Sump Pump Sizing Calculator — Total Dynamic Head & HP
Size a sump or sewage ejector pump by inflow (gpm), static lift, and discharge pipe friction. Returns Total Dynamic Head (TDH), flow velocity, and estimated motor horsepower per IPC 912 and Crane TP-410.
By TradeCalc, Plumber Calculators — Code-Referenced — IPC Section 912 (Sumps and Ejectors), ASPE PDH Vol. 2, Crane TP-410, Hydronic Institute Standards, HUD Handbook 4910.1
⚠️ Results are for informational purposes only. Verify against applicable codes and manufacturer specifications before use. Always consult a licensed electrician/HVAC contractor and your local AHJ (Authority Having Jurisdiction) before performing work.
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How to Size a Sump or Sewage Ejector Pump
How Sump Pump Sizing Works
A sump or sewage ejector pump must move the peak incoming water flow (gpm) against the Total Dynamic Head (TDH) — the total resistance the water faces leaving the pit. TDH is the sum of (1) static head (the vertical lift from the pump's "off" level up to the discharge point) and (2) friction head (the energy lost pushing water through the discharge pipe and its fittings). IPC Section 912 and ASPE PDH Vol. 2 require that the pump be sized so its published performance curve delivers the required gpm at the calculated TDH, with a safety margin.
The TDH Formula
TDH (ft) = static head + friction head
friction head = Hazen-Williams hf over equivalent pipe length
hf = 4.52 × L_eq × Q^1.85 / (C^1.85 × d^4.87)
HP = (gpm × TDH) / (3960 × efficiency)
- static head = vertical distance pump must lift water (ft)
- L_eq = straight pipe length + equivalent length of fittings (ft)
- Q = flow (gpm), C = 150 for PVC, d = actual pipe ID (in)
- 3960 = HP conversion (550 ft·lb/s × 60 s/min ÷ 8.34 lb/gal)
- efficiency = 0.50–0.60 for small submersible sump pumps
Equivalent Length of Fittings (Crane TP-410)
Each fitting adds friction equivalent to a length of straight pipe. For a 1.5" line: a 90° elbow ≈ 5 ft, a 45° elbow ≈ 2.7 ft, a gate valve ≈ 1.3 ft, a swing check valve ≈ 16 ft (it has a flapper that adds significant loss), and a tee taken on the branch ≈ 9.5 ft. Sum these with the straight pipe length to get L_eq. The check valve is usually the biggest single friction contributor — that's why modern systems use a "full-flow" or spring-loaded check valve with lower loss.
Worked Example
Scenario: A basement sump pump must handle 50 gpm peak inflow. The discharge rises 10 ft to grade, then runs 50 ft horizontally through 1.5" Schedule 40 PVC with four 90° elbows, one swing check valve, and one gate valve. Find TDH and required HP.
- Static head = 10 ft
- 1.5" Sch 40 PVC actual ID = 1.610 in, C = 150
- L_eq = 50 ft (straight) + (4 × 5 ft elbows) + (1 × 16 ft check) + (1 × 1.3 ft gate) = 50 + 20 + 16 + 1.3 = 87.3 ft
- friction hf = 4.52 × 87.3 × 50^1.85 / (150^1.85 × 1.610^4.87) = 4.52 × 87.3 × 1390 / (10,611 × 10.17) = 548,589 / 107,918 = 5.08 ft
- TDH = 10 + 5.08 = 15.08 ft
- Velocity = 0.4085 × 50 / 1.610² = 20.4 / 2.59 = 7.88 ft/s (under 8 ft/s limit ✓)
- HP = (50 × 15.08) / (3960 × 0.55) = 754 / 2178 = 0.35 HP → select 1/2 HP pump
A 1/2 HP submersible sump pump is the right selection — its curve typically delivers 50+ gpm at 15–18 ft TDH. The next size down (1/3 HP) would deliver only ~40 gpm at this head, leaving no margin for a heavier rain event. Always verify against the manufacturer's published pump curve before buying.
Practical Tips
- Size on peak inflow, not average. A sump that sees 20 gpm average but 60 gpm during a storm must be sized on 60 gpm or it will overflow. Estimate inflow by timing how fast the pit fills between pump cycles, or use a 110% safety factor on calculated inflow.
- The check valve is the biggest friction item. A swing check valve adds ~16 ft equivalent length on a 1.5" line. A "silent" spring-loaded check valve (e.g., JB or ProPlumber) cuts this to ~6 ft and also eliminates the slam noise. Always include a check valve in the L_eq takeoff.
- Velocity must stay 6–10 ft/s. Below 6 ft/s solids settle out and clog the line (sewage ejectors especially); above 10 ft/s you get water hammer and fitting stress. The 1.5" line at 50 gpm (7.9 ft/s) is ideal. A 1.25" line would be 11 ft/s (too fast); a 2" line would be 4.9 ft/s (too slow for solids).
- Always install a redundant pump. A single pump will fail during the storm you most need it. Install a second pump on a separate circuit with a battery backup, set 4–6" higher than the primary. The backup picks up the load if the primary fails, loses power, or is overwhelmed.
- Read the actual pump curve. The HP estimate is a starting point; the binding spec is the manufacturer's published curve (gpm vs ft of head). A "1/2 HP" pump from one maker delivers 55 gpm at 15 ft; another delivers 35 gpm at the same head. Match the curve to your TDH/gpm point.
Code References
IPC Section 912 (Sumps and Ejectors), ASPE PDH Vol. 2, Crane TP-410, Hydronic Institute Standards, HUD Handbook 4910.1