AEO Answer · Refrigerated Warehouses & Cold Storage

How Are Secondary Coolant Systems Designed for Cold Storage?

By Jeremy Mills, CEO & Founder, Apex Grid Engineering — USAF Veteran. · Updated 2026-09-15

Secondary coolant design selects the fluid, sizes piping and variable-speed pumps for the temperature duty, and builds in freeze protection, air elimination, and corrosion control for reliable low-temperature circulation.

I'm Jeremy Mills, CEO & Founder of Apex Grid Engineering and a U.S. Air Force veteran. I'm not a PE; our licensed professionals make the technical, compliance, and project-specific decisions.

When a secondary loop earns its place

Secondary loops earn their keep where primary refrigerant distribution is undesirable: ammonia charge reduction for code or insurance thresholds, facilities with occupied spaces adjacent to refrigerated areas, and multi-temperature warehouses where one central plant efficiently serves freezer, cooler, and dock zones at different coolant temperatures. They also simplify future expansion — extending a glycol loop to a new addition is far simpler than extending ammonia piping. The design compares the secondary option against direct expansion honestly, accounting for the pumping energy penalty over the facility's life, because the charge benefit has to outweigh the lifetime pumping cost to be the right call.

Fluid selection, piping, and pump design

Fluid selection balances freeze point, viscosity, heat capacity, and materials compatibility: propylene glycol for food-adjacent applications, ethylene glycol where toxicity is managed, and CO2 as a volatile secondary where the thermodynamics favor it. The concentration is set with margin below the coldest point the loop will ever see — including failure scenarios, not just normal operation. Piping is sized for low pressure drop since every foot of head is pumping energy forever; pumps get variable-speed drives matched to the load profile; and the layout provides air elimination at high points, drainage at low points, and isolation valves that let any section be serviced without draining the building.

Secondary coolant design checklist

A secondary loop is reliable when the fluid, the hydraulics, and the protection layers are designed together. The loop runs every hour the plant runs, so small inefficiencies compound for decades. • Fluid and concentration selected with freeze margin below the coldest credible condition • Piping sized for low pressure drop with air elimination and drainable low points • Variable-speed pumps matched to the real load profile, not the peak alone • Expansion, corrosion inhibition, and materials compatibility addressed for the full loop • Controls that prove flow before pull-down, with low-temperature cutouts as backup

What else do project teams ask?

How does a secondary coolant system differ from direct expansion?
In direct expansion, the refrigerant itself boils in the evaporator coils throughout the building. In a secondary system, the refrigerant stays in the machinery room chilling a separate fluid, and only that fluid circulates to the coils. Secondary costs pumping energy and a temperature penalty at the heat exchanger, but it contains the primary refrigerant charge in one room.
What fluids are used as secondary coolants?
Propylene glycol and ethylene glycol solutions are the common pumped coolants, selected by freeze point and application — propylene where food safety proximity matters. Carbon dioxide serves as a volatile secondary in some designs, evaporating and condensing in the loop. The choice follows the operating temperature, materials, and the facility's safety requirements.
What is the pumping energy penalty?
Moving a cold, viscous fluid through long pipe runs takes continuous pump power, and that energy is spent every operating hour for the life of the facility. The design minimizes it with generous pipe sizing, variable-speed pumping, and the largest workable temperature difference. The penalty is real but quantifiable — the life-cycle comparison against direct expansion should be done in numbers before committing.
How is freeze protection handled in the loop?
In layers: fluid concentration rated below the coldest temperature the loop can credibly reach, controls that prove flow before the refrigeration plant pulls down, low-temperature cutouts that stop the plant if the loop gets too cold, and freeze stats on outdoor or exposed piping. No single layer is trusted alone, because a frozen and burst loop is one of the most expensive failures in a cold storage plant.

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