Quote:
Originally Posted by ernestbud
your formula for pressure is as follows:
3/8 line resistence per foot=.064
lenth of run= 50 ft
50x.064=3.2
so add3.2lbs to the 12-14lb recommended= 15.2-17.2 lbs of applied pressure
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Didn't I read elsewhere on this forum that you should never modify CO2 pressure to suit your system? I thought for a correctly balanced system you should modify line diameter and length to suit the CO2 pressure? Which for domestic beer at 38F is usually 14 PSI.
I'm not an expert by any means and I'd love for somebody to correct me so that I know I'm working it out all wrong. But I'd work it out at this...
I thought the formula was...
L=(P-(H*0.5)-1)/R
Where L=Length (50 ft in this case), P=Pressure used (let's say 14),H=Lift (let's say 4 feet) and R=Resistance of line. We'd have to balance the equation to make L=50 (or close to it). The only variable we should really be altering is R since we don't want to change the carbonation level, and we can't change the lift.
50=(14-(4*.05)-1)/R
50=11/R
50R=11 (total resistance of the system)
We'd need to use lengths and diameters of line which equal 11 for this system...
If we use 47.5ft of .5ID (which is .025 resistance per foot) it would give us 1.1875 resistance. 3.25 feet of 3/16ID line (3 resistance per foot) would give us 9.75 resistance.
1.1875 + 9.75 = 10.9375
Not too far off from our ideal of 11lbs of resistance. We'd need to modify it slightly if the lift was different and we could use a little more of the .5ID line to make up the difference.
So.... 47 1/2 feet of 1/2"ID and 3 1/4 feet of 3/16"ID would do it. Puts you 3/4 feet over but what the hey?