transition from forced carb to serve

Homebrew Talk - Beer, Wine, Mead, & Cider Brewing Discussion Forum

Help Support Homebrew Talk - Beer, Wine, Mead, & Cider Brewing Discussion Forum:

This site may earn a commission from merchant affiliate links, including eBay, Amazon, and others.

rpacecar

Member
Joined
Feb 9, 2013
Messages
12
Reaction score
0
First batch finished, I bottled 13 and rest went to corny at 30 psi for 2 days. I turned gauge down to 6 psi to serve and pure head poured out. Am I supposed to purge out all air before setting to 6 psi.?
 
First batch finished, I bottled 13 and rest went to corny at 30 psi for 2 days. I turned gauge down to 6 psi to serve and pure head poured out. Am I supposed to purge out all air before setting to 6 psi.?

Yes. You should purge and then raise it to 6 psi again.
 
Serving pressure is the pressure required to maintain the volumes of CO2 fit for the style. 6 psi is not enough. For most beer, it's in the 10-12 pound area. Then you use line length to get a good pour.

Even if you purge it, the pressure in the head space will soon return to a pressure well above your serving pressure as CO2 comes out of solution. Your mistake was leaving it at 30 pounds for two days.
 
Yep, 6 PSI is far too low. Unless you're serving below freezing, I guess.

If you can't get good pours when the beer is in the 10-15 PSI range, then your line lengths are all wrong. Too foamy means too short of lines. No head and too slow means too long of lines.

First determine how many volumes of CO2 your style of beer needs. You didn't say what style it is, so here's a chart. http://www.tastybrew.com/calculators/priming.html

Then look for that number of volumes at your known serving temperature on this page. http://www.kegerators.com/carbonation-table.php

For example, I'll if you were force carbing an American Pale (2.26-2.78 vol), you might go middle of the road at 2.5 vol. If your serving temperature is 41F, then your beer needs to be at just shy of 12.8 PSI or so.

Why did you force carb for 2 days at 30 PSI? Unless you have a Wheat or other highly carbed beer, you're almost certainly overcarbed at this point. Next time, try force carbing at 3x the serving pressure for 24 hours. In the case of this American Pale at 41F, you'd carb at 38 or 39 PSI for 24 hours.

For now, figure out the appropriate serving pressure and reduce your regulator to that pressure. Every few hours, burp the keg using the pressure relief valve until you hear the regulator groan. You can speed it up by shaking between burps if you really must. It's going to take a little time to get it back out of the overcarbed range, unless you were carbing exceptionally warm.
 
Thanks for the replies, I purged and kept at 6 it's a Belgian ipa. Pour pressure seems fine but a little heady. Think ill take the advice and extend lines and up co2 to 10
 
You're getting foam for one of four reasons. Overcarbonation is ruled out because of the 6 PSI, so we're down to two.

1- The faucets are warmer than the beer. When the cold beer hits the warm faucets, the faucets get colder and the beer gets warmer. This causes the beer to be able to hold less dissolved CO2, so some falls out of suspension, causing turbulent flow and a chain reaction. In really bad situations, you can hear sputtering. You can determine if it's this one by touching the faucet or using an IR thermometer, then pouring a few pints.

2- The lines are kept warmer than the beer in the keg. Same as above, CO2 falls out of solution because of the temperature increase. This pushes some beer back into the keg and leaves CO2 pockets in the lines. This one is visible in all transparent and semi-transparent lines when you open the lid.

3- You have a major imbalance between keg pressure and line flow restriction. Very possible in this case. You either need longer or thicker lines. At only 5', you'd need something in the range of 5/16" ID line for around 12 PSI.

Use this formula to get a rough idea for how long your lines should be:

Brewer's Friend said:
L = (P -(H x .5) – 1 ) / R

Where:
L = length of beer line in feet
P = pressure set of regulator
H = total height from center of keg to faucet in feet
R = resistance of the line from the following table
1 = residual pressure remaining at faucet (this can be increased to 2 if you need to increase pressure to increase dispense rate)


Line Type: Resistance:
3/8” OD stainless beverage tubing .2
5/16” OD stainless beverage tubing .5
1/4” OD stainless beverage tubing 2
3/8” ID plastic beer line .11
5/16” ID plastic beer line .17
1/4” ID plastic beer line .7
3/16” ID plastic beer line 2.7

4- Damnit, I forgot already.

If you have Bev-Seal lines, then they need to be much longer.

Hope this helps.
 
Definitely gonna be 3. Currently everything is in the refrigerator. Line is only about the length of a keg tap id guess about 3-4 ft.
 
It's very common to experience 1 and 2 in a keezer because they don't have fans to recirculate the air. Stratification sets in. At the bottom, it's 10F colder than the top.

The solution is a recirculation fan of sorts. If you're in a refrigerator, I assume it has one already.
 
Yes It does. The line is 3/16 and 4 1/2 ft. Ill start there but for now I'll fill pitcher and enjoy more
 
Cool. :)

I fill two glasses when a tap is fully warm. Drink the second one. First one settles out to about 1/3 cup... dump it om top of the full one once its down half way. :)
 
Back
Top