Expansion Tank Concepts Part-2 · Expansion Tank Concepts Part-2 For HVAC Project...
Transcript of Expansion Tank Concepts Part-2 · Expansion Tank Concepts Part-2 For HVAC Project...
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Expansion Tank Concepts
Part-2
For HVAC Project Engineers/Managers
Presented By WTF
(Institute of Higher Learning)
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ASHRAE Formula – No Concepts Here!
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Air Elimination
AirControl
AIR
WATERWATER
WATER
AIR
AIR
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The Expansion Tank – What Does It Do?
4 Things: (Diaphragm/Bladder Tanks)
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The Expansion Tank – Location?
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The Basic Hydrostatic Formula
Pressuure
10 psig
23.1 Feet
2.31 Feet = 1 psi
10 psig
The Equivalence Of Pressure And
Pressure Head
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Add safety factor and
allowance for future loads
Phot
Pcold
So specifying Pcold and Phot
correctly is the goal for this discussion.
Also called [min, max], [initial, final], [fill, xxx]
1,000
45
100
0%
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StrainerBack-FlowPreventer
PressureReducingValve
Quick-FillBypass
PressureReliefValve
BuildingDomestic Cold
Water
PressureSwitchTo BMS
¾"
ShutThisOFF
Set =Fill – 10%
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0
29
psig
psig
Pump OFF – Hydrostatic Pressures
LPP
• If expansion volume was our only concern we could locate the expansion tank anywhere in the loop and it would do the job.
• But as we have seen, keeping the LPP safely positive and above any vapor pressure issues is also a key concern.
• We know that the tank should be on the pump suction.
• Either point A or B can be used. But you have to make sure that the LPP does not drop below 5 psig. (Not a system requirement – just good practice.)
A
B
Open Vent
0
29
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• Notes:
• Try to keep CHW, HW, CDW pressures under 100 psig in the system.
• If not - be very careful and check all equipment, accessories and instruments for their pressure ratings.
• Always try to incorporate a second safety relief valve. Pump discharge header is usually a good location.
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Standard Relief Valve on Copper Finned
Tube Boilers
RayPakHigher Relief Settings Available as add Option
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0
29
psig
psig
Pump OFF – Hydrostatic Pressures
LPPA
B
Open Vent
0
29
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12
12+29
psig
psig
Pump OFF - System Cold
12+29 psig
Pump Selection1,000 gpm @ 90 feet TDH (39 psi)
(= 29 psig)
• By placing the expansion tank at the LPP we have eliminated any chance of system pressures going negative or vapor flashing
• We need to check what is happening to the pressures below and see if there are any problems when the pump starts in this "cold" state and also a couple of slides down, in the "warm" state
• Note, right now the pump is OFF and the system is "cold". Maybe the chiller just recently cycled off.
• Let us work with this Pcold value of 12 psig and see how pressures look.
• Note: 5 psig for Pcold or fill pressure is probably a better choice – but there is a good chance that start-up guys will not pay attention to the scheduled values!
Pcold = 12 psig
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15
12
37
psig
psig
Pump ON - System Cold
76 psig
Pump Selection1,000 gpm @ 90 feet TDH (39 psi)
A
B C
• With pump running, there is always a pressure drop in the direction of water flow.
• Let us assume that there is a 4 psi head loss due to friction between A and B
• Point A pressure cannot change
• Point B pressure is now
= 12 + 29 – 4 = 37 psig
• Point C (with pump running)
= Point B + 39 = 76 psig
• Note that (unless the piping runs further below the 1st floor) this is also the highest pressure point in the system
(= 29 psig)
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Pcold = 12 psig
Pcold = 12 psig
Pcold = 12 psig
• For a given expansion volume and Pcold the tank size is inversely proportional to the Phot
selected.
• Therefore to avoid high pressures we increase tank size and to reduce cost and tank size we increase Phot.
• Incorrect fill pressure
Phot = 18 psig
Phot = 24 psigPhot = 36 psig
Not to any scale.P1V1 = P2V2 in action here!Where P1 and P2 are absolute pressuresFor example: 12 psig ≈ 27 psia
@ Fill @ Fill@ Fill
NetExpansionVolume
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Pump OFF - System WARM
• Hot summer weekend. The chiller pump has been OFF. Say water temp rises to 100°F
• Water expands and the expanded volume starts moving in the expansion tank – that is what the tank is there for
• Just roughly eye-balling the graphic, if the air is compressed to half its original volume, then P1V1 = P2V2 tells us that pressure will roughly double. Ignoring the formula, this makes sense intuitively. But remember these are Absolute Pressures. So 12 psig is 27 psia and 25 psig is 40 psia.
• With the pump OFF, the pump suction and discharge gages are reading 53 psig.
Phot = 24 psig24 psig
(= 29 psig)
25
24+29
psig
psig
24+29 psig
Pump Selection1,000 gpm @ 90 feet TDH (39 psi)
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Phot = 24 psig24 psig
(= 29 psig)
24
49
psig
psig88 psig
Pump Selection1,000 gpm @ 90 feet TDH (39 psi)
Pump ON - System Warm
• Warm start Monday morning
• Let us assume that there is a 4 psi head loss due to friction between A and B
• Point A pressure cannot change
• Point B pressure is now
= 24 + 29 – 4 = 49 psig
• Point C (with pump running)
= Point B + 39 = 88 psig
• Still OK, but getting high, so probably don’t want any higher Phot
even if it reduces tank size.
• Note again that the pump is indifferent ("cannot see") to the system static pressure
A
B C
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5 psig
LPP
A
29 psig
• It is OK to locate the tank at the bottom as shown, but we need to be very cautious about the following:
• The LPP must be kept above atmospheric –say 5 psig.
• The tank will be shipped with a 12 psig factory charge. The start-up tech must raise the charge with N2 to (5 + 29) psig.
• What happens if he/she doesn’t?
• The PRV is usually set at 12 psig from the factory. This setting must be raised to (5 + 29) psig.
• What happens if he/she doesn’t?
• Check to make sure relief valve setting makes sense.
• On taller buildings check fill pressure available.
• 34 psig is Pcold. When you start thinking about value to use for Phot you will realize why the top location is a better choice.
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Back to the Formula
20
Suppose in our CHW example the total system volume is:
= 1,000 gallons.
Rule of thumb for Net Expansion of water: 1% CHW 4% HW
30 GallonsTank Size =
40 psia
Tank Size =1,000 gallons x 0.01
1 - 27 psia 12 psig25 psig
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THE END