Free engineering calculator

    Slurry Pump Sizing Calculator

    Size a slurry pump from flow, solids content and solid density. The calculator derives the slurry specific gravity, applies a head margin for wear and friction, and returns hydraulic and shaft power with the IS motor frame for abrasive chemical and effluent duties.

    Parameters & Duty InputsInteractive

    Slurry duty

    [m³/h]
    [m]
    [%]

    Sand 2.65 · limestone 2.7

    [%]
    [%]
    Live Calculation EngineActive Live Sync

    Awaiting Valid Duty Parameters

    Adjust the parameters on the left to compute live hydraulic values, ranges, and sizing verdicts.

    On-Site & Workshop Support

    Slurry eating your pumps?

    Hard solids destroy standard impellers and seals. Our engineers specify hardened, open-impeller and diaphragm pumps for slurry duties.

    Slurry pump sizing explained

    1

    Slurry density first

    A slurry is denser than its carrier liquid, and the power absorbed scales with that density. Slurry specific gravity is calculated from the solids fraction by weight: SG = 1 ÷ ((1 − Cw) + Cw ÷ SG_solid). Ten percent sand (SG 2.65) in water gives about 1.066; twenty percent gives 1.14. Sizing the pump from the water SG would undersize the motor.

    The calculator does this conversion automatically from your solids percentage and solid density.

    2

    Head margin and wear

    Slurry duties deserve a head margin of 15–30 %: solids raise friction losses, and settled solids in the line need extra pressure to re-suspend at restart. The calculator applies the entered margin to the water-duty head before computing power.

    Wear is the other story: impellers, casings and seals erode, so hardened castings, rubber lining or open impellers are standard above about 10 % solids. Magnetic drive pumps must not be used with hard solids — the bushings and magnets cannot survive abrasion.

    3

    Application notes

    Effluent treatment, mining tailings, filter press feed and ash handling are the classic slurry duties. Diaphragm and peristaltic pumps handle high solids at moderate pressure; open-impeller centrifugal pumps handle medium solids at high flow. Teflow’s dewatering and slurry repair service re-builds eroded pumps with hardened parts — call +91 98251 62709 for a recommendation.

    Frequently Asked Questions

    Technical & Operational FAQs

    Q1.How do I calculate slurry specific gravity?

    SG = 1 ÷ ((1 − Cw) + Cw ÷ SG_solid), where Cw is the solids fraction by weight. Ten percent sand (SG 2.65) in water: 1 ÷ (0.9 + 0.1 ÷ 2.65) = 1.066. Use this SG in the power formula — sizing from water undersizes the motor.

    Q2.What head margin should slurry pumps have?

    15–30 % above the clean-water duty is common practice. Solids raise friction, and settled solids need extra head to re-suspend after a stop. The calculator applies your chosen margin to the head before computing power.

    Q3.Can a magnetic drive pump handle slurry?

    No — hard solids destroy the internal bushings and can stop the magnets. Magnetic drive pumps are for clean chemical duties. For solids, use open-impeller centrifugal, diaphragm or peristaltic pumps with hardened or rubber-lined wetted parts.

    Q4.What pumps are used for ETP sludge?

    ETP sludge pumps are typically peristaltic or diaphragm for thick sludge, and open-impeller centrifugal for dilute slurry at higher flows. Sizing follows the same density-and-margin method — enter the sludge solids content in this calculator.

    Q5.Why does my slurry pump overload the motor?

    Slurry density raises absorbed power, and a water-based motor size is too small. Recompute with the slurry SG and add the margin; also check for settled solids at start-up — running against a blocked line overloads the motor even with the right frame.

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    Need a custom hydraulic audit or specific duty curve verification? Call +91 98251 62709 or Request a Detailed Engineering Quote.