Duty
+ flooded, − lift
Use the head-loss tool
Liquid
Awaiting Valid Duty Parameters
Adjust the parameters on the left to compute live hydraulic values, ranges, and sizing verdicts.
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Chemical pump sizing explained
Total dynamic head
Total dynamic head (TDH) is the sum of the static heads and friction: suction static head (positive for flooded suction, negative for lift), discharge static head, and friction losses in pipe, fittings and valves. The pump must be selected for this TDH at the required flow — not for the discharge pressure alone, which changes with liquid SG.
A tank at 38 m above the pump with 2 m of friction needs 40 m TDH. That 40 m is the number to read on a pump curve, because curves are drawn in head, which is liquid-independent.
Power and motor sizing
Hydraulic power is flow × TDH × SG ÷ 367. Divide by pump efficiency for shaft power, then select the next IS 1231 motor frame. The SG makes chemical pumps heavier: the same 40 m duty needs 4.19 kW for water but 5.03 kW for 50 % caustic (SG 1.2) — and 6.4 kW for 98 % sulphuric acid (SG 1.84).
Motor efficiency and power factor are applied separately in the motor calculator; this tool gives the frame size directly.
Materials first, then sizing
Before sizing, confirm the wetted materials can survive the liquid at operating temperature. For HCl, PTFE and PFA rate excellent at all concentrations; PP swells above 30 %; SS316 pits. For caustic, PP and SS316 work well up to moderate temperature. The calculator shows the recommended families from the compatibility matrix for the liquid you choose, and the full compatibility selector covers temperature limits and elastomers.
Efficiency and realistic duties
Chemical pumps typically run 50–70 % efficiency at duty. If your existing pump computes below 40 %, it is worn or badly off its best efficiency point — plan an overhaul or re-rating. The repair-vs-replace decision comes down to the lifecycle cost, which the LCC calculator covers. Teflow sizes, builds, repairs and re-rates PTFE, PFA, PP and SS pumps — call +91 98251 62709 for a duty review.
Technical & Operational FAQs
Q1.How do I calculate total dynamic head?
TDH = suction static head + discharge static head + friction loss. Suction static is positive for flooded suction and negative for lift. Friction covers pipe, fittings, valves and strainers. Select the pump for this TDH at the required flow — pump curves are read in head, not pressure.
Q2.What is the pump power formula?
Hydraulic power (kW) = flow (m³/h) × TDH (m) × SG ÷ 367. Shaft power divides this by pump efficiency. For 25 m³/h at 40 m with SG 1.2 and 65 % efficiency: 25 × 40 × 1.2 ÷ 367 = 3.27 kW hydraulic, 5.03 kW shaft, 7.5 kW motor frame.
Q3.Why is SG in the power calculation?
A centrifugal pump produces the same head in metres for any liquid, but the absorbed power scales with density: heavier liquids absorb proportionally more power. Sizing from a water curve without the SG correction undersizes the motor for acids and alkalis.
Q4.Which material for HCl pumps?
PTFE and PFA rate excellent for HCl at all concentrations up to 200 °C and 180 °C respectively. PP is fair below 30 % and 60 °C, SS316 is risky (pitting) and FKM elastomers degrade. PFA-lined and PTFE pumps are the standard choice — Teflow manufactures both.
Q5.How much should I over-size a chemical pump?
Size to the true duty, not a blanket margin. A 10 % flow margin is common for future needs; over-sizing beyond 20 % pushes the pump off its best efficiency point and costs energy and seal life. If the system curve is uncertain, keep the motor frame one size up but select the impeller for the real duty — trim can be adjusted later.
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Need a custom hydraulic audit or specific duty curve verification? Call +91 98251 62709 or Request a Detailed Engineering Quote.