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Grex > Agora46 > #228: The world's most powerful diesel engine | |
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| 25 new of 49 responses total. |
russ
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response 25 of 49:
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Sep 23 00:41 UTC 2003 |
Re #23: The problem with that analysis is that it doesn't
reflect the fact that k (the ratio of the constant-pressure
specific heat to the constant-volume specific heat, for those
still interested) is quite a bit lower in the combustion gases
than in the air charge. Gasoline-engine exhaust has k of about
1.27, according to an Allied-Garrett engineer I quizzed once.
What this means in practice is that the same expansion of gases
does not lower their temperature as much as it heated the air
charge, so you're left with lots of heat to discard.
As an example, if you assume a constant k of 1.4 (not a good
assumption, but not bad for argument) and compress air at
100 kPa and 300 K by 20:1 in volume, you'd get air at 994 K
and about 6.66 MPa (megapascals, about 66 atmospheres).
Now burn fuel sufficient to heat the gas to 2000 K and reduce
k to 1.30. If we assume the same number of molecules of gas,
the pressure rises to 13.4 MPa. An expansion of 20:1 reduces
the temperature by a factor of 2.46, not the 3.3 times it was
heated; temperature falls to 814 K and pressure to 271 kPa.
Even a further isentropic expansion to 100 kPa only cuts the
temperature to 646 K; that's mighty warm exhaust, and every
bit of heat in the exhaust is heat not converted to work.
A real engine will have heat losses and friction losses too.
That's one of the reasons why you can't get 100% efficiency in
a combustion engine, no matter what you do. The 100 MPG
carburetor is a myth for solid thermodynamic reasons.
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gull
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response 26 of 49:
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Sep 23 14:09 UTC 2003 |
Re #19: Good question. My guess is either compressed air or a smaller
"pony" engine, but I'm not sure. I remember finding a page once about
marine diesel technology but I can't locate it now.
Re #21: My guess is that the reason you don't see ceramics used instead
of piston cooling is that the marine engine market is probably pretty
conservative. A single engine like this is often used to drive a
container ship, with no redundancy. Reliability and long life are the
most important design criteria.
Ceramics aren't even showing up in car engines yet, as far as I know.
In fact, many automotive turbodiesels oil-cool their pistons.
Re #22: Fuel cost may be an issue. Marine diesels run on what's
varyingly called "marine residual fuel" or "bunker oil". It's a very
heavy fuel oil (the gel point is as high as 70F for summer grades) and
is very cheap to produce, because it's essentially leftovers from the
refining process. Turbine engines usually burn lighter fuels, like
kerosine or automotive diesel, which would be more expensive. A turbine
design is going to be far more complex, as well -- you need reduction
gearboxes (which run at high input speeds, raising reliability issues
again), and since turbines can't run backwards you need some kind of
reversing gear to drive the ship aft. By comparison, a low-speed diesel
can drive a prop directly. Finally, turbines only run efficiently at
full output; you can't throttle them back without substantial losses.
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gull
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response 27 of 49:
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Sep 23 14:14 UTC 2003 |
I've found a couple references to compressed air being used to start
engines like this. Pressurized air is admitted into the cylinders,
timed to force the engine to rotate in the proper direction.
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russ
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response 28 of 49:
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Oct 5 04:59 UTC 2003 |
For those who are still interested in this, the manufacturer's
web site is http://www.wartsila.com.
It's pretty dry and doesn't have any of the more interesting
(to a geek/gearhead) technical details, but it's there.
I'm still looking for details on things like compression
ratios, intake and exhaust pressures, inlet temperatures...
At least I've found that it does start using compressed
air. (30 bar, it says. 1.5 megabytes of PDF to get that.)
And the exhaust temperature of their "flex" engine is so
low, I don't want to believe it: 285 degrees C. (Where
does the excess heat go? Out the cooling jacket?)
I'm wondering how well this 50%-efficient engine could be
operated on powdered coal, a la the University of Alaska
at Fairbanks cogeneration system.
