Hello Aaron,
Because the drastic change happens at lower tank levels and higher temperatures, and a vortex breaker did not correct, I recommend evaluating the Net Positive Suction Head
required for this pump. Obtain this value from manufacturer, in feet of fluid being pumped. Next, determine the Net Positive Suction Head
available during your operating conditions.
To maintain prime in a common centrifugal pump, the NPSH Available must exceed NPSH Required. When it does not, fluid in the suction & impeller will vaporize, and performance deteriorates with cavitation. Unfortunately, this one as reliable as gravity.
From memory, with personal notations:
the basic equation for determining Available NPSH is: NPSH
A = H
s + H
h - H
f - H
v.
H
s is absolute pressure at supply tank liquid
surface, in feet. If tank is vented, then = 1 atmosphere, or 33'.
H
h is static
elevation difference between 1) supply tank liquid surface lowest level, and 2) the pump suction.
This number scales with relative physical brewery size, may range from 1' - 20'.
H
f is dynamic,
frictional head loss in suction piping between supply tank and pump suction. In properly designed & maintained systems, this is small, i.e., 4'. Frictional losses increase with flow rate. H
f is impacted when suction piping is modified, or obstructed.
H
v ,,absolute
Vapor pressure of water. At 170 deg F, is 14'. An aspect of higher temperature fluids working against our pumping interests.
a hypothetical example:
NPSH
A = H
s + H
h - H
f - H
vNPSH
A = 33' + 2' - 5' - 14' = 16' Hence, Pump Manufacturer Requirement, NPSH
R should be
less than 16'.
Many, MANY problems in brewery pumping systems involve NPSH.
Centrifugal pump manufacturers offer helpful references to explain the hydraulics involved in this critical assessment, which should always be done during design phase. And your local equipment representative should be qualified to assist with the analysis.
Good hunting,
David
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David Ammons, PE
Brewing Process Engineer, Retired
Saint Louis MO
ammfamd2@gmail.com------------------------------
Original Message:
Sent: 12-09-2022 16:46
From: Aaron Dahl
Subject: Hot liquor pump pressure loss
All,
I have a pump problem (shocking) that I have been dealing with/living with for several months now, and I'm hoping to find a remedy for it after trying everything to eliminate this ghost in the machine. My hot liquor pump consistently loses pressure during sparging/knockout loop sterilization, when water temperature has increased and hot liquor volume has decreased. The pump behaves fine during vessel rinsing and mash in, but once I've increased the temp of the hot liquor for sparging (170) it gradually loses pressure until the flow out of the sparge is barely a trickle. Looking at the pump curve, like most pumps there is a loss of pressure with increased temperature, but this is an incredibly drastic condition. After I've completed wort knockout, and the water volume in the hot liquor tank has increased, full pressure resumes during final vessel rinsing. The water temp has decreased at this point and usually lands around 160.
I've replaced the seal kit on the pump, tightened and reseated every connection to and from the pump to eliminate any air being pulled in, removed the check valve (piping into brewhouse passes through two) on the brewhouse side, and installed a vortex breaker on the drain of the HLT to help eliminate any vortexes being pulled into the pump. I've talked to the brewhouse manufacturer (BrauKon), pump manufacturer (Grundfos), local service provider for the pump, and about every brewer in town about this issue, and nothing we have tried has solved this problem.
Any ideas would be greatly appreciated, thanks for any help!
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Aaron Dahl
Head Brewer
Golden Age Beer
Homestead, PA
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