The paddle shaft of a powder mixer, and how it comes out for cleaning
The illustrated paddle shaft has been drawn out of its stainless trough: angled flat paddles welded to a tube, a bearing housing and drive at one end only. In a powder line this is the mixing element. Its speed is not chosen by feel; it is set so the paddles throw material up into a fluidised zone without grinding it, and that point is defined by the Froude number. The single-ended bearing is what lets the whole shaft come out for cleaning.
Covers paddle shafts (paddle wheels) in batch powder mixers: the Froude number and the speed it sets, the fluidised mixing zone of double-shaft paddle mixers, fill level, mixing time and liquid addition, access options including extractable cantilevered shafts, and discharge valves. Loss-in-weight powder feeders are on Powder Feeder (1418); ingredient and bag-tip hoppers on 825 and 966; batching and blending systems on 403. Paddle-wheel aerators for ponds and paddle-wheel flowmeters share the name but are outside this page.
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PowderProcess.net defines the Froude number in powder mixing as the ratio of the forces other than gravity, centrifugal force above all, to gravity, calculated from the mixing tool's radius and angular speed, and uses it to sort dry mixers by how particles move.
PowderProcess.net's paddle-mixer page sets the speed of a double-shaft paddle mixer to reach Fr 1–1.1, where the paddles lift the solids into a fluidised zone, and says that running above Fr 1–1.1 shortens the mixing time little while the extra energy degrades the solids by breaking particles, and gives the speed by setting Fr = 1.1 for the tool radius. With Fr = Rω²/g, a paddle radius of 0.3 m needs ω = √(1.1 × 9.81 ÷ 0.3) ≈ 6.0 rad/s, about 57 rpm and 1.8 m/s tip speed; a 0.5 m radius needs about 44 rpm and 2.3 m/s (Editorial calculation).
Larger mixers therefore turn slower for the same fluidisation, while their paddle tips move faster.
| Froude number | Particle behaviour (PowderProcess.net) |
|---|---|
| Fr < 1 | Gravity exceeds inertia; dense-phase mixing, particles rolling over each other |
| Fr ≈ 1 | Tipping point; particles can be put in suspension and fluidisation occurs |
| Fr above about 6–7 | Powder centrifuged into a ring on the wall |
The Fr = Rω²/g form is the standard definition; PowderProcess.net's own equation images were not reproduced here.
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PowderProcess.net lists the operating parameters that set how fast a double-shaft paddle mixer reaches the required homogeneity.
Profiled paddles set at an angle promote both radial and axial movement, which PowderProcess.net links to the total mixing time. The angled paddles on the illustrated shaft are that feature.
Gericke states that its double-rotor Multiflux GMS mixes multiple powders and liquids into a homogeneous mixture even with quantities below 0.01 percent.
| Parameter | PowderProcess.net |
|---|---|
| Batch size | Minimum 30–40% and maximum 70–80% of total mixer volume |
| Speed | Calculated and set to Fr 1–1.1 |
| Minor ingredients | Added after the main ingredients or sandwiched, preferably into the central area |
| Mixing time | 30 s to 2–3 min for a dry mix; longer points to a setting problem |
| Liquid addition | A few percent of batch weight for light agglomeration; more needs deagglomerators (high-speed choppers) |
| Homogeneity | Set by the user and tested at qualification by sampling and analysis |
PowderProcess.net's mixing-time range is stated for double-shaft paddle mixers with a fluidised zone; single-shaft paddle mixers work on a different principle.
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Paddle mixers differ in how the chamber is opened for cleaning; the illustrated shaft shows the extractable option, first in PowderProcess.net's list ordered by ease of access.
Kemutec's point is the hygienic one: every bearing and seal inside or at the wall of the product zone is a place for residue, and a cantilevered shaft removes a set of them at the non-drive end. The trade-off is a shaft supported from one side only (editorial reading).
| Option | Source |
|---|---|
| Access options by ease: extractable shafts, front door, side doors, opening top cover | PowderProcess.net |
| Cantilevered shafts (bearings on one side) as an option on some makes, letting the shaft be extracted and the chamber left empty for cleaning | PowderProcess.net |
| Gericke ECD: drive shaft and mixing rotors on rails, extracted at the press of a button for 360° access; FDA and GMP-oriented stainless construction, continuously welded seams; six models from 36 to 1,320 gal | Gericke via Powder & Bulk Solids |
| Kemutec Gardner: cantilever agitator removes one set of bearings and seals at the non-drive end; full-diameter hinged, interlocked door; plough, paddle or interrupted spiral agitators | Kemutec via Powder & Bulk Solids |
| Discharge: rectangular flap valves; hygienic round valves with smaller gaps but slower discharge; bomb doors opening the whole bottom, discharge under 30 s and little residue | PowderProcess.net |
Gericke and Kemutec descriptions are from product announcements published in Powder & Bulk Solids.
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Paste it into your enquiry below or into an email to a maker, then replace every bracket.
Give the powders, bulk densities and particle sizes, batch volume and minor-ingredient fractions, any liquid addition, required homogeneity and test method, cleaning regime (dry, wet, full washdown) and hygiene standard, and discharge requirements. Ask for paddle radius, speed and resulting Froude number, fill range, mixing time trials, access option (extractable or cantilevered shaft, doors), seal type at the shaft, discharge valve type and residue.
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PowderProcess.net's paddle-mixer page sets the speed to reach Fr 1 to 1.1 for double-shaft paddle mixers with a fluidised zone, and warns that higher values shorten mixing little while breaking particles. [1] [2]
At Fr = 1.1, about 57 rpm with a tip speed of about 1.8 m/s (Editorial calculation from Fr = Rω²/g). [2]
PowderProcess.net gives a batch of at least 30–40% and at most 70–80% of total mixer volume. [2]
Sources checked 2026-10-13. Two pages from a powder-processing engineering reference site, and two mixer announcements from Gericke and Kemutec published in Powder & Bulk Solids.
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