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gull
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response 29 of 49:
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Oct 5 21:36 UTC 2003 |
I don't find that EGT too unbelievable, especially if it's measured
after the turbocharger. For automotive diesels, a pre-turbo EGT of
1300F is considered the edge of the danger zone, and that corresponds to
about 700 degrees C. The turbocharger takes energy out of the exhaust
so post-turbo EGTs in automotive engines are usually a couple hundred
degrees cooler than pre-turbo temperatures. EGT goes up as you add more
fuel, too, so how surprising that 285C figure is depends on the power
setting.
I'm pretty curious about the compression ratio and how much boost
they're running.
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russ
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response 30 of 49:
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Oct 6 03:12 UTC 2003 |
It was my impression that auto turbos could run at TITs of
1800 F. Don't the silicon nitride turbines run even hotter?
While digging deeper in the brochures from Wartsila, I found
that the figures I was looking at were for the flex-fuel
engine (fuel oil or natural gas). This engine runs at a
fuel-air equivalence ratio of about 0.45, or way, way lean.
(They do this for NOx control.) It no longer surprises me
that the exhaust is so cool.
The thermal efficiency of the 96C series attracts me, though.
It gets roughly 50%, and that is without using features like
insulated heads and piston crowns. (According to an article
on a Caterpillar engine I read some time ago, an adiabatic
engine actually loses output from the lower volumetric
efficiency of the hot cylinder surfaces, but can make it up
due to the greater heat output through the exhaust which is
available to run a compounding turbine.
U of Alaska-Fairbanks is running a coal-burning diesel
cogenerator to heat and power the campus. They expect to
run 41% efficiency to start, perhaps 48% once everything
is tuned to perfection. Our typical steam powerplants run
closer to 30% efficiency, perhaps 33%. If we could replace
them with diesels at 50% efficiency, that is 2/3 the coal
for the same useful energy. If we can use better technology
to boost efficiency to 60% (turbocompounding and a steam
boiler to run a bottoming cycle might get that much), that
is roughly half the coal for the same output. Half the coal
is half the carbon dioxide, among other things.
NOx is not a problem for stationary powerplants. It is
easily reduced to N2 using a bit of ammonia and a catalyst.
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gull
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response 31 of 49:
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Oct 6 13:25 UTC 2003 |
Re #30: A TIT of 1800F is probably possible in gasoline engines for
short periods of time. In diesels, though, there's very little
afterburning going on so the EGT is pretty directly linked to the
combustion chamber temperatures -- so it becomes a bad idea to exceed
the melting temperature of any of the engine components. (Some engines
use aluminum pistons, so even 1300F would be too high.) Plus high EGTs
cause all kinds of wear issues -- it's not uncommon for the exhaust
manifolds of turbocharged gas engines to glow cherry red under heavy
load, and it's also not uncommon for those manifolds to crack and break
up from thermal stresses.
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russ
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response 32 of 49:
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Oct 8 02:18 UTC 2003 |
If you've ever seen a dyno stand at an auto company, you'd know
that it doesn't take a turbo to have the manifolds and a fair
amount of the exhaust plumbing at a glow from dull red to orange.
And there's no air injected in the manifolds, so "afterburning"
has nothing to do with it; it's just metal that's exposed to
the exhaust flow and has neither insulation nor active cooling.
The combustion gases in any car engine are far hotter than
the melting point of iron, let alone aluminum. But that's
neither here nor there.
I take it that the potential of this diesel technology for
solving other problems doesn't interest you that much? I
find it fascinating for stationary powerplants; among other
things, it should be possible to start and stop one of
these engines in less than a minute, perhaps only seconds.
When you compare with the very long ramp up/ramp down times
for many steam powerplants, and the reasons why it took
Michigan so long to get back on the grid after 8/14, the
advantages are obvious to me.
One problem with burning coal is the mercury content. I did
some research on-line but nothing popped out with the usual
mineral form of mercury as present in coal, although I did
find a mention that coal washing can reduce it. Of course,
reducing the amount of coal used reduces the mercury too.
