What about the risk of loss of dissolved CO2 upon aeration start-up?
How does the viscosity of the cherry syrup contribute to the stratification, and how is this affected by the temperature of the near-freezing soda? In other words, how does your aeration plan change depending on whether the water is warm or cold?
A valid concern, as the compressor's intake is located in very close proximity to the exhaust. Indeed, the off-gassing of CO2 upon beginning the aeration caused the compressor to sputter and cough, very nearly filling the intake with cherry soda. Some sort of backflow preventer may be in order.
Warm soda? I'm not sure how to respond to that.
"Forget pounds and ounces, I'm figuring displacement!"
If we accept that: MBG(+)FGSF(=)HBG(F1) And we surmise that: BG(>)HBG(F1) while GSF(<)HBG(F1) Would it hold true that: HBG(F1)(+)AM500(x)q.d.(=)1.5lbGRWT? PB answer: It depends.
