Refrigerant Line Quick Sizer

Quick pressure-drop ACR copper sizing for refrigerant lines.

Inputs

Typically 35–45°F for A/C, 15–25°F for medium-temp refrigeration (range −20 to 60°F)
Typically 105–130°F condensing temp (range 70–140°F)
One-way run plus fitting allowances; sized at 10°F superheat and 10°F subcooling

Recommended ACR Copper Sizes

Suction Line
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Discharge Line
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Liquid Line
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Sizing Limits Used

LineMax friction lossVelocity check (FPM)Purpose
Suction (horizontal)2 °F≥ ~500, ≤ 4,000Capacity penalty; oil return
Suction (vertical riser)—≥ ~1,000Carry oil upward (large risers need more)
Discharge (hot gas)1 °F≥ ~500 horizontal, ~1,000 riser; ≤ 3,500Oil return; sound control
Liquid line1 °F≤ 300Stay subcooled; limit liquid hammer

Friction limits are over the entered equivalent length — the basis of the ASHRAE Refrigeration Handbook line-capacity tables (per 100 ft). Velocity figures are common rules of thumb.

Inputs, results, and method — as an Excel workbook or plain CSV.

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About This Calculator

This refrigerant line sizer recommends ACR copper tube sizes for the suction, discharge, and liquid lines of a DX system. Enter the system tonnage, refrigerant (R-410A, R-454B, R-32, R-134a, R-407C, or legacy R-22), the suction and discharge saturation temperatures, and the equivalent length; the tool finds the mass flow from the refrigerating effect, sizes each line for pressure drop, and reports the tube size, velocity, and friction loss. It shares its engine with the Refrigerant Pipe Sizer, which adds superheat, subcooling, and a full capacity table.

The suction and discharge (vapor) lines are sized for pressure drop and then checked for enough velocity to return compressor oil, while the liquid line is sized so its loss stays well inside the subcooling. Use the result as a preliminary check, then confirm against the equipment manufacturer's line-sizing tables.

Formula & Method

Mass flow: ṁ (lb/h) = tons × 12,000 ÷ (h1 – h4)
Velocity: v (fpm) = ṁ ÷ 60 ÷ ρline ÷ Atube
Friction: ΔP = f · (L ÷ D) · ρv² ÷ 2gc;  ΔT = ΔP ÷ (dPsat/dT)
Size: smallest ACR tube with ΔT ≤ 2 °F suction, 1 °F discharge, 1 °F liquid

The refrigerating effect h1 – h4 is taken at your suction temperature plus 10 °F superheat and your condensing temperature less 10 °F subcooling (for R-410A at 40/110 °F it is about 72 Btu/lb, or roughly 2.8 lb/min per ton). Densities, enthalpies, viscosities, and dP/dT come from the CoolProp reference equations of state — the REFPROP-equivalent data ASHRAE Handbook—Fundamentals Ch. 30 tabulates; for blends the temperatures are dew points and the liquid uses the bubble point, and discharge gas assumes 70% isentropic compression. The friction factor is Colebrook’s with drawn-copper roughness, and tube IDs are ASTM B280 ACR. The friction limits are the ASHRAE Refrigeration Handbook line-capacity-table basis applied to your equivalent length; the velocity checks are rules of thumb, made at full load (check staged or inverter equipment at minimum capacity). Use the Refrigerant Pipe Sizer to change superheat or subcooling.

Frequently Asked Questions

How does this refrigerant line sizer pick a tube size?
From the tonnage and the refrigerating effect at your suction and condensing temperatures it finds the refrigerant mass flow, then computes each ACR copper tube's friction loss with the Darcy-Weisbach equation and converts it to a change in saturation temperature. It picks the smallest tube that keeps the loss within 2 °F on the suction line and 1 °F on the discharge and liquid lines over your equivalent length (the ASHRAE line-capacity-table basis), then reports the velocity so you can confirm oil return. It uses the same engine as the Refrigerant Pipe Sizer, with 10 °F superheat and 10 °F subcooling.
What velocities are recommended for refrigerant lines?
Common rules of thumb: suction lines at least about 500 fpm in horizontal runs and about 1,000 fpm in vertical risers to carry oil, up to about 4,000 fpm before noise; discharge lines similar minimums up to about 3,500 fpm; liquid lines at or below about 300 fpm to limit liquid hammer when a solenoid valve closes. In this tool velocity is a check; the pressure-drop limit sets the size.
Why is the liquid line so much smaller than the suction line?
Liquid refrigerant is roughly 25 to 70 times denser than the suction vapor at air-conditioning conditions (about 26 times for R-410A, about 70 times for R-134a), so the same mass flow occupies far less volume and needs much less pipe area. The liquid line is still sized for low pressure drop, because a loss larger than the subcooling flashes liquid to vapor before it reaches the metering device.
Do vertical risers need special attention?
Yes. On vertical suction risers, velocity must stay high enough, roughly 1,000 fpm or more and higher in large risers, to carry oil up against gravity back to the compressor. When the pressure-drop size is too slow for a riser, the tool suggests a smaller riser size. At low load a single riser may not maintain that velocity, so a double-riser arrangement is sometimes used. Confirm riser design against the manufacturer's selection tables and ASHRAE Refrigeration Handbook guidance.

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AIM Works · launches Oct 15, 2026

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Results are design estimates for preliminary sizing. Verify final designs against applicable codes and standards — engineering judgment and a licensed professional engineer’s review are required.