At first glance, this appears to be a simple optimization problem. You partly recognize this in Post #3. Start by searching
compressibility factor hydrogen. You will quickly find that the effect is significant at 700 atm.
Then dig out a thermodynamics book and study the chapter on filling a tank from a high pressure tank. You can find some good hand waving discussion by searching
fill scuba tank temperature.
H2Fill said:
Lets pretend it's nitrogen then. I put in the note about ignoring safety to try and avoid going down this rabbit hole of how hydrogen is, surprise, explosive.
SURPRISE! Even inert gases are explosive at much lower pressures. Search
scuba tank explosion and
water heater explosion to learn about this. Keep in mind that scuba tanks run at less than half the pressure you are talking about, and water heaters less than 1/50 the pressure.
H2Fill said:
I am trying to get an idea of the feasibility of doing this
Part of the feasibility, and only hinted at in your Post #3, is the cost of compressing the hydrogen to pressures higher than the fill pressure. And that cost is a function of supply tank size.
All of which is why I said:
jrmichler said:
An engineer who thinks this is merely a pressure and mass calculation, and does not think to look further, fails.
We are here to help you. We tailor our answers to the ability of the OP based on what they post, and on their profile information. If, for example, you had said that you were a middle school student, you would have had entirely different answers. And those answers would have been less direct.