MaxStout, do you mind double checking my math for me?
I have 5.5G in a 7G fermenter. My fermenting temp is 65F and my temp to crash to is 35F.
Should be about .086 gallons, or about 11 oz.
MaxStout, do you mind double checking my math for me?
I have 5.5G in a 7G fermenter. My fermenting temp is 65F and my temp to crash to is 35F.
Thanks for clarifying. I had thought jar two was being drained dry.I can crash with my glycol chiller from 65F to 35F in an hour...but I go in 5F increments every 4 hours.
With a 3 pc airlock (using that now) on jar 2, the top hat of the airlock would suck down to seal off the stem if that happens, but jar 2 is half full of CO2 also.
But....I have never seen jar 2 fully emptied of sanitizer even with quart jars. 1/2G jars may be an overkill, but I plan to go that route next brew.
Should be about .086 gallons, or about 11 oz.
Thanks for clarifying. I had thought jar two was being drained dry.
One last question how long do you stay at 35F and do you see additional movement of starsan once the temperature stabilizes?
I am asking all these question as I have three fermenters and the cost of three harvesters is about the cost of buying a dedicated 5gal CO2 tank and regulator. I read the harvester thread and it seems like reabsorption of CO2 could need more than what can be captured in a 1/2gal jar so for an extended crash you might need to add more co2 somehow.
I believe if you have it connected in the beginning there is enough co2 produced during fermentation to purge any oxygen.Are you somehow flushing those jars with co2 before starting fermentation? If not, wouldn't the o2 in the air (in the jars) diffuse with the incoming co2 and still be present when cold crashing?
FWIW, here's the formula for determining suckback:
Suckback volume = Headspace volume*(1-(Mintemp+459.67)/(Maxtemp+459.67))
Temps in Fahrenheit. Volume units don't matter, as long as you use the same.
Thanks MaxStout. I'm on the same page now.
Once I hit equilibrium and the crash temp is stable, I don't see much movement in the jars. My process is to hit crash temps for a day or two, then move to keg with an O2 free pressure transfer. These brew buckets cant take more than 1-2 psi, so this is very delicate.
I guess I'm not giving the beer much time to reabsorb.
MaxStout, do you mind double checking my math for me?
I have 5.5G in a 7G fermenter. My fermenting temp is 65F and my temp to crash to is 35F.
I am coming up with .08577. Is this basically 1/4 of a gallon or 32 ounces?
Thanks for the formula and the other comments.
I think you also need to take into account contraction of the beer itself, which is something like 1 or 2% but still would still be within the reserve of a 1/2gal jar.
When you finally get around to using your setup I would like to hear if your results match the calculated values.
In the harvester thread it seemed people agreed co2 reabsorption is an issue but it was unclear how much time is required. Thanks for sharing your experience which I would guess is pretty typical for a cold crash.
Okay so I got the ss brew tech hose barb to connect a blow off tube to. I also want to use it to do pressurized transfers.
Issue is I only have one gas post coming out of my regular and it has a ball lock connection to it. Is there any way I could rig up a gas post that I can connect to the ball lock and then have tubing coming out of that into the blow off barb on the brew bucket?
Okay so I got the ss brew tech hose barb to connect a blow off tube to. I also want to use it to do pressurized transfers.
Issue is I only have one gas post coming out of my regular and it has a ball lock connection to it. Is there any way I could rig up a gas that I can connect to the ball lock and then have tubing coming out of that into the blow off barb on the brew bucket?
Question - for all yous guys doing O2 Free trasnfers
I assume you are using a Hose from the Conical out
into your Keg ( liquid out )
in order to get Beer from Conical to Keg
Isn't there some O2 in that Hose ?
Or do you fill the hose with Star San ? ( vodka ? )
All the effort to rid O2 from the Cold Side
that last step from Conical to Keg = whats in that hose ?
That Hose will have some "air" in it..... unless its filled with liquid.....?
What am I missing ?
Thanks
S
Question - for all yous guys doing O2 Free trasnfers
I assume you are using a Hose from the Conical out
into your Keg ( liquid out )
in order to get Beer from Conical to Keg
Isn't there some O2 in that Hose ?
Or do you fill the hose with Star San ? ( vodka ? )
All the effort to rid O2 from the Cold Side
that last step from Conical to Keg = whats in that hose ?
That Hose will have some "air" in it..... unless its filled with liquid.....?
What am I missing ?
Thanks
S
Presumably you have your keg purged and pressurized. Leave the end of the jumper hose that goes on the fermentor off. Open the pressure relief valve and put the jumper hose quick disconnect on the keg out post at the same time. This will allow CO2 to flow through the hose and just as the flow of the CO2 seems to stop put the open end of the hose on the hose barb of the fermentor....then transfer under pressure to the keg.
I open the pressure relief valve because I do have Star San in the tubing and don’t want the full pressure (I purge and pressurize at 30psi) of the CO2 spraying the Star San. You could just wait to pull the pressure relief valve on the keg after purging your jumper hose. It needs to be open during transfer.
This is the setup I have:
http://www.laundrybrewing.com/2017/05/blow-off-set-up.html?m=1
Works good.
