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1. Purpose and Engineering Decision
A compressor package converts electrical input into compressed-air energy and heat that leaves the selected system boundary through several paths. For cooling design, the critical question is not simply 'how many compressor kilowatts are installed?' but 'where does the heat go during the operating state being designed?'
It distinguishes heat rejected to room air, heat rejected to cooling water, heat deliberately recovered for useful service, and heat carried out with the compressed-air stream or other documented paths.
Mode | Primary output |
|---|---|
Package heat balance | Heat rejection by path for one compressor operating point |
Air-cooled room load | kWth released into compressor-room / duct air stream |
Water-cooled duty | Required cooling-water flow from kWth and allowable water temperature rise |
Heat-recovery scenario | Residual cooling load after verified useful heat recovery |
Fleet profile | Cooling duty by compressor operating state and simultaneous combination |
Design condition | Peak, normal and future cooling-load comparison |
2. Cooling Boundary Must Be Declared
Boundary | Include / exclude decision |
|---|---|
Compressor package electrical input | Main motor plus package auxiliaries if measured at package feeder |
Separate ventilation fans | Include only if the room HVAC/ventilation design treats them as internal heat loads |
Dryer / treatment electrical load | Separate row unless the project intentionally includes treatment-room cooling |
Cooling-water heat rejection | Remove from room-air load when genuinely transferred out of the room |
Recovered useful heat | Subtract only when a verified recovery system exports heat outside the cooling boundary |
Compressed-air enthalpy leaving package | Keep as a separate documented path where quantified |
The worksheet must display the chosen boundary. A water-cooled compressor cannot be treated as if all package input becomes room-air heat, and an air-cooled compressor with ducted hot air cannot be treated as if all heat remains in the room.
3. Steady-State Heat-Balance Framework
P_electrical + Other Internal Heat Inputs = Q_room + Q_water + Q_recovered + Q_air_stream_out + Q_other
This is a bookkeeping equation. Individual terms should come from manufacturer data, measured heat balances or explicit engineering assumptions.
4. Cooling Duty Worksheet with Assumptions - Required Asset
Item | Input / formula | Unit | Evidence / assumption |
|---|---|---|---|
Package input power | Measured or verified | kW | |
Operating state | Load / unload / VSD point | - | Controller / logger |
Room-air heat rejection | Entered / calculated | kWth | Model data / balance |
Cooling-water heat rejection | Entered / calculated | kWth | Model data / measured water side |
Useful heat recovery | kWth | Recovery circuit | |
Compressed-air / other exported heat | Entered if quantified | kWth | Method source |
Room residual heat load | Balance result | kWth | Calculated |
Cooling-air inlet temperature | User input | deg C | Design ambient / measured |
Cooling-air outlet temperature | User input | deg C | Design / measured |
Cooling-water inlet/outlet | User input | deg C | Design / measured |
Air / water flow | Calculated or measured | m3/s, m3/h, L/min | Calculation |
Design margin | Explicit user input | % or kWth | Project basis |
5. Room Residual Heat Load
Q_room,residual = P_in + Q_other,in - Q_water - Q_recovered - Q_air_or_other_export
If the user directly enters a verified room heat-rejection value from a package heat-balance document, that value may be used instead of reconstructing the whole balance. The tool should preserve whether the result is direct or residual-by-difference because confidence is different.
6. Air-Side Cooling Relationship
Q_air = rho_air x V_dot_air x cp_air x DeltaT_air
V_dot_air = Q_air / (rho_air x cp_air x DeltaT_air)
7. Water-Side Cooling Relationship
Q_water = m_dot_water x cp_water x DeltaT_water
Water flow (L/min) approx = Q_kW x 60 / (4.186 x DeltaT_C)
The water-side calculation is valid as a sensible-heat balance for liquid water over ordinary cooling ranges. Actual pump sizing, water quality, fouling allowance, pressure drop, glycol correction or cooling-tower design are separate engineering tasks.
8. Heat-Recovery Credit
Heat recovery reduces cooling duty only when recovered heat is exported outside the cooling boundary. If recovered hot water later releases its heat back into the same compressor room, no room-cooling credit exists.
Q_residual_after_recovery = Q_base_cooling - Q_useful_exported_recovery
9. Air-Cooled Compressor Boundary
For an air-cooled package, the package cooling air may discharge directly into the compressor room or be ducted outdoors.
Discharge arrangement | Room-cooling implication |
|---|---|
Hot air discharged into room | Most package air-side heat remains a room load |
Hot air fully ducted outdoors | Room load is limited to package radiation/leakage and other internal sources |
Seasonal heat-recovery duct | Use separate summer / winter scenarios |
Partial recirculation | Model only the verified fraction returned to room |
10. Water-Cooled Compressor Boundary
For water-cooled machines, the dominant heat path may be the cooling-water circuit, but motor, radiation and auxiliaries can still add heat to the room.
11. Reference Test Case A - Air-Side Flow for Known Room Load
Synthetic validation case: residual room heat load is 120 kWth. Cooling air enters at 32 C and may leave at 42 C. Use air density 1.12 kg/m3 and cp = 1.006 kJ/(kg.K).
V_dot = 120 / (1.12 x 1.006 x 10) = 10.65 m3/s
Reference result: approximately 38,341 m3/h of air to carry 120 kWth across a 10 C temperature rise.
12. Reference Test Case B - Cooling-Water Flow
Synthetic validation case: cooling-water circuit must remove 180 kWth with water entering at 30 C and leaving at 38 C.
Water flow = 180 x 60 / (4.186 x 8) = 322.5 L/min
This is the heat-balance flow only. Pump head, exchanger pressure drop, fouling and water-treatment requirements remain separate.
