CO₂ Refrigerant Compressor: Subcritical and Transcritical Systems for Industrial Refrigeration

Application Guide · CO₂ Refrigerant · Subcritical · Transcritical · Industrial Refrigeration · Russia

Carbon dioxide (R-744) is attracting renewed industrial interest as a refrigerant because it is non-toxic, non-flammable, has zero ozone depletion potential, and a global warming potential of 1 — the reference point for all other refrigerants. In industrial refrigeration, CO₂ is used in two distinct circuit configurations: subcritical (as the low-temperature stage in a cascade system with NH₃ or HFC on the high stage) and transcritical (as the sole refrigerant in a circuit that operates above its critical point on the high-pressure side). The CO₂ refrigerant compressor specification differs significantly between these two configurations and from the compressors used for nitrogen, oxygen, or NH₃ refrigerant service. This guide explains both and covers the DW and 4MW series configurations available for Russia and CIS industrial refrigeration.

✓ CO₂ · R-744 · GWP = 1
✓ Subcritical · Transcritical
✓ DW / 4MW Series
✓ GOST-R Certified · Russia
4MW DW CO2 refrigerant compressor subcritical transcritical industrial refrigeration cascade NH3 Russia GOST-R

CO₂ refrigerant compressor in subcritical cascade service — the low-stage compressor of an NH₃/CO₂ cascade system for cold storage at −35°C to −55°C. CO₂ at these temperatures operates at suction pressures of 10–20 bar absolute and condensing pressures of 30–40 bar absolute — approximately 3–4 times higher than NH₃ at the same conditions — requiring a compressor with cylinder materials, valve design, and piston rod packing rated for the substantially higher CO₂ operating pressures.

10–45 bar
Subcritical Suction
30–130 bar
CO₂ Discharge Range
GWP = 1
Zero ODP Refrigerant
DW / 4MW
Available Series
31.1°C / 73.8 bar
CO₂ Critical Point

CO₂ as a Refrigerant: Properties and Critical Point

CO₂ (R-744) has thermodynamic properties that distinguish it from every other common industrial refrigerant. Its critical point is at 31.1°C and 73.8 bar absolute — a temperature near ambient and a pressure far above the operating range of standard refrigerant circuits. NH₃, for comparison, has a critical point at 132.4°C and 113.5 bar: well above any practical condensing condition, so NH₃ refrigerant circuits always operate in the subcritical regime where the refrigerant condenses to liquid. CO₂, in contrast, can operate either subcritically (when the heat rejection temperature is below 31.1°C, as in a cascade system or a cold climate) or transcritically (when the heat rejection temperature exceeds 31.1°C, as in most ambient-temperature industrial applications).

This distinction matters enormously for the CO₂ refrigerant compressor specification. In subcritical operation, the compressor condenses CO₂ to liquid at the discharge, and the refrigerant circuit behaves similarly — at higher pressure — to a conventional NH₃ or HFC circuit. In transcritical operation, the high-pressure side does not condense — CO₂ gas is cooled in a gas cooler but remains supercritical — and the compressor discharge pressure must be controlled by a high-pressure valve rather than by a condensing temperature, reaching 80–130 bar absolute in warm-climate or high ambient-temperature transcritical systems.

Subcritical CO₂: The NH₃ / CO₂ Cascade System

CO2 refrigerant compressor subcritical cascade NH3 CO2 cold storage blast freezing Russia DW 4MW series

The most established industrial application of CO₂ refrigerant in Russia is the NH₃/CO₂ cascade system used for deep-freeze cold storage and blast freezing at −35°C to −55°C. In this arrangement, CO₂ is the low-stage refrigerant whose evaporator provides the refrigeration duty at the deep-freeze temperatures. The CO₂ condenses in a cascade heat exchanger that is itself the evaporator of the NH₃ high-stage circuit. The NH₃ high-stage compressor rejects heat to the ambient-temperature condenser in the normal way.

The advantage of this arrangement over a single-refrigerant NH₃ two-stage system at the same deep-freeze temperatures is twofold. First, the CO₂ low-stage circuit operates at suction pressures of 10–20 bar absolute at −40°C to −55°C evaporating temperature — significantly above atmospheric, unlike an NH₃ low-stage circuit which would operate at 0.4–0.8 bar absolute at the same temperatures, creating a partial-vacuum suction condition that increases the risk of air ingress through shaft seals. Second, the CO₂ low-stage circuit can be distributed across a large facility without the safety regulatory burden of NH₃ piping on the processing floor, since CO₂ is non-toxic. Only the NH₃ high-stage circuit, which remains in the machine room, falls under the Federal Law 116-FZ hazardous production object regime.