Just curious, has anyone modified their racking valve on the brew bucket by welding / soldering a TC connection?
What about something like this?
https://www.brewershardware.com/3-4...p-Ball-Valve-Quick-Clean.html?category_id=314
Then would it just be a matter of finding a matching TC ferrule to be welded onto the bucket? This is all new to me, I don't know anything about TC fittings and valves.
Although after looking at all this stuff, I guess the question is asked is it worth spending all the additional money rather than just getting a conical.
The steep angle at the bottom of the bucket (the cone) forces the supplied racking valve downward sharply making any work in that area tedious. Add to that the curvature of the cone, so any TC ferrule will again be tedious.
I have two of these, and in my opinion, you'll spend more time, dollars and energy on a project that is quite difficult. Raising the bucket on legs is a possible solution, but again, is this all worth it when a conical is not that much more $$ and designed for what you are looking for.
Yeah, that's ultimately the conclusion I came to after thinking about it more. I'm debating whether or not to buy some additional accessories (domed lid and TC connections for blow off and CO2 pressure transfers which will run me an additional $100) or spending a bit more and getting a Spike 7 gallon conical. Only issue with the conical is it won't fit in the current fridge i'm using to ferment in. Just gotta make sure the Brew Bucket fits with the domed lid and TC accessories.
Have you noticed any significant issues with the valves and getting the right seal? I got the bucket with the thermowell. I assume it's just a matter of making sure the seal is good before filling it like any other vessel with a valve.
Yeah, that's ultimately the conclusion I came to after thinking about it more. I'm debating whether or not to buy some additional accessories (domed lid and TC connections for blow off and CO2 pressure transfers which will run me an additional $100) or spending a bit more and getting a Spike 7 gallon conical. Only issue with the conical is it won't fit in the current fridge i'm using to ferment in. Just gotta make sure the Brew Bucket fits with the domed lid and TC accessories.
Have you noticed any significant issues with the valves and getting the right seal? I got the bucket with the thermowell. I assume it's just a matter of making sure the seal is good before filling it like any other vessel with a valve.
Agreed. If you go this route buying a domed lid, make sure the height additions fit in your current fermentation chamber.My understanding is that the domed lid helps with pressure. Plus the domed lid has a big tri clamp opening for dry hopping. Probably not necessary because all in I’m looking at another $100.
Agreed. If you go this route buying a domed lid, make sure the height additions fit in your current fermentation chamber.
I had shifted over to a glycol chiller once I got to the point you are discussing now. The refrigerator and freezer size and height limitations was one of my biggest reasons for the glycol chiller.I have about 7" of space above the brewbucket right now. I'll have to figure out if that will work with the domed lid, a 4" to 1.5" TC reducer and then the 1.5" 90 elbow hose barb for a blowoff. Any experience with this set up and how much space is required above the normal bucket lid?
I had shifted over to a glycol chiller once I got to the point you are discussing now. The refrigerator and freezer size and height limitations was one of my biggest reasons for the glycol chiller.
7" of height may sound like a lot of room to spare, but when you start adding the domed lid with accessories as mentioned, 7" will vanish in a hurry.
I am not trying to sound negative or make it look like your plan cant be done since it certainly can. I realized the limitations I was facing lifting and fumbling with heavy fermenters into freezers and refrigerators, plus you can only do limited fermenters at a time. Like my buddy was asking....how can I ferment an ale and a lager at the same time in the same fridge? I am running 4 fermenters at the same time off my chiller, and each fermenter has it's own unique temp setting.
Something to think about for the future....but in the meantime, I think Ss Support may be able to give you a fairly accurate measurement assessment if you email in a support ticket.
I'm trying to decide if I should get another brew bucket or just save up some extra money and go for a conical. Does anyone have both? Was it worth the extra money for the conical?
So I started doing pressure transfers out of mine, but I’ve found the seal on the bucket lid or the rigidity of the lid itself will not permit a leak free transfer even at 1psi. I’m getting into stainless fabrication and I’m thinking about building a slip on ring with screw down clamps (think unitank) for the lid. Wish the clamps on the lid that come with it had some adjustment.
So I started doing pressure transfers out of mine, but I’ve found the seal on the bucket lid or the rigidity of the lid itself will not permit a leak free transfer even at 1psi. I’m getting into stainless fabrication and I’m thinking about building a slip on ring with screw down clamps (think unitank) for the lid. Wish the clamps on the lid that come with it had some adjustment.
I got a question for those doing closed transfers with the standard lid. Is your lid air tight during the transfer? I get a bit of co2 leaking there as the standard clamps don't seal perfectly. It has a good seal during fermentation, but I get a co2 exiting there at 2 psi.
Is this normal?
I got a question for those doing closed transfers with the standard lid. Is your lid air tight during the transfer? I get a bit of co2 leaking there as the standard clamps don't seal perfectly. It has a good seal during fermentation, but I get a co2 exiting there at 2 psi.
Is this normal?
I got a question for those doing closed transfers with the standard lid. Is your lid air tight during the transfer? I get a bit of co2 leaking there as the standard clamps don't seal perfectly. It has a good seal during fermentation, but I get a co2 exiting there at 2 psi.
Is this normal?
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