Watch air flow through the coil rows and cool down in real time, with condensate dripping below the dew point, and read off the sensible, latent, and leaving-air conditions.
Parameters
Airflow
m³/min
Airflow through the coil.
Water flow
L/min
Chilled-water flow rate (counterflow).
Inlet air temperature
°C
Dry-bulb air temperature at coil inlet.
Inlet relative humidity
%
Inlet relative humidity. Sets the dew point and whether dehumidification occurs.
Chilled-water inlet
°C
Chilled-water inlet temperature. Lower means a colder surface and more dehumidification.
UA
kW/K
Overall heat-transfer conductance (drops with fin fouling).
Results (live)
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Leaving air temp.
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Leaving RH
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Total capacity
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Sensible capacity
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Latent capacity
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Sensible heat ratio
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Water-side ΔT
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LMTD
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Bypass factor
Air cooling through the coil rows (counterflow + condensation)
Blue = cold air, orange = warm air. Condensate drips off the fins once the air falls below its dew point.
$\varepsilon$ is the counterflow effectiveness with $C_r=C_{min}/C_{max}$. $Q_{sens}$ is sensible cooling ($\dot V$ in L/s, factor 1.21 kJ/m³K), $Q_{lat}$ is latent cooling ($h_{fg}\approx2501$ kJ/kg, $w$ = humidity ratio). When the coil surface (apparatus dew point $T_{ADP}$) drops below the air dew point, condensation begins; a smaller bypass factor $BF$ drives the outlet closer to $T_{ADP}$.
What is a chilled-water coil
A chilled-water coil is a heat exchanger inside an air-handling unit (AHU) that cools air by passing it over a bundle of finned tubes carrying chilled water. Chilled water near 7 °C, produced by the chiller, flows through the coil; air touching the fins gives up heat and its temperature drops. This is sensible cooling. If the coil surface falls below the air's dew point, water vapor condenses on the fins and drains away. The heat removed during condensation is the latent (dehumidification) load, which is what lets a coil both cool and dry humid summer air.
This simulator draws, in real time, air flowing left to right through the coil rows and cooling down, while chilled water warms up in counterflow. Condensate drips off the lower fins once the air falls below its dew point, and the leaving temperature and relative humidity, total capacity (sensible + latent), water-side ΔT, LMTD, and bypass factor all update together.
Physical model and key equations
The energy balance equates the air side and water side. With air capacity rate $C_a=\dot m_a c_{pa}$ and water capacity rate $C_w=\dot m_w c_{pw}$, let $C_{min}=\min(C_a,C_w)$ and $C_r=C_{min}/C_{max}$. The counterflow effectiveness is $\varepsilon=\dfrac{1-e^{-NTU(1-C_r)}}{1-C_r e^{-NTU(1-C_r)}}$ with $NTU=UA/C_{min}$.
Sensible capacity is $Q_{sens}=1.21\,\dot V\,(T_{in}-T_{out})$ ($\dot V$ in L/s; the 1.21 factor is the volumetric heat capacity of standard air). Latent capacity follows the drop in humidity ratio, $Q_{lat}=\dot m_a\,h_{fg}\,(w_{in}-w_{out})$ ($h_{fg}\approx2501\,\mathrm{kJ/kg}$). Whether dehumidification occurs depends on whether the apparatus dew point $T_{ADP}$ (≈ coil surface temperature) is below the inlet air dew point. The bypass factor $BF=(T_{out}-T_{ADP})/(T_{in}-T_{ADP})$ measures the fraction of air that slips past the coil; the smaller it is, the closer the outlet approaches the apparatus dew point. The water temperature rise is $\Delta T_w=Q/C_w$, and the driving force is evaluated with the log-mean temperature difference (LMTD).
How to read it
In the animation, air shifts from orange toward blue as it passes the coil rows (temperature drop), and condensate appears on the lower fins once it falls below the dew point. The counterflow chilled water (arrow at the bottom) is warmest near the outlet.
In the capacity bars, compare the heights of the sensible (blue) and latent (cyan) bars, i.e. the SHR. SHR = 1 means sensible only; the lower it is, the more dehumidification dominates.
On the psychrometric chart, the direction from the inlet point to the outlet point reveals "cooling only" (horizontal left) versus "cooling plus dehumidification" (sloping down-left).
Learn chilled-water coil performance by dialogue
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Doesn't a chilled-water coil just cool the air? What's the difference between sensible and latent heat?
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Roughly: sensible heat "lowers the temperature," latent heat "condenses water vapor." Send humid 30 °C air through the coil and its temperature drops first (sensible). If the coil surface is cold enough to be below the air's dew point, droplets form on the fins and the air dries out. That drying is the latent part. In the animation, water dripping off the lower fins is the moment dehumidification happens.
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So if I raise the chilled-water temperature, does dehumidification stop?
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Exactly, that's the lever. Try raising the chilled-water inlet from 7 °C to about 12 °C. Once the coil surface (apparatus dew point) sits above the air dew point, the latent bar drops to nothing and only sensible cooling remains. In practice you do this in shoulder seasons when you don't want to dehumidify; in muggy summer you lower the water temperature to gain latent capacity.
