[Equest-users] Chiller curve ball
Paul Diglio
paul.diglio at sbcglobal.net
Wed Mar 9 17:19:47 PST 2011
Vikram:
When defining a screw compressor in eQuest, I see three curves required.
1. EIR f(CHWT & ECT) which is the energy input ratio as a function of the
evaporator leaving water temperature and the condenser water entering
temperature. This is called lift. eQuest calls this DT.
2.Cap f(CHWT & ECT) which is the capacity as a function of lift.
3.EIR f(PLR & DT) which is the energy input ratio as a function of the part load
ratio and the DT or chiller lift.
Creating a performance curve using the temperature difference between the
condenser water entering and leaving temperature is incorrect. I think you
realize this because your chiller energy went up 30%.
If you are modeling a constant chilled water supply temperature you can plug
that in as Independent 1 and use the condenser entering water temperature as
Independent 2. If your chilled water temperature will be reset based on
terminal load or outside air temperature, then you would need to get the chiller
modeled by the manufacturer.
Paul Diglio
________________________________
From: "Sami, Vikram" <Vikram.Sami at perkinswill.com>
To: "equest-users at lists.onebuilding.org" <equest-users at lists.onebuilding.org>
Sent: Wed, March 9, 2011 6:54:13 PM
Subject: [Equest-users] Chiller curve ball
Ok – so I’m probably doing this all wrong.
I am trying to model a York scroll chiller in EQUEST. The table below
illustrates the Part Load rating Data
Load % Capacity (Tons) Cond. EWT (°F) Cond. LWT (°F) Compressor kW
EER COP EIR
100 135.8 85 95 104.1 15.6 4.6 0.217391
83.3 116.8 79.4 87.9 81 17.3 5.1 0.196078
66.7 96.9 73.5 80.4 60.1 19.3 5.7 0.175439
50 73.5 66.7 71.8 41.7 21.2 6.2 0.16129
33.3 48.2 65 68.4 26.6 21.7 6.4 0.15625
16.7 23.6 65 66.6 13.1 21.7 6.4 0.15625
eQUEST doesn’t seem to have a scroll chiller option – I assume screw is the
closest thing to it.
As far as I can tell – you need to define 3 performance curves:
1. A curve that defines the EIR based on the condenser water temp
"York - Temp vs EIR" = CURVE-FIT
TYPE = BI-QUADRATIC-T
INPUT-TYPE = DATA
INDEPENDENT-1 = ( 85, 79.4, 73.5, 66.7, 65, 65 )
INDEPENDENT-2 = ( 95, 87.9, 80.4, 71.8, 68.4, 66 )
DEPENDENT = ( 0.217391, 0.196, 0.175, 0.161, 0.156, 0.156 )
..
2. A curve that defines the part load based on the condenser water temp
"York Temp vs Part Load" = CURVE-FIT
TYPE = BI-QUADRATIC-T
INPUT-TYPE = DATA
INDEPENDENT-1 = ( 85, 79.4, 73.5, 66.7, 65, 65 )
INDEPENDENT-2 = ( 95, 87.9, 80.4, 71.8, 68.4, 66 )
DEPENDENT = ( 1, 0.833, 0.667, 0.5, 0.333, 0.167 )
..
3. A curve that defines the EIR based on the part load.
"York Part Load vs EIR" = CURVE-FIT
TYPE = QUADRATIC
INPUT-TYPE = DATA
INDEPENDENT = ( 1, 0.833, 0.667, 0.5, 0.333, 0.167 )
DEPENDENT = ( 0.217, 0.196, 0.175, 0.161, 0.156, 0.156 )
..
When I apply these curves to my chiller, my cooling energy goes up by 30%. Seems
like a lot. Is this reasonable or am I doing something wrong with my curve
selection?
Muchas Gracias in advance
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