Hi Guys,
Ive scored 4 large SS304 pots, 0.9m diameter x 1.2m high am im planning on building a big ass brew system out of them.
Ive got a couple of questions about design and lautering i wanted to run past everyone and see what options are actually available vs steaming ahead with a build reminiscent of a typical home brew setup and causing myself a headache in a few months time when i fire it up.
My original plan was a 3V Herms system with the Herms being in a separate smaller vessel for efficiency, however my calcs lead to believe ramp time with this will just be ridiculous unless i pack in 36KW+ into the Herms loop. The other options would be to use the kettle as a Rims system or K-Rims and use the elements already installed (ULWD of course) to ramp.
Im also slightly concerned about compacting the grain bed at this scale. Assuming 75% efficiency for the following %ABV beers on a 500L batch would result in a false bottom loading of:
5% - 100kg - 157kg/m2
6% - 120kg - 189kg/m2
7% - 140kg - 220kg/m2
This seems ideal considering that a "rule of thumb" is 140-250kg/m2 loading. But this would be for a pro brewer setup without recirculation, except prior to sparge to clear the grain bed. From the info i have read a wort velocity of 7-11mm/min seems a good rate to start the runoff without compacting the grain bed.
If i were to go with a Herms or Rims and recirculate, on this system with the tanks shaped how they are would result in 1L of liquid occupying 0.157cm of vertical space, so if you were to run off 5l/min that would be 7.9mm of wort per minute moving through the grain bed. Not exactly prime recirculation rate inorder to ramp temperature. Once you've set the bed the velocity could be increased quite a bit and avoid channeling etc, i just dont know to what extent as my only experience is HB and im pretty sure things dont scale linearly.
Just wondering if anyone has experience with recirculation at this scale, is it possible, potential issues, tell me its a terrible idea and its not even required?? For whatever reason, probably because my first system was a Herms and i do step mashing quite a bit, especially with raw wheat i seem to be attached to the idea of a similar system just at a larger scale.
Im still toying with the 3V system but just doing single infusion mashes while heating sparge water in the BK to 78 before transferring to the HLT to sparge. i would then recirculate at a slow rate to clear the grain bed before sparging. Cant see a problem with this.
Another hair brained idea is to make 2 x 2V K-Rims systems, though this would result in a lower efficiency, requiring more grain, and a greater loading on the false bottom meaning a greater chance of compacting the grain bed.
Thanks for the info, ill be sure to post up progress as this thing proceeds.
Cheers,
Ive scored 4 large SS304 pots, 0.9m diameter x 1.2m high am im planning on building a big ass brew system out of them.
Ive got a couple of questions about design and lautering i wanted to run past everyone and see what options are actually available vs steaming ahead with a build reminiscent of a typical home brew setup and causing myself a headache in a few months time when i fire it up.
My original plan was a 3V Herms system with the Herms being in a separate smaller vessel for efficiency, however my calcs lead to believe ramp time with this will just be ridiculous unless i pack in 36KW+ into the Herms loop. The other options would be to use the kettle as a Rims system or K-Rims and use the elements already installed (ULWD of course) to ramp.
Im also slightly concerned about compacting the grain bed at this scale. Assuming 75% efficiency for the following %ABV beers on a 500L batch would result in a false bottom loading of:
5% - 100kg - 157kg/m2
6% - 120kg - 189kg/m2
7% - 140kg - 220kg/m2
This seems ideal considering that a "rule of thumb" is 140-250kg/m2 loading. But this would be for a pro brewer setup without recirculation, except prior to sparge to clear the grain bed. From the info i have read a wort velocity of 7-11mm/min seems a good rate to start the runoff without compacting the grain bed.
If i were to go with a Herms or Rims and recirculate, on this system with the tanks shaped how they are would result in 1L of liquid occupying 0.157cm of vertical space, so if you were to run off 5l/min that would be 7.9mm of wort per minute moving through the grain bed. Not exactly prime recirculation rate inorder to ramp temperature. Once you've set the bed the velocity could be increased quite a bit and avoid channeling etc, i just dont know to what extent as my only experience is HB and im pretty sure things dont scale linearly.
Just wondering if anyone has experience with recirculation at this scale, is it possible, potential issues, tell me its a terrible idea and its not even required?? For whatever reason, probably because my first system was a Herms and i do step mashing quite a bit, especially with raw wheat i seem to be attached to the idea of a similar system just at a larger scale.
Im still toying with the 3V system but just doing single infusion mashes while heating sparge water in the BK to 78 before transferring to the HLT to sparge. i would then recirculate at a slow rate to clear the grain bed before sparging. Cant see a problem with this.
Another hair brained idea is to make 2 x 2V K-Rims systems, though this would result in a lower efficiency, requiring more grain, and a greater loading on the false bottom meaning a greater chance of compacting the grain bed.
Thanks for the info, ill be sure to post up progress as this thing proceeds.
Cheers,
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