13. Reference Test Case C - Split Heat Paths
Synthetic validation case: package electrical input is 200 kW. Verified water-side rejection is 145 kWth, useful heat recovery exported outside the room is 25 kWth, and another 8 kWth leaves with a documented external air stream.
Q_room = 200 - 145 - 25 - 8 = 22.0 kWth
Residual room heat load is 22.0 kWth under the stated steady-state boundary. The worksheet should flag any unexplained residual as either room heat or an unresolved balance term rather than forcing it to zero.
14. Reference Test Case D - Fleet Operating Scenario
Synthetic validation case: three compressors have room heat loads of 80, 55 and 25 kWth in the selected operating states. A separate dryer adds 12 kWth to the same room.
Item | Heat load |
|---|---|
Compressor A | 80 kWth |
Compressor B | 55 kWth |
Compressor C | 25 kWth |
Dryer / treatment | 12 kWth |
Scenario total | 172 kWth |
With explicit 10% project margin | 189.2 kWth |
15. Part-Load and Control-State Cooling Duty
Cooling duty follows the actual operating state, not only installed motor rating.
Q_scenario = Sum(Q_heat,state,i x simultaneous state flag_i)
16. Peak, Normal and Future Design Cases
Scenario | Purpose |
|---|---|
Normal production | Routine ventilation / water-cooling requirement |
Peak production | Maximum credible simultaneous operating heat load |
Hot ambient | Check reduced cooling-air temperature difference / cooler capability |
Future expansion | Planned additional machines / treatment equipment |
Emergency / temporary | Rental or temporary compressor heat load |
17. Design Margin
Q_design = Q_calculated x (1 + Margin%)
Margin is explicit and project-specific.
18. Air-Side Temperature Difference Sensitivity
For the same heat load, required air volume rises sharply as the allowed air-temperature rise becomes smaller.
Allowed DeltaT | Required air flow | Required air flow |
|---|---|---|
5 C | 21.30 m3/s | 76,683 m3/h |
8 C | 13.31 m3/s | 47,927 m3/h |
10 C | 10.65 m3/s | 38,341 m3/h |
12 C | 8.88 m3/s | 31,951 m3/h |
15 C | 7.10 m3/s | 25,561 m3/h |
This sensitivity table is why ventilation design must use realistic inlet and discharge temperatures rather than a generic air-change rate.
19. Water-Side Temperature Difference Sensitivity
Water DeltaT | Flow for 180 kWth |
|---|---|
4 C | 645.0 L/min |
6 C | 430.0 L/min |
8 C | 322.5 L/min |
10 C | 258.0 L/min |
12 C | 215.0 L/min |
20. Input Model
Input group | Field | Validation / note |
|---|---|---|
Package | Electrical input kW | > 0 for operating state |
State | Loaded / unloaded / VSD / standby | Required |
Heat path | Room-air heat | Direct or balance-derived |
Heat path | Water-side rejection | >= 0 |
Heat path | Exported heat recovery | >= 0 |
Heat path | Other exported heat | >= 0 |
Air side | Inlet / outlet temperatures | Outlet > inlet |
Air side | rho and cp | Visible assumptions / measured |
Water side | Inlet / outlet temperatures | Outlet > inlet |
Water side | cp / density | Visible assumptions |
Design | Margin | >= 0 |
Evidence | OEM data / measurement / calculation source | Recommended |
21. Validation and Guardrails
Condition | Required behaviour |
|---|---|
Negative heat-path value | Block calculation unless explicitly defined as a credit/export |
Sum of known exported heat > electrical + other heat input | Flag impossible balance |
Air outlet temperature <= inlet | Block air-flow calculation |
Water outlet temperature <= inlet | Block water-flow calculation |
Heat recovery deducted but not exported outside cooling boundary | Warn / do not subtract |
Installed motor rating used as measured package input | Label preliminary |
Peak scenario omits simultaneously operating auxiliaries | Warn |
Room heat derived as small residual from uncertain large terms | Lower confidence / recommend direct measurement |
Air-side flow interpreted as fan selection |
22. Output Specification
Output | Display rule |
|---|---|
Room residual heat load | kWth |
Water-side cooling duty | kWth |
Recovered/exported heat | kWth |
Required cooling-air flow | m3/s and m3/h |
Required cooling-water flow | L/min and optional m3/h |
Scenario total | Normal / peak / future |
Design duty | After explicit margin |
Heat-balance closure | Known inputs vs known heat paths |
Confidence / warnings | Always visible |
Calculators and worked examples
These tools give indicative figures for screening, comparison and for preparing an enquiry. They run in your browser and send nothing. Prices, tariffs and efficiencies shown are example values: replace them with your own. Results are not a performance guarantee or a design certificate; final selection is confirmed by an engineer against the machine data sheet and the site.
Compressor room ventilation
Estimate the cooling air a compressor room needs to keep its temperature rise within a limit.
The worked example below shows the method with fixed numbers. Turn on JavaScript to change the inputs.
Worked example
Inputs
- Total compressor input power (kW): 110
- Heat remaining in room air (%): 90
- Allowed room temperature rise (°C): 8
Result
- Heat to be removed: 99 kW
- Ventilation air needed: 10.26 m³/s
- 36,940 m³/h
- 21,742 CFM
Method. Heat to room ≈ input power × fraction rejected into the room (for air-cooled units, nearly all of it unless ducted). Airflow = heat ÷ (ρ × cp × ΔT), ρ = 1.2 kg/m³, cp = 1.005 kJ/kg·K. If the cooling air is ducted out of the machine, only the radiated part stays in the room.
What to take from it. This is a screening value. The machine maker states a required ventilation flow; follow it where it is higher.