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rcurl
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response 33 of 49:
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Oct 8 02:51 UTC 2003 |
Almost all the work on mercury from coal concerns its speciation in the
gas phase and fly ash. However one would expect HgS to be a common mercury
species in coal because of its very low solubility.
Another problem with burning coal directly in a diesel engine is
solids handling and erosion from abrasive combustion products.
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gull
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response 34 of 49:
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Oct 8 14:46 UTC 2003 |
Re #32: It's an interesting idea, but I think gas turbines have higher
efficiencies when used for power generation. The throttling and
gear-reduction issues aren't as important in a stationary application.
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russ
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response 35 of 49:
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Oct 9 00:52 UTC 2003 |
Now I wish that the site I found on the Wabash River powerplant
in Terre Haute had mentioned something about mercury removal.
It recovers sulfer as H2S and reduces it to the element, but
not a word about Hg.
The problems with abrasion caused by coal ash appear to be
soluble; the Fairbanks powerplant seems to have no show-stoppers.
The thing I'd worry about is ash fusion and buildup of slag
inside the engine.
Oh, another advantage struck me: coal-burning diesels would be
the ideal counterpart to large wind farms, because they could
be started and throttled very easily as the wind changed.
Do you know any decent (free) combustion/engine simulation
packages that run on Linux? I've been wanting to try some
of these concepts but the lack of a good model always tossed
me back to square one (I tried to model an engine in a
spreadsheet once, and gave up on the model when it gave me
an efficiency of greater than 100% and I couldn't find the bug).
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russ
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response 36 of 49:
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Oct 9 02:23 UTC 2003 |
Re #34: Gas turbines fueled by what, though? The Wabash River
plant is a coal-fired, integrated-gasifier combined-cycle plant
and just barely hits 40% efficiency overall. That's not much
better than a typical steam plant at 33%; if you can use a
diesel topping cycle to boost that past 50% you've got a big win.
If you think about it (and work the thermo), the gas turbine is
at a disadvantage because it does not do the combustion in a
(nearly) constant volume. The entropy of an ideal gas is
proportional to the log of the specific volume, and the gas
turbine gets nothing from that expansion in its combustion
systems. The diesel can harness the pressure increase and
turn more of the heat into work.
If I had a decent thermodynamic model I'd try to get the work
available from a more-complete-expansion cycle, perhaps with
a tuned exhaust system to maintain the turbine inlet at a
higher pressure than the turbocompressor. I'd like to have
a better idea of the possibilities than I've been able to
get thus far, but with the lousy info I've got I can't be
sure that my calculations relate usefully to reality.
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rcurl
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response 37 of 49:
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Oct 9 06:00 UTC 2003 |
Minor point - one must oxidize, not reduce, sulfur as H2S, to obtain
elemental sulfur.
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russ
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response 38 of 49:
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Oct 10 03:05 UTC 2003 |
I knew that mercuric sulfide was not very soluble (I found
it was used as a tatoo pigment), but I can't believe I
mis-spelled "sulfur". I've tried finding the reaction used
to convert H2S to pure sulfur, without success; I wonder if
it yields anything useful, like H2.
No suggestions for engine simulations?
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rcurl
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response 39 of 49:
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Oct 10 04:27 UTC 2003 |
The H2S is oxidized partially to SO2, which then reacts with the remaining
H2S by the disproportionation
2H2S + SO2 = 2H2O + 3S
The oxidation is catalyzed and there are several difrerent implementations
of this process.
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gelinas
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response 40 of 49:
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Oct 11 13:31 UTC 2003 |
So it starts with the reaction
H2S + O2 = H2 + SO2
right? So some free hydrogen is produced?
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rcurl
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response 41 of 49:
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Oct 11 18:47 UTC 2003 |
No free hydrogen is produced. The oxidation of H2S produces only H2O
and SO2. In fact, I do not know of any oxidation reaction that produces free
hydrogen so long as free oxygen is present. Water is thermodynamically
very stable and is strongly preferred as an oxidation product.
