I've been talking with Eerik form Solar Fire and the solar
concentrators - http://www.youtube.com/watch?feature=player_embedded&v=CXJgAmft2jI
He presents a simple problem and am wondering if anyone here can help
with the solution?
"I can calculate how much energy is reflected by the mirrors, and I
can determine a boiler radius and so discard any energy that falls
outside the boiler due to focal aberration throughout the day (some
light we allow to miss to keep a reasonable boiler size.).
What I can't do is the optimization of the boiler size; i.e. at what
point does increasing the boiler size create more losses than gains
(through convection with the air and radiating heat back into the
environment).
There's relatively simple equations to implement this, but I can only
easily understand the math part. How to judge the emissivity of steel
(does what kind of steel make a difference, how it's cut, will some
sort of paint help etc.), heat transfer coefficient through the steel
into the boiler (depending on steam temperature), etc.
With these equations in hand and reasonable values representing a
typical boiler (or many types of boilers, or general equations to
determine boiler properties etc.) then I can run an optimization to
output the ideal boiler size considering the intended application
temperature etc.
For now, I just try to keep the concentration factor at around ~200,
which seems a good value.
second problem:
What should we assume about losses in the steam pipe per meter square?
We used about 4-5cm of glass wool (resistant to 1200 C); good, too
much, not enough ?
Cheerio
Eerik"
http://www1.eere.energy.gov/industry/bestpractices/software.html
On Nov 26, 3:11 pm, Will Cleaver <willclea...@gmail.com> wrote:
> Hi Guys,
>
> I've been talking with Eerik form Solar Fire and the solar
> concentrators -http://www.youtube.com/watch?feature=player_embedded&v=CXJgAmft2jI
You can also look at 'black body approximation'. Make a coiled tube with one end closed and one end open. Put the closed end in your boiler. Shine your light into the open end.
Light going into the tube will reflect off the inside surface of the tube many times, with a certain amount of absorption every time. The path that allows light to reflect all the way in and all the way back out is vanishingly small, so the hole approximates a perfectly black, perfectly absorptive surface.
Better yet, it allows you to insulate your boiler well and pipe the light in through the tube. The only uninsulated surface radiating heat to the atmosphere will be the tube itself.
Copper pipe painted black inside should give you good absorption and heat transfer.
http://www.redrok.com/concept.htm#absorptivity
http://en.wikipedia.org/wiki/Selective_surface
http://en.wikipedia.org/wiki/Concentrating_solar_power
http://en.wikipedia.org/wiki/Absorbance
http://en.wikipedia.org/wiki/Stefan-Boltzmann_law
http://galileo.phys.virginia.edu/classes/252/black_body_radiation.html
heres something about insulating pipes
http://www.wbdg.org/design/midg_design.php
On Nov 27, 1:30 pm, Will Cleaver <willclea...@gmail.com> wrote:
> Thanks for the link Dorkmo. That is more whole-systems type stuff, for
> large plants.
>
> Thanks for the info Jamie.
>
> From Eerik;
> "We looking for more basic level stuff, such as what happens when light
> hits a surface. The easy equation that tells you how much energy you'll
> absorb based on steel thickness, concentration factor
> and temperature inside the boiler. it would only gain ~5 %"
>
> On 27 November 2011 15:53, jamie clarke <jamieclarke...@gmail.com> wrote:
>
>
>
>
>
>
>
> > Heat transfer coefficients for Mild steel:
>
> > Steam to mild steel to air= 11.3W/m^2 K (boiler radiation
> > to environment)
> > Water to mild steel to water= 340 W/m^2 K (feed water
> > entering boiler)
> > Steam to mild steel to water= 1050W/m^2 K (Cooling power of a
> > heat exchanger)
>
> > On Sun, Nov 27, 2011 at 3:34 PM, jamie clarke <jamieclarke...@gmail.com>wrote:
>
> >> The emissivity of a perfect vacuum is zero. If you encase the boiler in
> >> borosilicate glass and evacuate the air then any heat transfer from the
> >> boiler to the atmosphere will be radiant conduction and convection will be
> >> negligible.
>
> >> This means that the heat transfer through the steel can be neglected as
> >> the process will be nearly adiabatic. Heat transfer from the boiler would
> >> only begin to occur when the sun was gone. As an evacuated borosilicate
> >> shell for the boiler would probably be expensive you may need this link:
>
> >>http://www.engineeringtoolbox.com/overall-heat-transfer-coefficients-...