Cooling coil in an AHU: capacity and dehumidification calculation

How to design a cooling coil in an air handling unit. Calculating the cooling capacity, dehumidification, dew point and the air state after the coil.

The cooling coil in an air handling unit (AHU) cools the supply air below its dew point — condensing out the excess moisture and draining it away as condensate. The total cooling capacity is the sum of the sensible and latent heat: Φc=m˙(h1h2)\Phi_c = \dot{m} \cdot (h_1 - h_2), where h1h_1 and h2h_2 are the air enthalpies before and after the coil.

The principle of cooling with dehumidification

The air enters the coil at temperature t1t_1 and relative humidity φ1\varphi_1. The coil cools it through the dew point (tdt_d) to the outlet temperature t2t_2:

  1. Sensible cooling — a drop in temperature with no change in humidity, until the air reaches its dew point
  2. Latent cooling (dehumidification) — below the dew point the water vapor condenses, and the humidity ratio xx falls
  3. Outlet state — the air leaves the coil saturated (φ295100%\varphi_2 \approx 95\text{–}100\%) or is subsequently reheated to the required temperature

The principle of cooling without dehumidification

If the outlet temperature t2t_2 stays above the dew-point temperature, no condensation occurs — the air is merely cooled.

  1. Sensible cooling — a drop in temperature with no change in humidity, until the air reaches its dew point
  2. Outlet state — the air leaves the coil more saturated than at the inlet

Calculating the cooling capacity

Total cooling capacity

Φc=m˙(h1h2)[kW]\Phi_c = \dot{m} \cdot (h_1 - h_2) \quad \text{[kW]}

where m˙\dot{m} is the air mass flow rate [kg/s].

The sensible component

Φs=m˙cpa(t1t2)m˙1.006(t1t2)[kW]\Phi_s = \dot{m} \cdot c_{pa} \cdot (t_1 - t_2) \approx \dot{m} \cdot 1.006 \cdot (t_1 - t_2) \quad \text{[kW]}

The latent component (dehumidification)

Φlat=m˙r0(x1x2)m˙2501(x1x2)[kW]\Phi_{lat} = \dot{m} \cdot r_0 \cdot (x_1 - x_2) \approx \dot{m} \cdot 2501 \cdot (x_1 - x_2) \quad \text{[kW]}

where r0=2501 kJ/kgr_0 = 2501\ \text{kJ/kg} is the latent heat of water at 0 °C.

Condensate flow

qcond=m˙(x1x2) [kg/s]=m˙(x1x2)3600 [l/h]q_{\text{cond}} = \dot{m} \cdot (x_1 - x_2)\ \text{[kg/s]} = \dot{m} \cdot (x_1 - x_2) \cdot 3600\ \text{[l/h]}

A worked example

Given: an AHU, flow rate 3000 m³/h, coil inlet: t1t_1 = 32 °C, φ1φ_1 = 55%, outlet: t2t_2 = 14 °C, φ2φ_2 = 95%.

Psychrometric values:

  • Air density: ρ1.145 kg/m3\rho \approx 1.145\ \text{kg/m}^3m˙=300036001.145=0.955 kg/s\dot{m} = \frac{3000}{3600} \cdot 1.145 = \mathbf{0.955}\ \textbf{kg/s}
  • h1h_1 (32 °C, φ 55%): 74.6 kJ/kg\approx \mathbf{74.6}\ \textbf{kJ/kg}
  • h2h_2 (14 °C, φ 95%): 38.1 kJ/kg\approx \mathbf{38.1}\ \textbf{kJ/kg}
  • x116.6 g/kgx_1 \approx 16.6\ \text{g/kg}, x29.5 g/kgx_2 \approx 9.5\ \text{g/kg}

Results:

  • Total capacity: Φc=0.955(74.638.1)=34.9 kW\Phi_c = 0.955 \cdot (74.6 - 38.1) = \mathbf{34.9}\ \textbf{kW}
  • Sensible capacity: Φs=0.9551.006(3214)=17.3 kW\Phi_s = 0.955 \cdot 1.006 \cdot (32 - 14) = \mathbf{17.3}\ \textbf{kW}
  • Latent capacity: Φlat=0.955250116.69.51000=17.0 kW\Phi_{lat} = 0.955 \cdot 2501 \cdot \dfrac{16.6 - 9.5}{1000} = \mathbf{17.0}\ \textbf{kW}
  • Condensate: 0.9557.110003600=24.4 l/h0.955 \cdot \dfrac{7.1}{1000} \cdot 3600 = \mathbf{24.4}\ \textbf{l/h}

Sensible heat ratio (SHR)

The SHR (Sensible Heat Ratio) gives the share of the total cooling capacity that is sensible cooling:

SHR=ΦsΦc=17.334.9=0.50\text{SHR} = \frac{\Phi_s}{\Phi_c} = \frac{17.3}{34.9} = \mathbf{0.50}

Typical values:

  • Offices: SHR = 0.75–0.85 (low internal latent-heat production)
  • Restaurants, pools: SHR = 0.45–0.65
  • Tropical climate: SHR = 0.50–0.65

The temperature after the coil (bypass factor)

A real coil never cools all the air exactly to the surface temperature of the exchanger. The bypass factor (BF) = the fraction of air that passes through the coil without contact:

t2=tADP+BF(t1tADP)t_2 = t_{\text{ADP}} + \text{BF} \cdot (t_1 - t_{\text{ADP}})

where tADPt_{\text{ADP}} is the apparatus dew point temperature — the surface temperature of the exchanger.

The BF for a finned exchanger is typically 0.05–0.15. On the Mollier diagram, the outlet-air state lies on the line connecting the state t1t_1, φ1\varphi_1 with the saturation curve — the distance corresponds to the BF.

Cooling on the Mollier diagram

On the h-x diagram:

  1. Plot the inlet air state (point 1)
  2. Draw a line to the left toward the saturation curve — point 2’ is the ideal outlet (BF = 0)
  3. The actual outlet (point 2) lies on the segment 1–2’ at a distance BF from the saturation curve

You can also work the construction through by hand — a blank sheet to print draws the saturation curve at 0.5 mm, so it is easy to aim at with a ruler. PsychroView performs this calculation automatically once you enter the inlet state and the outlet temperature or enthalpy.

Frequently asked questions

How do I find the cooling capacity I need? The cooling capacity is set by the room’s heat gains (sun, people, luminaires, equipment) plus the heat brought in by ventilation. For a standard office, reckon on 60–100 W/m² of total cooling capacity.

Why is the coil outlet saturated air? The coil cools the air below its dew point — moisture condenses and the air approaches saturation. Downstream of the coil the air is typically φ = 90–100% and relatively cold (12–16 °C), which is why a reheater is usually placed after the coil.

What is a chilled-water coil and a DX coil? Chilled-water coil (CW) — cold water (typically +6/+12 °C) from a central cooling source (a chiller) flows through the fins. DX coil (direct expansion) — refrigerant evaporates in the fins directly from a compressor unit.

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Keywords: air cooling AHU, cooling coil capacity, air dehumidification, HVAC cooling coil, SHR calculation