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HODD Model TP32 with a transparent pump head in the HODD test facility, the blue-dyed test slurry visible inside

Construction industry · Model TP · size TP32

When the finest particles grind away every seal

Silicate slurries are among the most demanding media in process engineering. Precisely because their particles are so small, they reach into every sealing gap — and act there like an abrasive.

Customer

Building materials manufacturer, Germany

Range used

Model TP · size TP32

0

Mechanical seals in the pumped medium

several thousand €

Cost per failure previously

up to 30 %

Solids content of the medium

Technical data

Industry
Construction industry
Region
Germany
Process step
Transfer and filling
Medium
silicate slurry, alkaline
Solids content
up to 30 %
Particle size
0.3–5 nm
Density
1.3 kg/dm³
Temperature
30 °C
Operating mode
shift operation
Materials
PP and PE
Previously in use
progressive cavity pump
Implementation
2026

The starting point

Silicate slurries consist of the finest mineral particles suspended in a liquid. In this case they are in the nanometre range, at a solids content of up to 30 per cent. That fineness is exactly the problem: the particles reach sealing gaps that no coarse grain would ever enter.

A progressive cavity pump currently handles the duty. In its mechanical seal, the silicate particles acted like an abrasive and continuously wore down the sealing faces. The consequences came as a chain: growing leakage, falling service life, rising maintenance effort. The medium's tendency to crystallise made it worse, putting additional load on sealing faces and moving parts. Rotor and stator wore as well. The operator puts the cost of a single failure at several thousand euros — and failures kept coming.

A second problem was just as tiresome in daily operation: the alkaline medium foams when air is drawn in. The foam extended the filling time per canister, and whatever overflowed was lost.

Investigated first, then engineered

Before a suitable pump was identified, the slurry was investigated in the HODD test facility under realistic conditions. Three questions were central: how does the medium behave while being pumped, how strongly does it foam, and what does that mean for the hydraulics of the pump?

The test rig works with a transparent pump head. That makes visible in operation what normally stays hidden: how the chamber fills, how the medium behaves during the stroke, whether and where air is drawn in. The photographs on this page come from those trials; the blue dye makes the fill level inside the head readable.

Only on that basis was the concept for the pump developed.

The solution

The ideal solution is a Model TP–type pump, with wetted parts in polypropylene and polyethylene.

The decisive design feature is an absence: no rotating shaft and no mechanical seal work inside the pumped medium. That removes exactly the place where the silicate particles previously settled and wore down the sealing faces. It simply no longer exists.

A second property addresses the foaming: flow velocities inside the pump are low. The medium is handled more gently, and less air is drawn in than with a design that accelerates it.

The result

The operator receives a proposed solution whose design rests on trials with their own medium rather than on a data sheet. The wear point that previously caused recurring cost is no longer present by design.

One note for context: implementation is planned for 2026. The statements on wear, foaming and energy demand rest on the trials in the test facility and on the design of the pump, not on measurements in running plant operation.

From the project

  • The test pump draws the slurry from the supply container, the transparent pump head completely filled
  • View into the transparent pump head during the stroke — the chamber is half filled

Contact

We are happy to advise you personally — simply send us your enquiry via the form. For reliable sizing it helps us to have details on the medium, solids content, flow rate and pressure requirement.