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REDDY COMPRESSORS

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Compressed Air Cooling Load Worksheet

6 min read10 sections

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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.

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