Hi all,
I am looking to utilize an existing in-line CO2 sparger with N2, in order to draw out DO from a still product prior to entering a storage tank. I have no starting point for where to begin with gas flow rates and pressure gradient that will be, or if it's even realistic to expect significant DO reduction using such an insoluable gas in an in-line sparger.
Please let me know if you have any experience in a similar application.