NH₃ / CO₂ Cascade vs NH₃ Two-Stage: Deep-Freeze Comparison
Parameter NH₃ Two-Stage NH₃ / CO₂ Cascade
Low-stage suction at −50°C 0.41 bar abs (sub-atm) 13.8 bar abs (CO₂)
Air ingress risk at shaft seals High (vacuum suction) None (above atm)
NH₃ on processing floor Yes (full circuit) No (CO₂ only on floor)
COP at −50°C / +30°C 1.1–1.3 1.0–1.2 (similar)
System complexity Lower (single refrigerant) Higher (two refrigerants)

CO₂ Compressor Specification: High-Pressure Design Requirements

The defining characteristic of a CO₂ refrigerant compressor — whether subcritical or transcritical — is the substantially higher operating pressure compared with NH₃ or HFC compressors at the same temperature conditions. This pressure difference drives the most significant specification departures from the standard refrigerant compressor design:

Cylinder and Valve Pressure Rating
Subcritical CO₂ compressor cylinders are rated for 45–55 bar design pressure (compared with 20–25 bar for equivalent NH₃ service). Transcritical cylinders are rated for 130–150 bar. Cylinder wall thickness, valve body material (forged steel rather than cast iron for transcritical service), and studs are sized for the higher pressure class. Cylinder flanges and connections use higher-pressure class fittings throughout.
Piston Rod Packing
Piston rod packing for CO₂ service uses laminated PTFE/metallic ring sets rated for the full CO₂ discharge pressure. Standard NH₃ piston rod packing is rated for 25 bar and is not suitable for CO₂ service. The packing ring set geometry and the stuffing box dimensions are redesigned for CO₂ to handle the higher differential pressure across each ring element without excessive ring extrusion or accelerated wear.
Gas Valve Design
CO₂ gas valves operate at higher differential pressure than NH₃ valves in equivalent service, with a denser gas and higher flow velocity through the valve port. Valve plate thickness and spring rates are specified for the CO₂ pressure and flow velocity conditions. Valve seat leakage — which reduces volumetric efficiency — is more critical in CO₂ service than in NH₃ service because CO₂ is more penetrating through marginal seal contacts at the higher operating pressures.
CO₂-Compatible Lubrication
Conventional mineral refrigeration oils are not suitable for CO₂ compressor crankcase service because CO₂ dissolves readily in mineral oil at the operating pressures of a CO₂ compressor, significantly reducing oil viscosity and lubrication effectiveness. Synthetic polyalkylene glycol (PAG) or polyol ester (POE) oils with low CO₂ solubility are specified for all CO₂ refrigerant compressor applications.

Transcritical CO₂: Industrial Refrigeration at Ambient Temperature

CO2 refrigerant compressor transcritical industrial refrigeration ambient temperature Russia DW 4MW series 80 130 bar

Transcritical CO₂ systems operate the high-pressure side above the critical point (73.8 bar, 31.1°C), delivering heat to ambient air in a gas cooler rather than a condenser. This allows a CO₂ refrigerant system to operate without a secondary refrigerant at any ambient temperature, making it a true single-refrigerant system with the environmental credentials of R-744 (GWP = 1, ODP = 0).

The tradeoff is compressor discharge pressure. At a gas cooler outlet temperature of +40°C (typical for a warm ambient installation), optimal transcritical CO₂ system efficiency is achieved at a gas cooler pressure of approximately 90–100 bar — which becomes the compressor discharge pressure. At +50°C gas cooler outlet (hot climate or high-load conditions), optimal pressure rises to 110–120 bar. These discharge pressures are achievable in a reciprocating compressor but require the full high-pressure CO₂ specification: forged steel cylinders and heads, high-pressure-class gas valves, forged piston rod packing housing, and a high-pressure-class safety valve and discharge pipework system.

Transcritical CO₂ refrigeration in Russia is primarily adopted at large supermarket chains and food distribution centres where the environmental credentials and EU-equivalent regulatory alignment of R-744 are valued for corporate sustainability reporting. The technology is at an earlier adoption stage in Russia than in Western Europe, where transcritical CO₂ is already the dominant new-installation technology for supermarket refrigeration. The DW series CO₂ compressor covers the transcritical duty range for most Russian supermarket and food distribution applications at 55–350 kW.

Application Configuration Suction (bar) Discharge (bar) Series
Deep-freeze cascade (low stage) Subcritical 10–20 28–40 DW series
Cold store cascade (large scale) Subcritical 14–25 30–45 DW or 4MW
Supermarket / food retail Transcritical 25–40 80–110 DW series
Industrial transcritical (large) Transcritical 30–45 90–130 4MW series

All CO₂ configurations use PAG or POE synthetic lubricant; high-pressure-rated cylinders and piston rod packing; CO₂-specific valve design. Subcritical DW and 4MW series use the same opposed-balance frame as standard refrigerant compressors. Contact our engineering team for a CO₂ compressor specification at your operating conditions.

CO₂ Compressor Safety in Russia: GOST and Regulatory Framework

CO₂ is non-toxic and non-flammable, which means a CO₂ refrigerant system does not fall under the Federal Law 116-FZ hazardous production object regime that applies to NH₃ refrigeration plants above defined inventory thresholds. This simplifies the regulatory pathway for CO₂ refrigeration significantly: no Rostechnadzor HPO registration, no licensed operating personnel requirement specific to CO₂, and no mandatory emergency response plan for toxic gas release. The CO₂ refrigerant compressor must still comply with GOST pressure vessel and pressure equipment requirements (GOST R 53674 for pressure vessels, GOST standards for reciprocating compressors) and must carry GOST-R certification, but the regulatory burden is comparable to a standard compressed air or nitrogen system rather than an NH₃ plant.

