Mid March
Sounds like the Chinese New Years go ya?
Mid March
Sounds like the Chinese New Years go ya?
Observation!About the smell:
I brewed on Sunday and tried something new to see if I could reduce the smell. I drain the effluent into a PVC pipe and down the drain. I stuffed a rag in the top to try to seal it.
View attachment 612445
I felt that it reduced the odor a fair amount but it was still significant. However, when I opened the garage doors after brewing to air out the space it was better than the previous time.
I poked my head down under the sink and it seemed clear to me that this is where the odor seems to mostly be coming from.
I'm going to try a few other variants; I probably can seal that pipe better than I did. I didn't put a plug in the sink drain and it's possible I had some odor coming back up from the P-trap. I may try some foam sealer to seal up the top.
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Here's one other question: I'm using Fermcap-S to prevent boilovers. Any chance this is part of what's producing the smell? Is there an alternative to using Fermcap that would also prevent boilovers?
View attachment 611006 Was able to successfully try out my 30G Spike kettle with the SteamSlayer, using some spare parts I had lying around. After boiling water for an hour to see the rate and effectiveness, I decided to try with some wort. I had bought a More Beer Blonde Ale extract kit for a test. While I have a drain in my garage, I was glad to dump that smelly water outside. The garage stayed dry!
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View of the 2" TC Tee piece with the misting nozzle:
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Tear down. With the Norcal piece that I ordered this morning, I will be able to reduce several of the pieces when it comes on Friday.
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Edit:
When the Norcal part arrives the items in purple will no longer be needed.
About the smell:
I brewed on Sunday and tried something new to see if I could reduce the smell. I drain the effluent into a PVC pipe and down the drain. I stuffed a rag in the top to try to seal it.
View attachment 612445
I felt that it reduced the odor a fair amount but it was still significant. However, when I opened the garage doors after brewing to air out the space it was better than the previous time.
I poked my head down under the sink and it seemed clear to me that this is where the odor seems to mostly be coming from.
I'm going to try a few other variants; I probably can seal that pipe better than I did. I didn't put a plug in the sink drain and it's possible I had some odor coming back up from the P-trap. I may try some foam sealer to seal up the top.
*********
Here's one other question: I'm using Fermcap-S to prevent boilovers. Any chance this is part of what's producing the smell? Is there an alternative to using Fermcap that would also prevent boilovers?
As many have reported in this thread, the power to maintain a boil is much less than with an open kettle, typically 50-60%. So if you didn't turn down the power during the boil, the overly vigorous "boil over" is expected.With that being said, I had 7 gallons in a 15 gallon spike kettle and there was a “boil over” that all ran down the steam hose. Another benefit of this. I think I was boiling with too much power to the element.
I brewed Saturday using my setup for the first time. I did not notice any unpleasant odors. My hose was running to a bucket right under my brew table so there was nothing sealing off vapors. I did not use any ingredients for preventing boil overs. So maybe?
With that being said, I had 7 gallons in a 15 gallon spike kettle and there was a “boil over” that all ran down the steam hose. Another benefit of this. I think I was boiling with too much power to the element.
Certainly you could make it work. Would it have any advantage over the steam slayer? Just off the top of my head, I'd say no.What are the thoughts on trying something like this? I was thinking that the steam could pass through the smaller inner tubes and hooking this up to my glycol chiller to run through the inside of larger tube. This type of condenser is used in larger applications like power plants where they condense their steam from their combustion turbine and then recirculate and reheat it for the steam turbine. This would eliminate the use of having a water spray system. Would the glycol chiller provide enough cooling to condense the steam and provide the vacuum?
What are the thoughts on trying something like this? I was thinking that the steam could pass through the smaller inner tubes and hooking this up to my glycol chiller to run through the inside of larger tube. This type of condenser is used in larger applications like power plants where they condense their steam from their combustion turbine and then recirculate and reheat it for the steam turbine. This would eliminate the use of having a water spray system. Would the glycol chiller provide enough cooling to condense the steam and provide the vacuum?
The tube I have pictured above has the smaller tubes inside with space around them for the cooling water/glycol to flow while the steam passes through the inner tubes, or vice versa depending on how you hook it up. Could you collect the condensate as it runs out of the condenser and use that as your cleaning water?
For starters, I know that the load on the glycol system would cost more in electricity and wear and tear than 10 gal of tap water. It would also render your glycol useless fir fermentation control during boiling as it would be too hot. Finally, people are finding the diluted waste water to smell bad. What do you think the concentrate would smell like?
What are the thoughts on trying something like this? I was thinking that the steam could pass through the smaller inner tubes and hooking this up to my glycol chiller to run through the inside of larger tube. This type of condenser is used in larger applications like power plants where they condense their steam from their combustion turbine and then recirculate and reheat it for the steam turbine. This would eliminate the use of having a water spray system. Would the glycol chiller provide enough cooling to condense the steam and provide the vacuum?
