Ceramic Bead Size Selection for SLS Powder Removal: Matching Mesh to Part Geometry

By Jiangsu Henglihong Technology Co., Ltd.  |  Last updated: July 2026

Bead size is the primary variable in ceramic bead SLS depowdering — more influential than blast pressure on both surface finish Ra and the ability to clean internal channels. Choose too coarse and fine features stay powder-filled; choose too fine and cycle times become impractical. This reference guide provides the complete size selection framework: mesh-to-mm conversion, Ra and cycle time trade-offs, the internal channel sizing rule, and a full selection matrix across all SLS materials and geometry categories.

0.05–0.35 mmPractical bead size range for SLS depowdering
1/4 ruleBead dia. ≤ 1/4 of smallest internal channel
Ra 3–16 µmAchievable range across bead size grades
1.8–2.5×Typical cycle time increase from 0.20 mm to 0.08 mm

1. Why Bead Size Is the Primary Variable

In ceramic bead SLS depowdering, three parameters control the cleaning outcome: bead size, blast pressure, and blast time. Of these, bead size has the broadest influence — it determines both the ceiling on surface finish Ra and the physical access to internal features. Blast pressure adjusts the energy within the range set by bead size; time adjusts coverage completeness. But no amount of pressure increase or extended cycle time can compensate for a bead that is too large to enter a channel that needs cleaning. Bead size must be specified first.

The physics are straightforward. A bead’s kinetic energy is proportional to its mass (which scales with diameter cubed) and the square of its velocity. Doubling bead diameter from 0.10 mm to 0.20 mm increases mass — and therefore kinetic energy — by approximately 8×, at the same velocity. This energy increase delivers faster cleaning but creates a coarser peening action on the surface, producing higher Ra. The trade-off is inherent to the physics and cannot be fully compensated by reducing pressure: using coarser beads at lower pressure gives less energy than fine beads at that same lower pressure, with the additional downside of reduced channel access.

2. Reading Ceramic Bead Size Specifications

Ceramic beads are specified in multiple systems. Understanding the equivalences prevents ordering errors and ensures you match supplier specifications to your process requirements.

Size Range (mm)US Mesh RangeTyler Mesh RangeMedian d₅₀ (µm)Common Application Label
0.05–0.10150–270150–270~70Ultra-fine / Extra-fine
0.10–0.15100–150100–150~125Fine
0.15–0.2560–10060–100~200Medium-fine (standard)
0.25-0.3545–6048–60~300Medium
0.35–0.5035–4535–48~420Medium-coarse

Always request the particle size distribution (PSD) data — specifically d₁₀, d₅₀, and d₉₀ — rather than relying on mesh range alone. A nominal 0.10–0.15 mm bead specification covers a meaningful range of particle sizes; the d₉₀ tells you the upper size limit of 90% of the particles, which governs channel access behaviour. Jiangsu Henglihong Technology Co., Ltd. supplies ISO-classified ceramic beads with full PSD documentation on request.

3. Ra and Cycle Time Trade-offs by Bead Size

The relationship between bead size, achievable Ra, and cycle time follows a consistent pattern across SLS nylon materials. The data below represents ZS ceramic beads on standard PA12 SLS at 60 PSI in a suction-feed cabinet.

Bead Size (mm)Typical Ra Range (µm)Cycle Time FactorPrimary Trade-off
0.05–0.10Ra 3–62.5× baselineFinest finish; longest cycle; limited throughput
0.10–0.15Ra 4–81.6× baselineFine finish; moderate cycle extension; good for appearance parts
0.15–0.25Ra 6–111× (baseline)Standard production range; best throughput per Ra unit
0.25-0.35Ra 9–160.7× baselineFaster cycle; coarser finish; limited to open geometry

The cycle time factor is normalised to the 0.15–0.25 mm range at the same blast pressure and coverage completeness standard. In practice, switching from 0.15–0.25 mm to 0.10–0.15 mm at the same pressure adds 30–60% to cycle time for equivalent PA12 depowdering. Switching to 0.05–0.10 mm adds 120–150%. This time cost must be weighed against the Ra improvement needed for the specific part application.

4. Complete Bead Size Selection Matrix

The table below provides a starting-point bead size recommendation for each combination of SLS material and geometric category. These are starting points, not process specifications; first-article qualification on each new part design establishes the correct protocol for that geometry.

