Drawing No. EH–TH–024 // Thermal Engineering & HVAC
HVAC Formula Sheet
A practical HVAC reference connecting envelope transmission, airflow, psychrometrics, moisture control, ventilation, fan power and equipment efficiency. Mass-based moist-air equations are emphasized because air density and psychrometric properties vary with pressure, temperature and humidity.
Fast reference, with engineering context
Use the equations directly for screening calculations, then open the linked EngineerHub tools for input handling and unit conversion. Formula applicability and major limitations are stated beside each relation.
Reference conventions
Room sensible and latent heat balance
01 // Envelope transmission heat
For steady transmission through an assembly represented by an overall U-factor, heat flow is proportional to area and temperature difference.
| Symbol | Meaning | SI units | US customary |
|---|---|---|---|
| q̇ | Transmission heat rate | W | Btu/h |
| U | Overall assembly U-factor | W/(m²·K) | Btu/(h·ft²·°F) |
| A | Assembly area | m² | ft² |
| ΔT | Indoor-outdoor temperature difference | K | °F |
Worked example — winter wall transmission
Given: U = 0.35 W/(m²·K), A = 120 m², indoor-outdoor ΔT = 25 K.
US check: ≈3583 Btu/h.
This is transmission only; infiltration, ventilation, thermal bridges and internal/solar gains are separate.
For dynamic cooling loads, thermal storage and solar/radiant effects matter. ASHRAE heat-balance or RTS methods are more complete than steady UAΔT.
02 // Sensible heat carried by air
For a known dry-air mass flow, the sensible heat associated with a dry-bulb temperature change is approximated with moist-air specific heat.
| Symbol | Meaning | SI units | US customary |
|---|---|---|---|
| ṁda | Dry-air mass flow | kgda/s | lbda/h |
| cp,ma | Moist-air heat capacity per kg dry air | kJ/(kgda·K) | Btu/(lbda·°F) |
| W | Humidity ratio | kgw/kgda | lbw/lbda |
| ΔT | Dry-bulb temperature change | K | °F |
Worked example — cooling supply air sensibly
Given: ṁda = 1.5 kg/s, cp ≈ 1.006 kJ/(kg·K), ΔT = 12 K.
US check: ≈61,800 Btu/h.
For precision, use the actual moist-air state instead of a fixed volumetric ‘air factor’.
ASHRAE also publishes convenient standard-air volumetric factors, but mass-based calculation is more accurate when altitude or temperature differs significantly from standard conditions.
03 // Total moist-air heat
The total heating/cooling rate of an airstream follows directly from the moist-air enthalpy difference.
| Symbol | Meaning | SI units | US customary |
|---|---|---|---|
| h | Moist-air enthalpy | kJ/kgda | Btu/lbda |
| ṁda | Dry-air mass flow | kgda/s | lbda/h |
| V̇ | Moist-air volume flow | m³/s | cfm |
| v | Specific volume per dry air | m³/kgda | ft³/lbda |
| q̇t | Total heat rate | kW | Btu/h |
Worked example — cooling a moist-air stream
Given: ṁda = 1.5 kg/s; entering h₁ = 60 kJ/kgda; leaving h₂ = 42 kJ/kgda.
US check: ≈92,100 Btu/h.
Use a consistent psychrometric enthalpy reference within one unit system.
Cooling below dew point also removes condensate. A complete coil energy balance may include the enthalpy of drained condensate.
04 // Humidity ratio from vapor pressure
At a known total pressure, humidity ratio follows from water-vapor partial pressure.
| Symbol | Meaning | SI units | US customary |
|---|---|---|---|
| W | Humidity ratio | kgw/kgda | lbw/lbda |
| pw | Water-vapor partial pressure | Pa or kPa | psia |
| p | Total absolute pressure | Pa or kPa | psia |
| φ | Relative humidity | fraction or % | fraction or % |
| pws | Saturation vapor pressure at dry bulb | Pa or kPa | psia |
Worked example — 25°C and 50% RH at sea-level pressure
Given: Tdb = 25°C, RH = 50%, pws ≈ 3.1692 kPa, p = 101.325 kPa.
Use local station pressure for altitude-sensitive psychrometrics.
Relative humidity alone does not identify moisture content; the same RH at different temperatures corresponds to different humidity ratio and dew point.
