As I understand the theory, say a beer was kegged @13 PSI and that is the required pressure at 38 F. when the gas is in balance, But some say to add 1 pound pressure or 14 Psi for "Push". Again as I understand it the "Push" is to offset the resistance of the beer passing through the beer line and being slowed down by friction contact with the edge or wall of the beer line. Also though less mentioned it would offset the rise in elevation from the beer level in the keg to the tap.
I must be missing something and so ask to learn what it is. As I see it elevation or keg to tap is a constant, and takes a certain given amount of thrust (in this case pressure) to over come gravity.
Regarding beer line resistance: I've doubled my length and slowed the flow noticeably. But I doubt I cut it in half (flow per minute) and doubt it's a linear effect guess I can check the resistance charts to confirm this. But this does prove there is beer line resistance in play.
Here's what trips me up and I need help with. Personally I have a 1 & 1/2 F. temp. degree gradient between the units bottom and top. Also a 6 & 1/2 F temp. difference between bottom and tower tap, and 1st. pour is good very close to 2nd. But let's imagine a perfect world where all temps. are the exact same; bottom, top and tower. WHY do I need "Push"? To off set gravity and resistance? If so as I see it the only time those 2 factors come into play is when the tap is open and that in the lifetime of a keg is a very very small percent. Pretty much the constant state of my keg is tap closed so there is no gravity to overcome the beer is already up there and in a closed system there is no need for thrust to counteract gravity. The beers not moving either so resistance is a moot factor also.
I uses to add the 1 pound Push but have recently upon reflection of all this quit. I have ascertained no ill effects. So why push?
1) If it's for resistance slowing my pour, then shortening my line works as well. If it's for gravity, uphill push then since I was after a slower pour anyway the rise works to my benefit.
2) What little time the tap was open for is quickly adjusted for by the Co2 infusion to steady state pressure.
My premise is if 13 Psi is the correct kegged and current temp. pressure then there is no need to Push.
3) What harm am I doing by not pushing? Breakout? Can't see how if the temp. were constant and the line is sealed when tap is closed the pressure through out would remain the same in theory. So no breakout. Flow speed correctly controlled by line length not pressure so why change PSI?
I must be missing something and so ask to learn what it is. As I see it elevation or keg to tap is a constant, and takes a certain given amount of thrust (in this case pressure) to over come gravity.
Regarding beer line resistance: I've doubled my length and slowed the flow noticeably. But I doubt I cut it in half (flow per minute) and doubt it's a linear effect guess I can check the resistance charts to confirm this. But this does prove there is beer line resistance in play.
Here's what trips me up and I need help with. Personally I have a 1 & 1/2 F. temp. degree gradient between the units bottom and top. Also a 6 & 1/2 F temp. difference between bottom and tower tap, and 1st. pour is good very close to 2nd. But let's imagine a perfect world where all temps. are the exact same; bottom, top and tower. WHY do I need "Push"? To off set gravity and resistance? If so as I see it the only time those 2 factors come into play is when the tap is open and that in the lifetime of a keg is a very very small percent. Pretty much the constant state of my keg is tap closed so there is no gravity to overcome the beer is already up there and in a closed system there is no need for thrust to counteract gravity. The beers not moving either so resistance is a moot factor also.
I uses to add the 1 pound Push but have recently upon reflection of all this quit. I have ascertained no ill effects. So why push?
1) If it's for resistance slowing my pour, then shortening my line works as well. If it's for gravity, uphill push then since I was after a slower pour anyway the rise works to my benefit.
2) What little time the tap was open for is quickly adjusted for by the Co2 infusion to steady state pressure.
My premise is if 13 Psi is the correct kegged and current temp. pressure then there is no need to Push.
3) What harm am I doing by not pushing? Breakout? Can't see how if the temp. were constant and the line is sealed when tap is closed the pressure through out would remain the same in theory. So no breakout. Flow speed correctly controlled by line length not pressure so why change PSI?
Comment