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Industrial application selection

Pump Bearings: Radial & Thrust Model Selection

This guide concerns rolling bearings in the support assembly, not process-lubricated sleeve bearings. Pump type, impeller geometry, operating point and shaft arrangement determine the reactions that the bearings must support.

Impeller thrustRadial supportFluid exclusionUpdated 1 Oct 2026
A candidate is not a fitment certificate

Keep the evidence with the model shortlist

The models on this page illustrate bearing roles; they are not confirmed replacements for an unspecified machine. Keep the original complete marking, machine position, load and speed duty, temperature, lubricant and mounting arrangement together. Check the candidate's recorded values below and leave unreported parameters unknown.

Check drawings and model records · Investigate a failure before replacing it · Plan installation and force paths

Define the duty

What matters in this application

Operating envelope

Include the normal duty point, start-up and off-design operation when determining radial force and thrust direction.

Bearing arrangement

Identify which bearing locates the shaft and how reverse thrust is resisted. A single angular-contact bearing is not bidirectional thrust support.

Lubrication and sealing

Identify grease or oil supply, housing drainage and possible process-fluid ingress; an integral bearing seal does not replace the pump's mechanical seal.

Choose an architecture

Which bearing structures make sense?

Deep groove ball bearings

Investigate for radial support with axial demand within the bearing's permitted range.

Check first: Do not select by radial rating alone when impeller thrust is significant.

Angular-contact bearing pairs

Consider for defined combined loads and controlled axial location.

Check first: Match contact angle, pairing arrangement, preload/endplay and the manufacturer's set requirements.

Cylindrical radial support

Consider as part of a separate radial/thrust arrangement.

Check first: The thrust bearing and the floating path still need explicit design.

Side by side

Compare the recorded specifications

Different sizes and bearing structures are shown for different duties. C and C₀ are catalogue load ratings, not permissible equipment loads. Limiting speed is not an approved operating speed.

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Pumps — shortlist catalogue data
ParameterSKF6205FAG6306SKF7206 ACCBMKOYO7306B
Bore d (mm)25303030
Outside D (mm)52726272
Recorded width (mm)15191619
Dynamic C (kN)14.830.527.536.6
Static C₀ (kN)7.816.217.319
Catalogue limiting speed (rpm)1800013700220006900

— = not reported, or not directly comparable for a mounted unit. Width conventions differ for inserts, complete units and bearing assemblies; inspect the dimensional drawing. Values are read from the current BearingScope records, not estimated from model numbers.

From shortlist to specification

Work through the selection

  1. Record pump speed, fluid conditions, impeller geometry and the full range of expected hydraulic loads.
  2. Resolve radial reactions and axial thrust at each support, including reverse thrust where applicable.
  3. Choose the locating arrangement and calculate life, static safety and bearing-pair setting.
  4. Review oil level or grease supply, seals, alignment and commissioning temperature before service.
Investigate before replacing

Symptoms worth checking

Axial movement or seal distress

Review thrust direction, bearing arrangement, axial retention and pair setting.

Rust or milky lubricant

Investigate water/process-fluid entry and housing sealing rather than treating a bearing shield as a fluid barrier.

Vibration away from the duty point

Check hydraulic conditions, cavitation, alignment and support loads before assuming a bearing-size problem.

Symptoms are investigation prompts, not a diagnosis. Isolate equipment safely and follow its maintenance procedures before inspection.

Have the original designation?

Look up the complete model and suffix before comparing potential alternatives.

Common questions

Application questions, answered

Can I replace an angular-contact bearing with a deep-groove bearing of the same size?

Not on dimensions alone. Axial capacity, stiffness, location and pairing differ. Confirm the entire arrangement against the pump drawing.

Are sealed bearings enough to stop pumped liquid?

No. Integral seals retain grease and limit some contamination; process-fluid containment is a separate pump-sealing function.

Should pump bearings be back-to-back or face-to-face?

The design determines the arrangement from stiffness, moment loading, alignment and thermal effects. Preserve the specified arrangement and matched-set requirements.

Reference basis & recommendation limits

  • NSK — Bearings for Pumps & Compressors
  • SKF — Bearing selection process

Application principles are informed by the listed technical references. Model shortlists are BearingScope editorial selections from its database, not manufacturer endorsements or equipment-fit approvals. Confirm the latest exact specification and the complete equipment design before use.

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