05 // Cooling and dehumidification moisture removal
The water removed from an airstream follows directly from the humidity-ratio reduction.
| Symbol | Meaning | SI units | US customary |
|---|---|---|---|
| ṁw | Condensate / moisture-removal rate | kg/s | lb/h |
| ṁda | Dry-air mass flow | kg/s | lb/h |
| W₁,W₂ | Entering/leaving humidity ratio | kg/kgda | lb/lbda |
| hfg | Approx. vaporization enthalpy | kJ/kg | Btu/lb |
Worked example — dehumidifying an airstream
Given: ṁda = 1.5 kg/s, W₁ = 0.012, W₂ = 0.008 kg/kgda.
Use the full moist-air/condensate enthalpy balance for accurate coil duty.
The 2500 kJ/kg latent approximation is convenient but not a substitute for a psychrometric energy balance when coil leaving conditions and condensate temperature matter.
06 // Air changes per hour
ACH normalizes ventilation or infiltration flow to the room volume.
| Symbol | Meaning | SI units | US customary |
|---|---|---|---|
| ACH | Air changes per hour | h⁻¹ | h⁻¹ |
| V̇ | Volumetric airflow | m³/s | cfm |
| Vroom | Room volume | m³ | ft³ |
Worked example — ventilating a 250 m³ room
Given: V̇ = 0.25 m³/s and room volume = 250 m³.
US check: 0.25 m³/s ≈ 530 cfm.
ACH is a volumetric turnover metric; it does not directly measure contaminant-removal effectiveness.
Outdoor-air requirements may be based on occupancy, floor area, contaminant generation or code-prescribed minimums rather than ACH alone.
07 // Fan / air-moving power
Ideal air power is pressure rise times volumetric flow; divide by fan/system efficiency for shaft or electrical input as appropriate.
| Symbol | Meaning | SI units | US customary |
|---|---|---|---|
| P | Input power represented by η | W | hp |
| Δp | Fan total/static pressure rise, consistently defined | Pa | in. w.g. or lbf/ft² |
| V̇ | Airflow | m³/s | cfm |
| η | Fan/drive efficiency used in equation | fraction | fraction |
Worked example — fan moving 2.5 m³/s
Given: V̇ = 2.5 m³/s, pressure rise = 600 Pa, overall efficiency = 0.65.
US check: ≈3.09 hp.
Be explicit whether η is fan-only, fan+drive, or wire-to-air efficiency.
Actual system operating point is set by the intersection of the fan curve and system-resistance curve. Filters and dampers change pressure demand.
08 // COP and EER
Coefficient of performance compares useful heating/cooling output to input power. EER is a common I-P cooling-efficiency expression.
| Symbol | Meaning | SI units | US customary |
|---|---|---|---|
| COP | Coefficient of performance | dimensionless | dimensionless |
| Q̇useful | Heating or cooling output | W | Btu/h |
| Pinput | Electrical input | W | W |
| EER | Energy efficiency ratio | — | Btu/(Wh) |
Worked example — heat pump at one operating point
Given: Useful heat output = 12 kW; electrical input = 3 kW.
Do not compare COP/EER values measured at different rating conditions as though they were identical.
Seasonal metrics (SEER, SCOP, HSPF and regional variants) include part-load and climate assumptions and are not simple point COPs.
09 // Quick formula summary
Compact print reference. Use the detailed sections above for definitions and limitations.
| Topic | Equation | Purpose | Tool |
|---|---|---|---|
| Envelope | q̇=UAΔT | Transmission | Wall heat transfer |
| Sensible air | q̇=ṁcₚΔT | Dry-bulb load | HVAC BTU |
| Total moist air | q̇=ṁdaΔh | Sensible + latent | HVAC BTU |
| Humidity ratio | W=0.621945pw/(p−pw) | Moisture state | Wet bulb |
| Moisture removal | ṁw=ṁdaΔW | Condensate | Dew point |
| ACH | ACH=3600Q/V | Ventilation turnover | Ventilation |
| Fan power | P=ΔpQ/η | Air-moving power | Ventilation |
| COP | COP=Qout/Pin | Equipment efficiency | Heat pump |
10 // Assumptions & limitations
Fundamental equations are only useful when their assumptions match the actual problem.
Steady formulas are excellent for screening and heating transmission, but full cooling-load calculations include solar/radiant storage, schedules, infiltration, internal gains and thermal mass.
Mass-based equations are preferred when pressure, temperature or humidity differs materially from standard-air conditions. ASHRAE explicitly notes elevation corrections for volumetric shortcut factors.
Use consistent total pressure and one psychrometric reference system. Dew point, wet bulb, humidity ratio and enthalpy are coupled state properties.
11 // Technical references
ASHRAE 2025 is the primary source basis. The sheet uses mass-based equations where practical and labels common approximations as approximations.