One safety consideration specific to CO₂ that does not apply to NH₃ or HFC refrigerants is asphyxiation risk. CO₂ at concentrations above 5% by volume in air causes rapid loss of consciousness without warning odour. Unlike NH₃, which gives intense olfactory warning at 5–10 ppm — far below the dangerous concentration — CO₂ is odourless and its physiological effects become severe before most people notice unusual breathing. CO₂ gas detectors in the machine room and in any enclosed space where CO₂ piping is routed are therefore a standard safety provision for CO₂ refrigerant installations, regardless of the absence of the NH₃-equivalent toxicity classification.

Related Application · Plastics Manufacturing

CO₂ in PET Bottle Production: Carbonation and Cold-Fill Refrigeration

CO₂ appears in PET bottle production at two distinct points in the value chain. First, the beverage itself: carbonated soft drinks and mineral water filled into PET bottles contain dissolved CO₂ at 3–8 bar, and the filling line refrigeration system keeps the beverage chilled during filling to maintain carbonation. This filling line refrigeration — typically at +2°C to +5°C — may use an NH₃/CO₂ cascade or a transcritical CO₂ system for the CO₂ refrigerant compressor duty described in this guide. Second, the PET bottle itself is produced on an injection stretch blow moulding (ISBM) line, where the stretch-blow air contacts the interior of the bottle during the forming cycle. The ISO 8573-1 Class 1 oil-free blow air requirement for food-contact PET bottles — bottles that will be filled with carbonated beverages — parallels the zero-contamination philosophy of the CO₂ beverage filling refrigeration system: both protect the product in the bottle from any compromise of the packaging integrity or beverage quality.

Related equipment: One-step three-station ISBM machines producing food-contact PET bottles for carbonated beverage filling — the same PET bottles that are filled on refrigerated lines using CO₂ refrigeration systems.

ISBM Machine ›injectionstretchblowmolding.com

FAQ — CO₂ Refrigerant Compressor

Q1: Why can an existing NH₃ compressor not be used for CO₂ service?
An NH₃ refrigerant compressor cannot be used for CO₂ service for three fundamental reasons. First, the operating pressure: a CO₂ compressor in subcritical cascade service operates at 28–45 bar discharge pressure, which is 2–3 times the NH₃ compressor design pressure of 16–20 bar. Second, the lubrication: mineral refrigeration oil used in NH₃ compressors has high CO₂ solubility at CO₂ operating pressures, resulting in severe oil dilution and loss of crankcase lubrication. A CO₂ compressor requires synthetic PAG or POE lubricant. Third, the gas valve design: CO₂ gas valves are designed for the higher gas density, higher differential pressure, and different flow velocity profile of CO₂ at its operating conditions — NH₃ valves would have incorrect lift, spring rate, and seating geometry for CO₂ service, resulting in poor volumetric efficiency and short valve life. A CO₂ refrigerant compressor is a purpose-built machine, not a converted NH₃ unit.
Q2: Is transcritical CO₂ refrigeration viable in Russia’s cold climate regions?
Transcritical CO₂ refrigeration performs particularly well in cold climates because the ambient temperature at which heat is rejected is lower — reducing the gas cooler outlet temperature and therefore the optimal high-side pressure. In Novosibirsk, Yekaterinburg, or Krasnoyarsk where winter ambient temperatures routinely fall below −20°C, the transcritical CO₂ system shifts to subcritical operation during winter (since the ambient temperature is below the CO₂ critical point of 31.1°C), achieving its highest efficiency of the year. The compressor operating conditions shift between subcritical in winter and transcritical in summer, requiring a control system that manages the transition and a compressor that is rated for both pressure regimes. This cold-climate advantage is one of the reasons transcritical CO₂ refrigeration is well suited to Russian conditions compared with the same technology in warm-climate markets where it must always operate transcritically.
Q3: What information is needed to specify a CO₂ refrigerant compressor?
To specify a CO₂ refrigerant compressor, our engineering team requires: subcritical or transcritical configuration; evaporating temperature (°C) and suction pressure (bar); discharge pressure (bar) — condensing pressure for subcritical, target gas cooler pressure for transcritical; refrigerating capacity (kW) at the operating conditions; whether the CO₂ circuit is the low stage of a cascade system (and if so, the NH₃ high-stage condensing temperature); site ambient design temperature; motor voltage (380V or 6 kV); and required system availability (single machine or N+1 standby). Our engineering team returns a CO₂ compressor configuration with verified pressure ratings, synthetic lubricant specification, and quotation within 48 hours.
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Request a CO₂ Refrigerant Compressor Specification

DW and 4MW series CO₂ refrigerant compressors for subcritical cascade and transcritical service — high-pressure-rated cylinders, CO₂-specific valve design, PAG / POE synthetic lubricant, GOST-R certified. Response within 48 hours.