What are the thoughts on trying something like this? I was thinking that the steam could pass through the smaller inner tubes and hooking this up to my glycol chiller to run through the inside of larger tube. This type of condenser is used in larger applications like power plants where they condense their steam from their combustion turbine and then recirculate and reheat it for the steam turbine. This would eliminate the use of having a water spray system. Would the glycol chiller provide enough cooling to condense the steam and provide the vacuum?
You could calculate the number of BTUs needed, I think--In my system, with a fairly rigorous boil, the effluent was about 140 degrees. I was boiling off 1 gallon per hour, and the water spray is about 9 gph. The water starts out about 50 degrees or so. It takes a BTU to raise a pound of water 1 degree fahrenheit (about--that's at 39 degrees IIRC, but close enough for purposes here). Ten gallons is 84.3 pounds. Nine gallons is 75.06 pounds.
This is where it's early, I haven't had enough coffee, and I'm sure there's an engineer out there who can more accurately figure this out, but I'm thinking that if 75.06 pounds of water is raised in temperature from 50 to 140, that would be a capture of (75.06 pounds of water x 90 degrees of temp change) of 6755 BTUs of energy.
Engineers, is that at least in the ballpark? Or has the lack of coffee sapped my brainpower?
Your math is not the whole story. You are correctly calculating the heat required to raise the water spray from 50F to 140F BUT you are also adding the condensed steam to that water stream, so it doesn't cover the entire system. You have to add the 1 gal x 8.3 lbs/gal of condensed steam to the mix, the latent heat removed by condensing, and the sensible heat removed to bring it down from 212F to 140F.
You really don't need to do all that however. It's pretty easy to calculate how much heat you need to remove in order to condense the steam:
1 lb of 212F steam = 970 btu's (heat of vaporization of water)
1 gal of water = 8.3 lbs (yes, this changes depending on temperature, but it's close enough...)
If you boil off one gallon during the boil, you need 8.3 x 970 = 8,051 btu's.
Ideally, the steam slayer effluent only needs to be below boiling temperature - any extra means you are flowing more water than you need to. Practically, you probably want it a good amount cooler to make it safer to handle/dispose of. I've seen PVC drain lines melt because 200F+ condensate was put down it for a long time.
I also think the traditional 1 gal/hour boil off rate is way off. Most people that are using the steam slayer are finding the boil rates are much lower, which makes sense, because you'd never be able to condense 8.3 lbs of steam in an hour and get the effluent at 140F with only 6755 btu's.
About the kind of response I'd expected.
In other words: I was close, wasn't I?
Love it!The laws of thermodynamics, per Robert Heinlein. (I think)
1. You can't win.
2. You can't break even.
3. You can't get out of the game.
If I were starting with a clean sheet of paper, I'd provide for both. I don't see a down side to good ventilation, the issues come with trying to retrofit it. The plumbing for the steam slayer is minimal, so why not? I'm trying to squeeze a brewery into my too-small laundry room, so I'm quite jealous!Well, I'm convinced! Seems there is no need to reinvent the wheel here. Thought it may be another way to tackle the same problem but definitely seems like the steam slayer is hard to beat in this instance. On another note though, my wife and I are in the process of working with a home designer and my wife has graciously agreed to let me have a brew room in the basement. Super excited about this by the way! However the question seems to me, which method of steam management is best. Not really concerned with the cost at this point, not saying money is no object though. I am just curious, if being able to design it from the get go, is a hood/fan ventilation to the outside method better than the steam slayer method since this can be planned for and installed from the get go?
Well, I'm convinced! Seems there is no need to reinvent the wheel here. Thought it may be another way to tackle the same problem but definitely seems like the steam slayer is hard to beat in this instance. On another note though, my wife and I are in the process of working with a home designer and my wife has graciously agreed to let me have a brew room in the basement. Super excited about this by the way! However the question seems to me, which method of steam management is best. Not really concerned with the cost at this point, not saying money is no object though. I am just curious, if being able to design it from the get go, is a hood/fan ventilation to the outside method better than the steam slayer method since this can be planned for and installed from the get go?
My local climate is just as you describe. I've always enjoyed brewing outdoors in the spring and fall, but it's often pure misery in summer and winter. That's why I'd like to have both options available. If I could only choose one, it would be the condenser, since it is good regardless of weather.I think a lot depends on the climate where you live. If you go with ventilation, you are pulling air from the outside into your room, and then exhausting it back outside. If air goes out, it must be coming in somewhere. Is that air too hot or too cold? Do you have to cool it down or heat it up?
For me, I live in an area where the summer is very humid, and the winters can get down into the low teens. The big advantage of electric brewing indoors is to eliminate the weather issues while brewing. If you are bringing that weather inside because of ventilation, then it kind of defeats the purpose in my mind. The steam slayer is a great way to avoid having to spend a lot of energy heating and cooling that make-up air.