Centrifuge DO issue and lack of clarity can be driven by many factors.
One challenge with the question is the model HB centrifuge was not mentioned and the different models have different capacities. Another challenge is the inlet turbidity was mentioned in NTU which is a turbidity unit but normally we would think of machine capacity in % volumetric solids. Different materials can increase inlet turbidity without increasing percent solids (think oats used in the brewhouse or glycogen haze from poor yeast health). Finally, even the same model machine can come with a short, medium or long disc stack changing the machine performance and comparability.
Another interesting item to understand is does the machine start up well and then loses clarity over the run (assuming steady incoming solids). Another thing to explore while having issues is if three or four full size shots in a row (as fast as possible) recover the performance of the machine?
Because of all these factors I am assuming the machine used to perform well and that the inlet solids have not changed.
Here is a list of points to consider in rough likelihood:
1) Solids plugging the disc stack reducing surface area
a. Too many root cause drivers to list…so after CIP open machine and inspect disc stack and if indeed solids are still present then can pursue this issue further
2) Improper machine assembly after overhaul or maintenance or failed seal that is letting inlet beer mix with clarified beer
3) Improper rpm (not likely)
In regards to DO pick up issues again a list in rough order of likelihood (ignoring issues outside the machine):
1) Running slower than machine design will cause cavitation in the paring disc due low inlet pressures which allows the hydro hermetic seal water and then air to enter the process flow raising the beer DO
a. This can be offset to a degree (with limits) by varying the outlet pressure to keep the liquid in the paring disc on the "pump curve"
b. Your supplier should be able to provide the pump curve for your machine so you are aware of the limitations
c. One note, in my experience seal water on hydro-hermetic machines is not normally deaerated water but of course confirm with your manufacturer what you should use
i. If deaerated water is not required by the manufacturer but a brewer finds it helps lower DO then it is likely the machine is being operated in a manner that seal water is being drawn into the process flow
2) Insufficient CO2/N2 purge around the bowl
3) Insufficient seal water flow
4) Damage to the paring disc due to long term cavitation exposure (months) leading to less pumping capacity and changing the pump curve leading to DO pick up
5) Bad seals allowing oxygen in
Hope this helps and reach out if you need any help.
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Travis Audet
Slant Six Consulting
Hooksett NH
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Original Message:
Sent: 01-07-2024 14:24
From: Jason Brenden
Subject: centrifuge operation
Hey All,
Looking for some help trouble shooting a few issues with our GEA westfalia hb centrifuge. Overall, it seems to run much slower than it should, usually around 10bbl/hour to get NTU output of ~75, has variable DO pick up and would also like to hit some lower NTUs.
I didn't work here during the instal of this machine and have never ran one before. The current procedure for everyone has been to just run the preset recipes that got set up during instal but we are looking to improve the operation of it. We've been having a really hard time getting help from our supplier so figured I'd start here.
Anyone who could help shed some light on this would be much appreciated. Right now we are running most beers with an inlet NTU of ~200, bowl speed of ~8,000 RPM and outlet NTU of ~75. This gets us about 10-13bbl/hr.
Maybe this is normal? DO can jump from 20ppb to 100+ depending on the day and we aren't sure why. Going to look into CO2 in solution coming out of the fermenter to see if that effects it.
Thank You!
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Jason Brenden
Head Brewer/Director of Operations
Bridger Brewing
Bozeman MT
(218) 256-1132
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