Without knowing the source it would be hard to tell. I don't see the DIN number listed? Perhaps the most knowledgeable person regarding this is Mr. Pex, go to
www.mrpex.com and maybe drop him a line. Perhaps he has a method to test to test the tube.
Here is a link to one of his articles for years ago. (broken link removed)
There is no question that non barrier pex will cause systems components to fail prematurely. We saw this first hand back in the 1980 when PB polybutylene and other non barrier rubber products were used. On high temperature systems the results were often seen within the first year. Most often the expansion tanks would pinhole being a thin walled steel product.
Pumps would corrode so badly that impellers would jam, usually the second failure. Then threaded connections would corrode away around the thread, at the thinnest part of the wall dimension. Often times expansion tank nipples would corrode right out of the thin steel tanks and the tanks would fall to the floor. Even cast iron and steel boilers would fail after some time.
I've seen threaded nipples snap off at the cast iron boiler connections.
The byproducts of all the corrosion was a thick red sludge that would gum up valves and eventually plug the tube. The small diameter radiant tubes would plug to the point that they could not be flushed out. We tried pressure washers at 150 psi and more to flush plugged tubes in some cases. Almost as if someone put concrete in the tubes

Many of those early radiant inslab systems had to be abandoned and baseboard or forced air systems retrofitted.
So the question was not IF components would fail from non barrier tube use, but when. The water temperature is a big factor. The high operating temperature baseboard systems, for example would fail rather quickly, lower temperature could go a few years before leaks developed.
Those radiant manufacturers in denial tried to head off the inevitable with corrosion inhibitor products. These did have some sucess but were expensive, possibly toxic and required frequent "boosts" depending on temperatures again.
I'm not sure the cost difference between barrier and non barrier would balance the failure potential. Perhaps if you are installing thousands of feet of tube? But even then isolating the non barrier tube with a plate HX and non ferrous pumps, etc would prove to be a better solution.
hr