Hi,
Has anyone succeeded in bottling around 4 vols brews using a counter-pressure filler without losing too much carbonation?
I've been trying without any success but I have two set-ups ideas I'd like to try and would like to have your opinion on the matter.
1. Let's start with a brew @ 34ºF and a pressure of 24 PSI for 4 volumes of CO2. Now if I want to bottle with a CPBF I would need to have my bottle at a similar pressure. This is where I have been having problems because the silicone stopper just pops out due to the high pressure. The idea is to mount the counter pressure on a wall and exert downward pressure on the CFBF to avoid the stopper from popping out.
2. Same brew @ 34ºF/ 24PSI/ 4vols. Let's say I pressurize my bottle at 14 PSI and use that same pressure to push the brew out of the keg (I have a T-connector); I am left with a 10 PSI pressure difference. If I use a length of tubing with ID of 1/4 in to compensate for the 10 PSI, I would need around 12 feet of tubing to reduce foaming and loss of carbonation. Pretty much how they do it for draft beer.
In both instances, the bottles will be cold, and the tubing as cold as I can.
Thanks
P.S. Bottle conditioning is not an option as I want to apply the same science for sodas.
Has anyone succeeded in bottling around 4 vols brews using a counter-pressure filler without losing too much carbonation?
I've been trying without any success but I have two set-ups ideas I'd like to try and would like to have your opinion on the matter.
1. Let's start with a brew @ 34ºF and a pressure of 24 PSI for 4 volumes of CO2. Now if I want to bottle with a CPBF I would need to have my bottle at a similar pressure. This is where I have been having problems because the silicone stopper just pops out due to the high pressure. The idea is to mount the counter pressure on a wall and exert downward pressure on the CFBF to avoid the stopper from popping out.
2. Same brew @ 34ºF/ 24PSI/ 4vols. Let's say I pressurize my bottle at 14 PSI and use that same pressure to push the brew out of the keg (I have a T-connector); I am left with a 10 PSI pressure difference. If I use a length of tubing with ID of 1/4 in to compensate for the 10 PSI, I would need around 12 feet of tubing to reduce foaming and loss of carbonation. Pretty much how they do it for draft beer.
In both instances, the bottles will be cold, and the tubing as cold as I can.
Thanks
P.S. Bottle conditioning is not an option as I want to apply the same science for sodas.