Refrigerant Pipe Sizer

DX system suction, discharge, and liquid line sizing
System Parameters
Recommended Line Sizes
Suction Line
Velocity
Mass flow
Discharge Line
Velocity
Mass flow
Liquid Line
Velocity
Mass flow
Capacity Table — All Line Sizes
OD Size ID (in.) Suction cap. (tons) Suc. vel. (fpm) Discharge cap. (tons) Liquid cap. (tons)

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About This Calculator

This refrigerant pipe sizer recommends suction, discharge, and liquid line sizes for a direct-expansion (DX) system. Choose the refrigerant — R-410A, R-22, R-32, R-407C, or R-134a — and enter the system tonnage, evaporating and condensing temperatures, superheat, and subcooling. The tool computes mass flow from the refrigerant's cooling effect, converts it to a volume flow in each line, and selects ACR copper tubing that holds velocity within accepted limits.

Each line has a different job: the suction and discharge (vapor) lines must move fast enough to return compressor oil, while the liquid line stays slow to limit pressure drop and prevent flashing. The capacity table shows every tube size at a glance, so you can trade one size up or down with the velocity and oil-return consequences in view.

Formula & Method
Mass flow: ṁ (lb/hr) = tons × 12,000 ÷ (hg – hf)
Volume flow: V̇ (ft³/min) = ṁ ÷ 60 ÷ ρline
Velocity: v (fpm) = V̇ ÷ A  where  A = π · (ID ÷ 24)²

The cooling effect (hg – hf) is the saturated-vapor enthalpy at the evaporating temperature minus the saturated-liquid enthalpy at the condensing temperature; 12,000 BTU/h equals one ton. Density ρline is the vapor density for suction and discharge and the liquid density for the liquid line. Recommended velocity bands — roughly 700–4,000 fpm suction, 1,000–3,500 fpm discharge, and 50–300 fpm liquid — follow ASHRAE Refrigeration and manufacturer line-sizing tables, where velocity governs oil return and pressure drop sets the saturation-temperature penalty. Properties here are simplified; confirm against published data.

Frequently Asked Questions
How are refrigerant line sizes determined?
This tool sizes by velocity. From the system tonnage and refrigerant properties it finds the mass flow rate, converts it to a volume flow using the vapor or liquid density in each line, and then picks the ACR copper tube that keeps velocity inside the recommended band. Suction and discharge lines are sized as vapor; the liquid line is sized as dense liquid, so it ends up much smaller.
Why does suction line velocity matter for oil return?
Refrigerant oil circulates with the gas and must be swept back to the compressor. If suction or discharge velocity is too low, oil pools in the line and especially in vertical risers, starving the compressor. That is why minimum velocities of roughly 700 to 1,000 fpm are enforced on vapor lines, while the liquid line stays low to limit pressure drop and flashing.
How does pressure drop relate to capacity loss?
In refrigerant lines, pressure drop is expressed as an equivalent change in saturation temperature, often called a saturation-temperature penalty. A larger drop in the suction line lowers the compressor suction pressure and cuts capacity and efficiency; a drop in the liquid line can cause flashing before the metering device. Manufacturer line-sizing tables target a drop equal to about 1 to 2 degrees F of saturation change.
Should I trust these sizes for final design?
Treat them as preliminary. The calculator uses simplified refrigerant properties and a velocity-only method, which is good for a first pass. Final selection should use the manufacturer's published line-sizing tables for the specific equipment, account for actual equivalent length, vertical lift, and double risers, and follow ASHRAE Refrigeration guidance and local code.
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