[Equest-users] using IPLV in eQuest
Paul Diglio
paul.diglio at sbcglobal.net
Fri Feb 25 10:44:17 PST 2011
Actually what everyone is calling dt is more accurately referred to as lift. It
is the difference between the saturated evaporating temperature and the
saturated condensing temperature, which is different than the condenser water
temperature and the evaporator water temperature.
A more accurate curve can be built if you have the chiller manufacturer model
both these variables for you, rather than leaving the evaporator water
temperature constant and just varying the condenser water temperature. Any
change in the evaporator pressure will effect the condensing pressure and any
change in the condensing pressure will effect the evaporator pressure.
Paul
________________________________
From: Nick Caton <ncaton at smithboucher.com>
To: James Waechter <jamesw at McKinstry.com>; equest-users at lists.onebuilding.org
Sent: Fri, February 25, 2011 1:21:42 PM
Subject: Re: [Equest-users] using IPLV in eQuest
James etal,
Rohini will need to create performance curves to make this particular
comparison. Otherwise using the default curves will result in identical part
load performances.
The following is excerpted from the following (short) recommended reading
concerning what IPLVmeans:
http://ashrae-cfl.org/2010/03/understanding-iplvnplv/
IPLV (or NPLV) = 0.01A+0.42B+0.45C+0.12D
Where:
A = COP or EER @ 100% Load
B = COP or EER @ 75% Load
C = COP or EER @ 50% Load
D = COP or EER @ 25% Load
John is saying knowing only the IPLV and the 100% load condition efficiency
(variable ‘A,’ above) is not enough information to extrapolate the IPLV curves
to compare the two chillers.
For the exercise of comparing the two non-centrifugal chillers of the same
technology/type, I would just focus on making a custom EIR-FPLR (not
EIR-fPLR&dT) for each chiller, and use the library CAP-FT AND EIR-FT curves. My
understanding is the effects of temperature on capacity and EIR outside of
centrifugal VSD chillers is negligible. NOTE: Whenever using any of the
default library chiller performance curves, that means you MUST normalize to and
specify the chiller at ARI conditions – those curves aren’t normalized to
anything else.
So! If you can find the IPLV A, B, C and D values for both chillers’ curves,
you could come up with your EIR-FPLR curve coefficients (curve type = quadratic
or cubic) using a curve-fit in excel… or alternatively make eQuest figure the
coefficients by entering those points as raw data.
You may more easily just make your own curves, following John’s advice and
getting part load unloading curves (100%, 90%, 80%... etc) held at a constant
chilled & condenser temperature to match the ARI* conditions (85CWT if this is
water cooled) at which you’re specifying the chiller capacity/EIR. Again, you
could either go into excel, normalize the data (review DOE2 help entry for
EIR-FPLR), make a scatter chart, and get the coefficients using a curve fit… or
enter the data as raw points into eQuest and the coefficients will be figured by
eQuest… whatever makes more sense to you.
For others and personal future reference…. If you are looking to make an
EIR-fPLR&dT curve (for centrifugal chillers or otherwise): Ask your rep instead
for multiple (minimum 3) part load unloading runs, holding the delivered chilled
water temp constant, and vary the condenser water temperature incrementally for
each run (i.e. 85, 75, 65). Choose a range of CWT’s that cover the anticipated
range to be encountered in the actual design. This will get you enough data to
have the minimum 3 delta-T’s represented in your part load data points to build
this curve correctly. You’ll be using eQuest “raw-data” entry method to make it
generate the coefficients.
~Nick
* Rather than ARI conditions (85F CWT), you could be normalizing to Design
condition EIR/CAP, provided you’re making a full set of custom curves in the
same fashion.
NICK CATON, E.I.T.
PROJECT ENGINEER
Smith & Boucher Engineers
25501 west valley parkway
olathe ks 66061
direct 913 344.0036
fax 913 345.0617
www.smithboucher.com
From:equest-users-bounces at lists.onebuilding.org
[mailto:equest-users-bounces at lists.onebuilding.org] On Behalf Of James Waechter
Sent: Friday, February 25, 2011 10:55 AM
To: equest-users at lists.onebuilding.org
Subject: Re: [Equest-users] using IPLV in eQuest
John,
If the only parameter Rohini enters into the program is the full-load EIR –
which he said is the same for both chillers – how will eQuest know to bend the
curves differently for the two chiller options. It is my understanding that
program would use the same chiller efficiency curves for both machines even
though their IPLVs are different.
In order to overcome this issue, are you saying Rohini should get chiller
performance data from each of the manufacturers and enter his own custom
curves? I recall there was a discussion on that topic a few months back.
Regards,
James Waechter Jr., P.E., CEM, LEED A.P.
Energy Engineer – Rocky Mountain Region
p 303 215 4062 | m 727 686 3248
McKinstry
Consulting | Construction | Energy | Facility Services
www.mckinstry.com
From:equest-users-bounces at lists.onebuilding.org
[mailto:equest-users-bounces at lists.onebuilding.org] On Behalf Of John Aulbach
Sent: Friday, February 25, 2011 9:41 AM
To: R B; eQUEST Users List
Subject: Re: [Equest-users] using IPLV in eQuest
Rohini:
Won't happen. IPLV is a number which has one equation and 4 unknowns. Actually,
three unknowns as you know the 100% point. You need a manufacturer's curve run
at 85F constant condenser water temperature. Let eQuest do the curve bending
after that. ARI curve won't work right.
John R. Aulbach, PE, CEM
Senior Energy Engineer
________________________________
PartnerEnergy
1990 E. Grand Avenue, El Segundo, CA 90245
W: 888-826-1216, X254| D: 310-765-7295 | F: 310-817-2745
www.ptrenergy.com| jaulbach at ptrenergy.com
________________________________
From:R B <slv3sat at gmail.com>
To: eQUEST Users List <equest-users at lists.onebuilding.org>
Sent: Fri, February 25, 2011 7:25:18 AM
Subject: [Equest-users] using IPLV in eQuest
Hi All,
I would like to compare two screw chillers with same full load kW/ton and
different IPLV kW/ton. I am using the full load number for the EIR. Where can
the IPLV number be used? Is there some way to scale the performance curves to
reflect different IPLV's?
-Rohini
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