Hmm... Given that you're having leak problems, I have to ask: Is the container even designed to hold 10 psig, or is this something that is being tried as a new approach to an existing problem? I have to think that if this vessel is designed to hold a 10 psig blanket, it would be designed to maintain that pressure over its expected operating conditions. 10 psig might not sound like much, but assuming a perfect cube, each face of the cube is going to see a load of 22000 lbf or so at 10 psig. I sure wouldn't want to be anywhere near it if it's not designed to handle it.
If I'm misreading the situation and the vessel really is designed to hold that much pressure, then I definitely agree with chief. Get a PSV immediately upstream of the vessel as step one. If you do manage to seal your leaks up and get the system running, and the compressor control to stop it at a vessel pressure of 10 psig fails, then the compressor is probably going to run until it gets the whole vessel to its internal cutoff. If it's able to do that until everything is at 20 psig, then you're getting into ASME Boiler and Pressure Vessel Code ranges. Your vessel might not be covered by it, but the fact that you'd be in the same potentially lethal pressure ranges in a failure would give me pause.