This week I reviewed an energy model that looked fine at first glance.
Reports were clean. 23% Savings looked decent. No obvious red flags.
But once I opened the plant, I found something that shows up more often than most teams realize:
The model was running on a default chiller curve.
And that one “quiet” default turned into a meaningful result once we corrected it — and then took the review one layer deeper.
Most modeling software will let you run a chiller plant using generic/default performance curves.
The model doesn’t crash. The reports don’t complain. The project team moves forward.
The problem is that chillers rarely spend most of their operating hours at full load. A large portion of annual energy is accumulated at part-load, where the curve shape matters a lot.
So when the curve is generic, the energy is generic, and the savings can be distorted in either direction.
In this case, the default curve was undercounting the savings that the actual chiller could deliver.
First, we replaced the default curve with the official manufacturer performance data (normalized for modeling).
That alone improved the model results by about 4%.
This is the point where many teams stop and take the win.
But the truth is: correcting curves often reveals a second layer.
Because once the equipment performance is realistic… controls matter more.

(Illustration: default curve vs manufacturer curve — normalized. Not an exact submittal.)
Even in a simplified view, you can see the point:
Curve shape drives part-load energy. And part-load drives annual energy.
After the curve swap, we checked one more thing:
Sequencing / staging logic.
This is where a lot of “plant savings” fall apart, not because the equipment is wrong, but because the plant is effectively being simulated as if it’s operating in a way that would never happen in real life.
Once we updated sequencing to match realistic operation at part load, the results improved again.
Total outcome after both changes:
✅ 30% savings over the Baseline (+~7% improvement)
That’s the two-step pattern I see constantly:
Plant modeling issues are dangerous because they often:
But reviewers (and experienced QA reviewers) know where these mistakes hide.
And even when the reviewer doesn’t call it out directly, fragile plant assumptions often collapse under scrutiny when:
The goal isn’t to “optimize a model.”
The goal is to produce savings that are both:
If you’re modeling chillers, these are some of the highest-value areas to QA:
The trap is that everything can look fine… right up until someone experienced opens the plant.
This exact issue is what our Second-Look Model Review is designed to catch:
defaults and plant assumptions that don’t show up in the reports but quietly drive the outcome.
If you’d like a targeted plant QA review (or help tightening your modeling assumptions to be reviewer-safe), reach out here:
Bob Fassbender is the founder of Energy-Models.com and Fassbender Energy Advisory. A former Trane software engineer and instructor, Bob has more than 20 years of experience in energy modeling, building performance, utility incentives, and energy strategy. His work spans whole-building energy modeling, calibration, independent technical review, decarbonization planning, utility incentive strategy, renewable energy analysis, and owner advisory services. Bob has supported projects ranging from commercial buildings and utility programs to large-scale data center developments involving power infrastructure, geothermal systems, heat recovery, and long-term energy planning. Through Energy-Models.com, Bob has trained thousands of energy professionals in eQUEST, OpenStudio, EnergyPlus, LEED modeling, and building performance analysis. He continues to advise owners, engineers, architects, and developers on energy-related decisions while exploring emerging technologies such as artificial intelligence, machine learning, and advanced building analytics.
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