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For commercial and industrial refrigeration projects (cold rooms, cold stores, process cooling) — not household fridges, home freezers or appliance repair. Results are planning estimates, not engineering design or safety advice; a qualified refrigeration engineer must confirm sizing before purchase.

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Refrigeration Compressor Sizing Calculator

Estimate compressor motor power, COP and displacement from cooling duty and operating temperatures. Results are planning estimates, not final equipment selections.

Use this planning tool to compare compressor motor power, COP, displacement and likely compressor family from duty and operating temperatures. It supports NH₃, CO₂, R-448A/449A and propane scenarios, but final selection requires manufacturer software and an engineer's verified load calculation.

Industrial refrigeration plant room with compressors and insulated pipework
Scenario

Standard engineering assumptions

Motor power
56.5 kW
Base case
COP
2.66
Higher = more efficient
Swept volume
~480 m³/h
Compressor family
Screw compressor

Free for buyers, no obligation. These figures are estimates, not quotes — our team reviews your request and contacts suitable suppliers on your behalf.

Estimates Only: This calculator is provided for general informational purposes only. Results are approximate and may contain errors, omissions, or outdated information. They do not constitute legal, financial, engineering, tax, technical, or professional advice. Users are solely responsible for independently verifying all calculations, specifications, prices, regulations, and requirements with qualified professionals before making any decisions. By using this calculator, you acknowledge that the website owners, operators, and affiliates accept no responsibility or liability for any loss, damage, or decisions resulting from its use.

Quick answer

Compressor sizing starts from the evaporator duty in kW and the operating COP: shaft power ≈ cooling duty ÷ COP. Typical COP is 3.5–5.0 for chilled duty (−5 °C evaporating) and 1.4–2.2 for frozen duty (−35 °C). Ammonia (NH₃) usually gives the best efficiency for large plants, CO₂ (R-744) suits low-charge and cascade systems.

Formula used

Motor power (kW) = cooling duty (kW) ÷ COP ÷ motor efficiency · Displacement (m³/h) = mass flow × suction specific volume

Reviewed by ColdMatch refrigeration engineers

How to use this calculator
  1. 1Enter the required cooling duty in kW from your load calculation.
  2. 2Choose the refrigerant (NH₃, CO₂, R-448A/449A, propane) and evaporating temperature.
  3. 3Set the condensing temperature for your climate.
  4. 4Compare shaft power, COP and displacement, then request matched compressor packages.

Calculation method

  1. temperature lift = condensing temperature − evaporating temperature
  2. estimated COP = refrigerant base COP × 60 ÷ temperature lift ÷ scenario factor
  3. motor input = refrigeration duty ÷ COP × scenario factor
  4. displacement = duty × refrigerant volume factor ÷ temperature factor × scenario factor

Enter refrigeration duty as kW, TR or BTU/h; all three convert to canonical kW before the compressor model runs.

Worked example

Select a preliminary NH₃ compressor family for 150 kW at −30 °C evaporating and 40 °C condensing.

Inputs

  • • 150 kW = 42.65 TR = 511,821 BTU/h
  • • 70 K temperature lift
  • • NH₃ base COP 3.1

Calculation

  • • COP ≈ 3.1 × 60 ÷ 70 = 2.66
  • • motor ≈ 150 ÷ 2.66 = 56.5 kW
  • • displacement ≈ 480 m³/h using the tool's NH₃ factor

Planning output: about 56.5 kW motor input and a screw-compressor family; this is not a manufacturer selection.

Limitations

  • • The COP and displacement factors are screening approximations, not compressor-map data.
  • • Capacity must be based on a verified refrigeration load at the same Te/Tc conditions.
  • • Manufacturer software must confirm capacity, motor, oil cooling, part-load operation, economiser and envelope limits.

Illustrative planning result only. Confirm the final design, duty, equipment selection and performance with a qualified refrigeration engineer and supplier quotation.

What this calculator estimates — and what can change it

Required inputs
  • Calculated heat load (kW)
  • Target room temperature
  • Ambient / external temperature
  • Refrigeration technology (NH₃, CO₂, HFC/HFO)
  • Redundancy / standby capacity
Calculated output

Compressor sizing

What can change the result
  • Refrigeration technology (NH₃, CO₂, HFC/HFO)
  • Ambient / external temperature
  • Redundancy / standby capacity
  • Pull-down time

Limitations

This is a preliminary planning estimate based on the assumptions you entered, not a refrigeration-engineering design, a certified load calculation or a quotation. Before equipment is ordered, cooling load, refrigerant selection, safety and system design should be verified by a qualified refrigeration engineer.

Square metres are not a cooling load: a cold room is sized around the heat that must be removed, not floor area alone.

Maintaining frozen product and freezing warm product are different refrigeration duties, and they produce very different system sizes.

Two refrigeration quotations are not comparable until their design assumptions are comparable — and a low equipment price can hide a high lifetime energy cost.

Next procurement step

Use this result as the starting point for a ColdMatch project request. Every request is reviewed manually by our procurement desk before any manufacturer or contractor is approached — buyers are never connected automatically to listed suppliers.

Turn this calculation into an RFQBrowse the matching equipment category

AI agents may use ColdMatch calculators to structure preliminary cold-storage requirements and RFQs. Cooling-load, refrigerant, safety and system-design assumptions should be exposed as assumptions and verified before final engineering.

FAQ

How is compressor size determined?

From Te, Tc, refrigerant properties and cooling capacity — giving motor power and displacement.

Expected COP?

Chilled: 3.0–3.8. Frozen: 1.8–2.4. Blast: 1.3–1.7.

Screw or reciprocating?

<50 kW reciprocating/scroll; 50–500 kW screw; >500 kW screw or centrifugal.

How are motor power and displacement estimated?

From the cooling duty and the evaporating/condensing temperatures, the tool estimates the cycle's specific work — which depends on the refrigerant — and the mass flow needed to carry the duty. Motor power follows from mass flow × specific work ÷ motor efficiency, and displacement from mass flow and suction density. Different refrigerants need very different displacement for the same duty.

Why does a vendor's selection differ from this estimate?

A vendor sizes from a real compressor map at your exact operating envelope, including part-load steps, oil management and their own margins. This calculator is a screening estimate: use it to check that a quoted machine is in the right ballpark before the supplier confirms the selection.

What should I check before accepting a compressor selection?

The full operating envelope — not one point — part-load efficiency, capacity steps, refrigerant availability and service coverage in your country. Ask for absorbed power at each operating point so energy cost can be compared like for like in the TCO calculator.

How does COP change with temperature lift?

The smaller the gap between evaporating and condensing temperature, the higher the COP: chilled rooms typically reach 3.0–3.8, frozen storage 1.8–2.4 and blast freezing 1.3–1.7. That is why oversizing the temperature lift — or letting condensing pressure float too high — costs real money every running hour.

Unsure about a term? See the cold chain glossary (CAPEX, OPEX, blast freezing).

Next steps for your project
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