Quick answer
Why ammonia and CO2 are gaining ground in industrial cold storage—and how buyers should weigh efficiency, safety, regulation and cost. Not in every application. Ammonia can be highly efficient for large central plants, while CO2 can perform strongly in appropriate low-temperature and cascade configurations. Compare annual energy models using the same loads, ambient conditions and system boundaries. Refrigerant choice alone cannot establish which proposal will consume less electricity.
Key takeaways
- Is ammonia more efficient than CO2 for industrial cold storage? Not in every application.
- Do F-gas phase-downs mean existing synthetic systems must be replaced? Not necessarily.
- Are natural refrigerants safe inside a cold-storage facility? They can be used safely with appropriate engineering and operating controls, but neither is risk-free.
- When is an ammonia/CO2 cascade system worth considering? Consider it when substantial low-temperature loads and a preference to limit ammonia to a designated plant area align with the site’s operating strategy.
Reviewed: Oct 2026 · ColdMatch Group
Short answer: Ammonia and CO2 are increasingly chosen for industrial cold storage because they reduce exposure to HFC phase-down pressures and can deliver strong lifetime performance. Neither is automatically the best option: climate, temperature duty, safety engineering, maintenance capabilities and whole-life cost should determine the specification.
# Why Natural Refrigerants Are Winning in Industrial Cold Storage
For long-life cold-storage assets, refrigerant selection is a business decision as much as an engineering choice. It affects energy demand, serviceability, permitting and future conversion risk. Natural refrigerants are gaining ground because buyers increasingly evaluate these factors together rather than selecting the lowest equipment price.
Why are F-gas rules changing refrigerant decisions?
HFC phase-down programmes and regional F-gas requirements are changing the outlook for many synthetic refrigerants. Depending on the jurisdiction, buyers may face restrictions on particular equipment, tighter servicing requirements or reduced availability of higher-global-warming-potential refrigerants. The implications differ by refrigerant, application and location.
A phase-down is not a universal ban on every synthetic system. Nevertheless, a cold store expected to operate for many years needs a credible refrigerant supply and maintenance strategy. Equipment that remains serviceable today may present a less attractive lifecycle proposition if its refrigerant becomes harder to source or its permitted uses narrow.
Ammonia and CO2 avoid the HFC phase-down issue, but they do not avoid regulation. Pressure-equipment rules, building and fire requirements, occupational safety obligations and environmental permits still matter. Ask suppliers to identify applicable local requirements and explain both present compliance and foreseeable servicing constraints.
How do efficiency and climate benefits strengthen the case?
Refrigeration has two distinct climate impacts: direct emissions from refrigerant leakage and indirect emissions associated with electricity consumption. Ammonia has no direct global-warming impact as a refrigerant, while CO2 has a much lower direct climate impact than many conventional HFCs. However, refrigerant choice alone does not establish a system’s overall environmental performance.
Ammonia can deliver excellent efficiency in well-designed industrial plants. CO2 also performs strongly in suitable configurations, particularly for low-temperature duties. Actual consumption depends on ambient conditions, suction and condensing temperatures, compressor selection, heat-exchanger performance and control strategy.
Warm climates require particular care when evaluating transcritical CO2. Advanced configurations can improve performance, but their benefits must be demonstrated against the site’s annual operating profile—not assumed from a favourable design point.
Start with a defensible load estimate using the cooling-load calculator. Door openings, incoming product temperature, pull-down requirements and defrost can materially change the design. Good insulation, infiltration control and commissioning remain essential regardless of refrigerant.
Where do ammonia and CO2 fit best?
Ammonia is a strong candidate for central industrial plants serving substantial, sustained loads. Its thermodynamic performance and established industrial service practices make it attractive where the site can support the required safety systems and operating competence. Low-charge designs and secondary cooling loops can limit refrigerant inventory or keep ammonia away from selected occupied areas.
CO2 can suit low-temperature distribution, packaged systems and facilities where avoiding ammonia in storage or processing areas is a priority. Its high operating pressures require purpose-designed equipment, while architecture and local climate strongly influence efficiency.
Ammonia/CO2 cascade systems combine the two: ammonia typically serves the higher-temperature stage, while CO2 serves the lower-temperature circuit. Both refrigerants are natural, although the combined installation introduces additional interfaces and controls.
The NH3 versus CO2 buyer’s guide can help frame the shortlist. Compare complete system designs rather than treating refrigerant names as competing equipment specifications.
