In general I agree with the conversions posted, however, if you are getting less than optimal results, or going through the gas much much faster than you anticipated, I will drag out my handbook of chemistry and physics and make a calculation of what your density conversion factors should be. That could be referenced to a He scale, a Ar scale, a CO2 scale or whatever.
I believe the floating ball flow meter is called a Thorpe tube flow meter, and has a tapered inner tube, where the ball and the pressure of the gas find equilibrium. An old rotameter would give a more accurate measurement (used in medical applications where there is a need for more precise control of gas delivery, for example in anesthesia). It would be nice to have a rotameter to check the calibration of other meters. Back to the Thorpe tube meter...a couple of things...first they can be pressure compensated or non-pressure compensated. Second, I believe that they are more accurate when there is a downstream resistance to flow (for example a valve in a TIG torch).
I believe the orifice type flow regulator, which reads pressure on the high pressure side of an orifice, is more suspectable to downstream flow resistance, and therefore increase in pressure on the low pressure side of the orifice. I think this type of metering scheme is called a Bourdon flowmeter. Not really a flowmeter, but under the right circumstances, it is close.
Probably the best way to view the operation of a Thorpe vs Bourdon is that the Thorpe (floating ball) doesn't care about downstream flow restrictions, and truly measures flow. Whereas the Bourdon (orifice) meter measures pressure on the high side of the orifice, and assumes that the flow in unimpinged. If it is restricted, then the Bourdon will read high, compared to the actual flow.
Other than the potential inaccuracy of Bourdon meters when there is a downstream flow restriction, I am not clear on effects of temperature, as an example. I will ask around. One of the guys I know is a fluids guy.
I am interested in this because I have a Multimatic 200 and will want to MIG a SS exhaust later this year when the tractor is down for the winter.
I picked up about 25 ESAB R-33-FM-320 regulator/flowmeters (sold some, and kept a handful). What I wanted to do was to have a dedicated regulator/flow meter for each gas I might use. I also didn't have a regulator/flowmeter for CO2. Since CO2 reliefs are slightly different than for inert gases, I figured I was safe with the CO2 regulator. The parts breakdown for the R-33-FM-xxx regulator shows one flowmeter internal "calibrated" tapered tube for CO2, and another for other gases. I have ordered one for other gases (~$18), but don't have it yet, and haven't inserted it into one of the R-33-FM-320 regulators. When I do that, I will also change out the CGA 320 fitting for a CGA 580 fitting.
My final thought is on the gas mix. I have read claims that the actual mixes are / were subject to marketing hype, as to which one worked better than the other. I have not researched that, but it is something to keep in mind.
Regarding pricing, I was recently quoted $72 for 60 cu ft, and $140 for a 125 cu ft refill. The two LWS I use were willing to swap a N2 tank for a tri mix tank, and then back again when I was finished with the tri mix. I like sensible business people who do the reasonable thing.