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There's also a "bypass factor" number. What is that?
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A coil is full of gaps, so some air slips through without ever touching a fin. The bypass factor BF is a measure of that fraction. The smaller BF is, the better the air contacts the surface and the closer the outlet gets to the water temperature (more precisely, the apparatus dew point). Push the airflow too high or foul the fins, and BF rises, hurting both cooling and dehumidification. Swing the airflow slider up and you'll see the outlet temperature rise.
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How do I use water-side ΔT and LMTD when designing?
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Water-side ΔT is "how many degrees the chilled water warms before returning," which drives pipe and pump sizing; 5–8 °C is a common target. LMTD is the heat-transfer driving force, and from $Q=UA\cdot LMTD$ you can back out the required coil UA. If total capacity is short, you can increase UA (add coil rows) or lower the water temperature—try both here and compare the effect.
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Can I take this result straight as my design value?
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It's plenty for a first pass, but not the final word. Real coils vary with fin geometry and water velocity, and the apparatus dew point here is a simplified approximation. Always confirm with standards, measured data, the vendor's selection software, and a detailed psychrometric analysis. Treat this as a place to build intuition for which inputs matter.
Real-world applications
First-pass selection of AHU chilled-water coils for offices and commercial buildings (sizing required rows, UA, and water temperature).
Checking dehumidification capacity in humid summers (whether sub-dew-point cooling handles the latent load).
Diagnosing capacity loss in existing coils (separating fin fouling / UA loss from outlet-temperature rise and lost dehumidification).
Evaluating shoulder-season energy savings (the effect of raising water temperature to switch to sensible-only operation).
Common misconceptions and cautions
"Outlet temperature = water temperature" is wrong. The bypass factor and effectiveness limits always keep the outlet above the apparatus dew point. With 7 °C water, an outlet near 10 °C is normal.
Ignoring latent heat badly underestimates capacity. In humid air, latent can be nearly half the total; sizing on sensible alone leaves both the coil and the chiller short.
This is a simplified model. The apparatus dew point is a surface-temperature approximation, and air is assumed at standard density 1.2 kg/m³ and specific heat 1.006 kJ/(kg·K). Correct with measured or vendor data at high altitude, high humidity, low water velocity, or special fins.
FAQ
Start with leaving air temperature and relative humidity, plus total cooling capacity. Then read the capacity bars to see the sensible/latent split, and watch the animation of air cooling through the coil rows to find where dehumidification begins. When the coil surface drops below the air dew point, condensation (dehumidification) starts and a latent load appears.
Sensible heat lowers the air temperature (Q_s = 1.21·V̇·ΔT); latent heat condenses water vapor (Q_L = ṁ·hfg·Δw). The capacity bars show their ratio (sensible heat ratio, SHR). If the coil surface stays above the dew point, latent is zero (sensible only); below it, dehumidification lowers the SHR.
The bypass factor BF measures the fraction of air that slips past the coil without contacting it: BF = (T_out−ADP)/(T_in−ADP), where ADP is the apparatus dew point (≈ coil surface temperature). A smaller BF means the air contacts the surface more closely and the outlet approaches the ADP. Fouled fins or excessive face velocity raise BF and degrade dehumidification.
Use it for first-pass chilled-water coil selection and for diagnosing existing coils. Sweep airflow, water flow, chilled-water temperature, and UA to check whether the required leaving conditions, total capacity, and water-side ΔT are met. Final decisions still require standards, measured data, detailed analysis, and vendor limits.
How to Use
Set inlet air conditions: airflow (m³/min), inlet air temperature (°C), and inlet relative humidity (%).
Enter water-side parameters: chilled-water flow (L/min), chilled-water inlet temperature (°C), and overall conductance UA (kW/K).
Watch the animation of air cooling and condensing, then read off leaving temperature/RH, total capacity (sensible + latent), water-side ΔT, LMTD, and bypass factor. Use the presets (sensible-only / dehumidifying / high-load) to compare typical conditions.
Worked Example
Office building example: airflow 120 m³/min, inlet air 30 °C at 55% RH, water flow 80 L/min, chilled-water inlet 7 °C, UA 6 kW/K. The leaving air is about 10 °C and near saturation, sensible capacity ≈ 41 kW, latent capacity ≈ 30 kW, total ≈ 70 kW, water-side ΔT ≈ 7 K, and SHR ≈ 0.58. Raising the chilled-water inlet to 12 °C pushes the apparatus dew point above the air dew point, so latent capacity switches to zero (sensible only)—useful for deciding whether dehumidification is needed (this is a simplified ε-NTU + apparatus-dew-point model).
Practical Notes
Density correction: this model assumes air at 1.2 kg/m³ and 1.006 kJ/(kg·K). At high altitude or high humidity, density and specific heat change, so adjust the airflow conversion. Fouling lowers the real UA to 60–75% of the design value.
Latent / dehumidification: for sub-dew-point cooling, always design the coil surface temperature, dew point, latent load, and condensate drainage. The apparatus dew point here is a simplified approximation; finalize with vendor data.
Pump head check: the pump must overcome coil-side plus piping-system pressure drop at the chosen water flow. Target a water-side ΔT of 5–8 K.