Thank you all for your responses and your time. My primary error was simple… not including the PLR factor itself within the curve. Your comments greatly increased my understanding of how the chiller and boiler plant are modeled - I'm glad that I made the error so I could learn so much. I will now pay close attention to the condenser loop reset strategy when modeling a chiller VSD (for example).
Taylor
________________________________________________________
Taylor Keep
Mechanical, LEED® AP
Arup
901 Market Street Suite 260
San Francisco, CA 94103
tel: 415 946 0279
fax: 415 957 9096
taylor.keep@xxxxxxxx
www.arup.com
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