to turn in
page 4 if you do this problem!
(a)
A different fuel
with a much slower reaction rate is used, i.e. the reaction is close to
extinction.
(b)
The walls are
roughened to make the flow turbulent in both the reactant and product streams.
(c)
The dividing wall is made perfectly
non-conducting, so that there is no conduction in either the streamwise (i.e.
parallel to the flow direction) or spanwise (i.e. from products to reactants)
direction.
(d)
The walls are coated
with a high-emissivity material, so that radiative heat transfer between the
center dividing wall and the outer walls increases greatly (but there is still
no radiative or from the gas, and no heat loss to ambient).
(e)
The mass flow
rate is doubled (same mixture composition).
Problem #3. Name
________________________ (Do
only 4 of 5 parts)
|
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|
|
(a) A fuel with slower reaction rate is used |
(b)
The walls are
roughened - turbulent |
|
|
|
|
(c) The dividing wall is non-conducting |
(d) The walls are coated with a high-e material |
|
|
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(e) The mass flow rate is doubled (same mixture
composition) |
Spare in case you mess one up – state which
one youÕre doing here! |
4.
Turbulent combustion (5 points each part)
Consider a turbulent premixed flame in a lean
methane-air mixture whose laminar burning velocity (SL) is 10 cm/s =
0.10 m/s. The integral length
scale of turbulence is 5 cm. Use
the following mixture properties if needed: air density (r) = 1.18 kg/m3, viscosity (n) = 1.5 x 10-5 m2/s, thermal
diffusivity (a) = 2.2 x 10-5
m2/s.
a) What turbulence intensity (uÕ) would be required
to extinguish this flame if extinction occurred according to BradleyÕs
criterion, namely Ka = 0.37 ReL1/2?
b) What would the Kolmogorov length scale be at this
condition?
d) For this stoichiometric mixture, what would the
turbulent burning velocity be?
(Use any model you want that is appropriate for the combustion regime
you decided on in part c).
e) If you used a turbulent jet flow (like that
analyzed in the context of nonpremixed turbulent flames in Lecture 10), what
jet exit diameter (do), exit velocity (Uo) and downstream
distance (x) would provide the required uÕ and LI? (Note that there may be more than one
suitable combination of do, Uo, and x.)
Problem #5 (Hypersonic propulsion) (4 points
each part, 1 point free)

Consider
a simple hypersonic propulsion system at an initial Mach number of 7 that
consists of:
Process 1: Heat addition at constant area from M =
7 to M = 3
Process 2: Isentropic expansion back to Pe
= Pa