What safety, skills and maintenance trade-offs matter?

“Natural” does not mean harmless. Ammonia is toxic and has limited flammability under certain conditions. CO2 can create dangerous concentrations in enclosed spaces and operates at high pressure. Both require engineered containment, appropriate detection, ventilation, pressure protection and documented emergency procedures.
The practical questions extend beyond the machinery room:
- Where could a release travel, and who could be exposed?
- How are alarms, ventilation and emergency shutdowns coordinated?
- What happens during power loss, maintenance isolation or prolonged shutdown?
- Who can respond locally, and which spares are available?
- How will technicians safely isolate, service and recommission the plant?
CO2 designs need particular attention to pressure management during standstill and power interruption. Ammonia designs require careful decisions about charge, equipment location, material compatibility and release management.
Maintenance capability should influence procurement before the specification is fixed. Confirm technician competence, inspection responsibilities, training provision and emergency support. A highly efficient installation can become operationally fragile if only a distant specialist understands its controls. Budget for commissioning, operator training and ongoing maintenance—not just equipment delivery.
When do synthetic or hybrid systems still make sense?
A synthetic refrigerant can remain a rational choice when it fits local rules, the required temperature duty and the available service infrastructure. Examples include constrained retrofits, smaller independently operated zones, temporary capacity and sites where introducing ammonia would create disproportionate complexity.
Lower-GWP synthetic options deserve a technically fair assessment, but they are not interchangeable. Some introduce flammability considerations; others involve temperature glide, different operating pressures or equipment compatibility requirements. Require a refrigerant-specific assessment rather than accepting “future-proof” as a specification.
Hybrid layouts can also be practical. A site might combine an ammonia central plant with a secondary fluid loop, use an ammonia/CO2 cascade, or retain serviceable synthetic equipment while expanding with natural refrigerants. Secondary loops add pumping and heat-transfer penalties, while mixed systems broaden maintenance needs. The right transition is the one that manages those trade-offs without undermining uptime.
How should buyers compare lifecycle value?
For projects of USD 250K+, purchase price is only one part of the decision. Compare proposals against the same temperature requirements, product throughput, ambient conditions, operating schedule and redundancy expectations. Otherwise, apparently cheaper bids may simply contain less scope.
Build the comparison around:
- Installed scope, including electrical works, ventilation, detection and controls.
- Annual energy modelling using realistic loads and local weather.
- Maintenance, refrigerant supply, inspections, training and spares.
- Resilience during equipment failure, defrost and power interruption.
- Expansion options and future refrigerant-related constraints.
Use the cold-storage cost benchmarks for early budgeting context, then replace assumptions with site-specific quotations. The refrigeration TCO calculator can help organise lifecycle scenarios; its outputs depend on the quality of the inputs.
Require bidders to disclose exclusions, modelling assumptions and performance verification methods. A structured process for comparing supplier proposals helps distinguish genuine value from omitted work or optimistic operating assumptions.
What are the next steps for your cold-storage project?
Define the site, temperature zones, product movements, expansion plans and available utilities before choosing a refrigerant. Include local service capabilities and any restrictions on machinery-room location or refrigerant use.
ColdMatch Group is the industrial refrigeration and cold-chain procurement platform of Global B2B Group. It is vendor-neutral, focuses on projects of USD 250K+ and works with a network of 100+ suppliers. It is not an automatic marketplace: buyers submit a request, ColdMatch reviews it and prepares a brief, then manually introduces qualified suppliers.
Submit your project for review to start a requirements-led sourcing process that keeps refrigerant selection tied to your operating needs.
Plan it with ColdMatch tools
Turn this guide into project numbers with these planning tools. Results are estimates from your own inputs, not supplier quotations.
- Submit your project for a reviewed supplier brief — For commercial projects from USD 250,000, ColdMatch reviews the brief before introducing independent suppliers.
Related reading: Cold Storage Design for Hot Climates: Planning Guide · How to Reduce Cold Storage Energy Costs: 2026 Guide
Sources and how to read this guide
Regulatory and technical statements refer to the official sources below. Project-specific values such as capacities, loads and costs must be confirmed by your engineer and supplier proposals.
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Energy & backup powerEnergy & backup power cost calculator
Annual energy spend from load and running hours, plus the cost of generator hours during outages.
Frequently asked questions
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