Post #49: Adapting the Industrial Reactor for Research – III (ρ in instrumentless tracking of IV and other applications)
Relevant equations: Vhs = Vre – (1000x + 10xy + m1/ρ mhs = 2pVhs/RThs Io – (12.7/x)(m – m2 – mhs) A close look at Vre, Vrm and Vhs : The reactor volume (Vre) distribution as we move up the reactor from the lowermost point in the bottom dish is erratic and cannot be calculated easily thru geometry. It further changes with the temperature. Thankfully, we don’t need it because we are not calibrating the reactor. Interestingly, it can be…