Quote: | And why would anyone mix glycerol with H2O2 if it's better to use separated cells in battery? | Appologies,
but I want to specifically zero in on this point from another angle as well.
Consider steam reforming, say with methane and superheated steam, from wikipedia's article on it, I quote:
"At high temperatures (700 – 1100 °C) and in the presence of a metal-based catalyst (nickel), steam reacts with methane to yield carbon monoxide
and hydrogen. These two reactions are reversible in nature.
CH4 + H2O ⇌ CO + 3 H2"
They then go on to say that you can use the water gas shift reactions at lower temperature to make even more hydrogen and convert the CO to CO2.
Okay, the point is that the first steam reforming step is very endothermic because it makes so much hydrogen.
Industrially, you have two choices to solve this problem. You either burn fuel on the outside in a furnace with these gases flowing in pipes on the
inside OR as is often the case and simpler, you burn some of the methane internally with oxygen to make the heat for you!
How much? Just enough for this to tick over.
So you feed CH4, superheated H2O and some O2 and it works, you still get out CO and H2, but because of the oxygen, you change the CO to H2 ratio that
you get. Sometimes having a lower CO:H2 ratio is imperative for the next down stream step (whatever you were making this mixture for), in that case,
you have no choice but to run the reformer without co feeding oxygen and worry about the extreme heat transfer that is needed from the outside through
the pipe walls in your furnace.
Anyway, as I've often said before, my system is similar, except that we go the low temperature equivalent and therefore have to use more reactive
things for kinetic reasons. So instead of methane or hydrocarbons (too inert at low T), I propose glycerine as a compromise between hydrogen making
capacity and reactivity (sacrifice some hydrogen making capacity compared to pure hydrocarbons but gain reactivity). However, just like steam
reforming methane, the reaction:
C3H8O3 + 3H2O => CO2 + 7H2
is very endothermic, so you 'fix' this by the same trick as in steam reforming, you co feed an oxidant. However, you want your oxidant to also be nice
and kinetically active (by the way oxygen is not as kinetically active as you might think, it has the slowest kinetics in a fuel cell even with
platinum catalysts), so I propose using H2O2, which is in between H2O and O2 but has fantastic chemical kinetics on a catalyst.
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