Hi Pete,
1)
Well, believe it or not, Rocketdyne was actively looking for such
student outreach programs at the time! They were all for us doing
other “types” of programs (such as presentations, simulations, etc.),
just no live demonstrations. The problem, as it was explained to me,
was that Boeing (who then owned Rocketdyne) simply did not want to
expose themselves to that type of a liability (live demonstrations).
Basically, the larger the company, the more likely the lawsuit, and
they didn't think it was worth it for the outreach.
2)
Yes, I endeavored (in my earlier post) to emphasize that the actual
performance would be lower (due to various losses). The flight losses
themselves constitute a major hit (in other words, the drag and
gravity losses), so even with exceptional “engine” performance itself
the delta-V obviously won't get there in the atmosphere – much of it
will be lost to drag and gravity (as I had mentioned earlier), but
that was just a quick check on the ideal.
The other thing is that I was really 'generous' with the mass ratio; I
selected a weight around 100g (a bottle is about 50g, so I simply
doubled it), but with all that bottle reinforcement it could easily be
several times heavier (possibly even 500g or more). Obviously, if
such were the case the ideal delta-V would be far lower. The overall
concept here was simply a rough estimate of potential capability in an
ideal sense.
3)
As I noted in the earlier post, certainly the engine itself is going
to have flow losses and such; they may be significant depending on the
design (but you might be surprised). I didn't include such flow/
discharge coefficients because I wanted to get an idea for the maximum
performance and this was intended just as a quick check on the ideal.
The flow rate was among the most rough estimates since it was a guess
gathered from simply watching the video and observing the water until
it seemed as though the main thrust stopped, which had appeared to be
about 2.5 seconds or so (could have been somewhat more or less). It's
also a guess that the amount of water is ~1L (about 0.5 full); could
be more or less. These are unknowns, and they would obviously affect
the actual figures. Again, just a rough ballpark...
Anyway, 0.4L/s and 100m/s is roughly about A=qdot/v, or ~4mm^2 area,
or ~2.26mm (0.9”) diameter throat, this would be under fairly ideal
conditions and assuming those rough flow rate estimates. The venturi
nozzle (assuming it has a proper entrance cone) might provide a fairly
high discharge coefficient. But in any case, I watched the video
again and the “burn” is perhaps closer to 2s, which increases the flow
rate somewhat and also the nozzle diameter. So, let's say somewhere
between 1.5s and 2.5s (again, could be a bit more or less) and do them
both... Again neglecting a flow coefficient (assuming k=~1) and just
treating qdot=~kAv, 0.0004/100=4e-6 m^2, or about 4mm^2 area... That's
about 2.26mm (0.089”) throat diameter given the first 2.5s estimate.
With the second 1.5s estimate, 0.00067/100=6.7e-6, about 6.7mm^2 area,
or about 2.92mm (0.115”) diameter.
As a secondary check, thrust is about 2*dP*At, linear average delta
pressure is around 793 psi, and via midway expansion around 652 psi.
Selecting the original 2.5s burn, throat is ~0.089” diameter or
0.0062in^2. Thus, original average thrust estimate should somewhere
around 2*(652-14.7)*0.0062=~7.9lbs and 2*(793-14.7)*0.0062=~9.65lbs.
The average estimate at 2.5s burn and 1L was ~9lbs, so this checks.
So, if the flow rate guesses are reasonable, I would surmise that the
throat diameter might be around 0.09” to 0.125” (roughly 2-3mm) given
an ideal case, and the actual perhaps a bit more depending on the
nozzle, it's design, and design exit pressure, but probably not much
more than about 0.15” (~3.8mm) with k=~1. So it's probably somewhere
within that general ballpark, say about 0.12” +/- 0.03” (3mm +/-
0.762mm).
Re hovers around 2.2e5 through the throat section at 100m/s, but by
the time the fluid enters the section, it would have dropped to
roughly atmospheric pressure (via the venturi) based on the nozzle
design assumption used in the rough estimate. I simply used
atmospheric at the exit to roughly approximate the highest reasonable
exit velocity attainable. I didn't notice any extra long throat
sections in the clip, but if there was a desire for an extended throat
pipe, the venturi contraction ratio could be adjusted to account for
added loss (thus slightly larger throat) and/or some pressure recovery
attempted with a relatively shallow expanding exit cone, but most
likely the throat section and exit can probably be made quite short
and give better performance.
Anyway, this is all very rough and depends on the accuracy of all
those quick estimates (like the flow rate, etc.)... if those are
different then the figures will also change. Again, just a quick
check, first pass on the ideal...
4)
Appreciate your positive feedback on my post!
I agree with your assessment on MathML and LaTeX. I've considered
writing (and may write) a tool/plug-in that converts the “typical” way
we tend to convey equations (in common text) into a reasonable
graphical format. Basically, those existing options (at least right
now) rely heavily on the user for formating nearly each aspect, but it
would be nice (and perhaps better) if we could use typical software-
style language conventions (C, for instance) and have the tool
recognize reserved key symbols (like rho, *, etc.). Matrix
representation, etc., could be handled by separate commands if
needed. I'd like to see something such as: for (i=0;i<100;i++) {q
+=someFunc(i);} automatically convert into sigma notation, for
example.
5)
As far as putting up the derivations for N-Prize solutions, you're
correct in that not many teams are providing significant details as to
their chosen direction. But, I think this may have some positive
effects (and some negative effects also). I would like to discuss
this with you more, perhaps in private or on a separate thread; I have
a lot to say on this issue but I'll have to do it a bit later...
~Sage
www.littlemonsterrocket.com
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