I would love a copy of that doc... please do send one my way.
i also made a calculation based on that line from the KE report
- surprisingly i got zero comments - although i consider it a very relevant
issue... 25 atm at startup is much more at 500C... i would love it if
someone could double
I question the amount of nickel used. The one liter (1000 cc) Cat-E used 100
grams of catalyst. By proportion, a 50 cc volume should use only 5 grams of
catalyst. The density of the catalyst is too high. It should be about 3g/cc
since it is porous.
On Wed, Apr 20, 2011 at 5:33 AM, .:.gotjosh
Axil,
I agree about 5g in proportion, but the KE report says:
The central container seen in figure 3 has an estimated volume of 50 cm3
and it contains 50 grams of nickel.
I also thought about the powder density/porosity and chose a number close to
the full density of nickel metal, as i imagined
In reply to .:.gotjosh's message of Wed, 20 Apr 2011 11:33:49 +0200:
Hi,
[snip]
I suspect that Hydrogen wouldn't be absorbed by the Ni fast enough for it to
become saturated when the Hydrogen is initially connected, so one might expect
the Hydrogen pressure in the container to actually drop
Re: estimated volume
Catalyst volume is important stuff. How true is it? Who made the estimate?
Any idea?
On Wed, Apr 20, 2011 at 3:35 PM, .:.gotjosh ene...@begreen.nu wrote:
Axil,
I agree about 5g in proportion, but the KE report says:
The central container seen in figure 3 has an estimated
At 02:24 PM 4/19/2011, Jed Rothwell wrote:
Below is the latest version. Not
many changes. The original is in .docx format. If anyone wants a copy let
me know.
H gas pressure in the cell
is 25 bar (~360 psi) (Rossi? Blanton)
That's from the KE report :
Startup. Prior to
startup, the hydrogen
Alan J Fletcher a...@well.com wrote:
That's from the KE report :
Thanks.
- Jed
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