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gelinas
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response 42 of 49:
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Oct 11 23:10 UTC 2003 |
Yeah, I remembered that later. It takes a little bit of heat to start the
hydrogen-oxygen reaction, but the reaction is exothermic, so it provides the
heat necessary to keep itself going.
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russ
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response 43 of 49:
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Oct 12 01:06 UTC 2003 |
There are bacteria which get their energy from the oxidation
of hydrogen sulfide (some of them produce large amounts of
solid sulfur as a metabolite). It seems possible that some
mechanism could recover useful energy from the combustion
of H2S.
Hmmm.... some fuel cells run at well above the melting
temperature of sulfur... could be interesting if it wouldn't
poison the catalysts. All you'd need is a sufficiently
reducing environment on the fuel side and you'd recover
molten sulfur as the byproduct.
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rcurl
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response 44 of 49:
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Oct 12 05:00 UTC 2003 |
There isn't much H2S around to use as a fuel. It is also more toxic
than HCN. I don't think it will be an optimal fuel.
The more common bacterial use of sulfur compounds is of SO4(-2, sulfate),
which they use as an oxidant, reducing the sulfur from +6 to -2 (as H2S).
This is the source of H2S in much of deeper Michigan groundwater.
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russ
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response 45 of 49:
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Oct 12 14:27 UTC 2003 |
If you are gasifying coal or "sweetening" natural gas, there
can be plenty of H2S around. Certainly enough to be a problem.
Disposing of solid sulfur is probably easier and cheaper than
other possibilities like gypsum.
The Wabash River powerplant page claims 30,000-odd tons of
sulfur recovered during its test period. If we assume 10,000
tons a year of sulfur taken from H2S, the yield of hydrogen
would be about 625 tons a year or 1.7 tons of H2 per day. At
61,000 BTU per pound that's over 60,000 KWH per day, or
about 2.5 megawatts continuous. Gas wells probably handle a
lot less H2S, but a few tens of kilowatts might still be
welcome; production of a valuable byproduct such as sulfur
rather than a waste product like gypsum might be worth it too.
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rcurl
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response 46 of 49:
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Oct 12 14:46 UTC 2003 |
Have you said how you are going to get H2 from H2S?
Yes, sulfur from desulfurization is supplying most of our needs for sulfur
- much more than from Frasch plants. But you cannot yet economically
recover H2 from H2S, although there is ungoing research
(http://members.tripod.com/sulfotech/h2scrack.html).
The main use for all that sulfur is for producing sulfuric acid. I don't
think there is any surplus that needs to be thrown away.
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russ
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response 47 of 49:
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Oct 12 17:45 UTC 2003 |
I wouldn't get H2 from H2S, I'd convert H2S to H2O+S
via an anode reaction like this:
H2S + 2 OH- -> 2 H2O + S + 2 e-
As long as there was H2S present, the environment would be
too reducing to allow SO2 to form.
This depends on a catalyst which isn't poisoned by sulfur,
of course, but given our progress in genetic analysis of
extremophile organisms (and the tendency of those organisms
to live on things like H2S) I'm not sure that this is going
to be a huge obstacle. You might be able to find a lot of
the enzymes in bacteria growing at hydrothermal vents.
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rcurl
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response 48 of 49:
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Oct 12 18:38 UTC 2003 |
In #45 you said "the yield of hydrogen would be about 625 tons a year or
1.7 tons of H2 per day". That sounded like getting H2 from H2S. What did
you mean, then?
"As long as there was H2S present, the environment would be too reducing
to allow SO2 to form" means that SO2 is formed, but reacts immediately
with the excess H2S. This is the process I described earlier (I now recall
it is a form of the Claus process, which is conducted in the liquid phase
and does require a catalyst to be practical. No electrolysis is required.
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russ
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response 49 of 49:
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Oct 12 21:57 UTC 2003 |
Rane, if you look at the half-reaction in #47 you'll see
that H2 need never be formed. The energy required to
dissociate H2S into S and bound hydrogen (which later
combines with hydroxyl) would reduce the voltage somewhat,
but the "fuel" is free.
I have no doubts that this would yield energy, because
there are already aerobic bacteria which metabolize H2S.
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