SLS MaterialPart CategoryMin Feature / WallRecommended Bead SizeExpected RaCycle Factor
PA12Large open / simple geometryWall ≥ 3 mm0.20–0.30 mmRa 8–14 µm0.7×
PA12Standard productionWall 2–3 mm0.15–0.25 mmRa 6–11 µm
PA12Complex geometryWall 1.5–2 mm0.10–0.20 mmRa 5–9 µm1.4×
PA12Fine internal channelsChannel 0.6–2 mm0.10–0.15 mmRa 4–8 µm1.8×
PA12Ultra-fine channels / latticeChannel <0.6 mm0.05–0.10 mmRa 3–6 µm2.5×
PA12Pre-dye blast (standard colour)0.15–0.20 mmRa 6–10 µm
PA12Pre-dye blast (light/bright colour)0.10–0.15 mmRa 4–7 µm1.4×
PA12-GBStandard (glass-filled)Wall ≥ 2 mm0.20–0.30 mmRa 10–18 µm1.2×
PA11Standard geometryWall ≥ 2 mm0.15–0.25 mmRa 6–12 µm
PA11Complex / flexible assemblyWall 1–2 mm0.10–0.15 mmRa 5–10 µm1.5×
TPU A85–95Standard body geometryWall ≥ 2 mm0.08–0.15 mmRa 10–16 µm1.5×
TPU A85–95Lattice / fine wallStrut ≥ 1.5 mm0.05–0.10 mmRa 12–20 µm2.0×
TPU A75–85AnyAny ≥ 1.2 mm0.05–0.10 mmRa 12–22 µm2.2×

5. The Internal Channel Sizing Rule

Internal channels — fluid passages, wire routing tunnels, articulation slots, venting channels — are among the most common depowdering failure points in SLS production. The powder-cake removal phase and compressed-air blow-off do not clean them; ceramic bead blasting is the only reliable method. But only if the beads can physically enter.

The One-Quarter Diameter Rule

Maximum safe bead diameter = smallest internal channel diameter ÷ 4

  • 4 mm channel → beads ≤ 1.0 mm (any standard size)
  • 2 mm channel → beads ≤ 0.50 mm (0.25–0.35 mm range works comfortably)
  • 1.5 mm channel → beads ≤ 0.375 mm (use 0.25–0.35 mm)
  • 1.0 mm channel → beads ≤ 0.25 mm (use 0.15–0.25 mm)
  • 0.6 mm channel → beads ≤ 0.15 mm (use 0.10–0.15 mm)
  • 0.4 mm channel → beads ≤ 0.10 mm (use 0.05–0.10 mm)

The one-quarter ratio provides the clearance margin needed for beads to enter, impact the channel wall, and exit without bridging. Beads at exactly the channel width — or larger — will bridge the entrance opening, forming a plug that prevents further entry. Bridging is particularly problematic because it is not immediately visible during blasting; the channel exit appears clean under casual inspection but the interior wall carries full semi-sintered skin.

For blind channels — those that do not have an exit — bead blasting is inherently limited. Beads enter but cannot exit; they pack the channel. For blind channels with diameters above 4 mm, compressed-air blow-out mid-cycle can dislodge accumulated beads and allow additional cleaning passes. For blind channels below 2 mm, manual compressed-air depowdering is more practical than media blasting.

6. Multi-Geometry Build Strategy

A common SLS production scenario: a single build contains multiple part designs, some with fine internal channels (requiring 0.10–0.15 mm beads) and others with simple open geometry (where 0.20–0.30 mm beads would suffice for faster throughput). How should bead size be selected for the batch?

Set bead size for the finest feature that requires blasting. In the example above, use 0.10–0.15 mm beads for the entire batch. The simple-geometry parts will be adequately blasted at fine bead size — the only consequence is a longer cycle time than strictly necessary for those parts. Do not compromise channel cleaning to protect throughput on simpler parts.

The exception: if the build contains a large quantity of simple-geometry parts and only a few complex-geometry parts, it may be economical to blast the two groups in separate cycles at different bead sizes. Run the simple-geometry parts at 0.20–0.30 mm for fast throughput, then switch to 0.10–0.15 mm for the complex parts. This requires media purging between cycles if you maintain a single cabinet — approximately 2–5 minutes of purge time — which must be included in the throughput calculation.

7. Bead Size Selection for Pre-Dyeing Blast

When the ceramic bead blast cycle serves as surface preparation for dyeing — as it does in the majority of PA12 and PA11 SLS colour production — the bead size selection must account for the relationship between surface Ra and dye uptake depth.

Finer beads produce lower Ra, which means less surface micro-porosity per unit area and shallower dye penetration. Coarser beads produce higher Ra, more surface area per projected unit, and deeper colour. This relationship can be used as a direct process control variable:

  • Target: deep black, navy, or dark grey: use 0.15–0.25 mm beads (Ra 7–10 µm) for maximum colour depth
  • Target: standard commercial colours (red, blue, green): use 0.12–0.20 mm beads (Ra 6–9 µm) — balanced depth and colour uniformity
  • Target: light pastel shades or custom light tones: use 0.08–0.15 mm beads (Ra 4–7 µm) to limit dye uptake depth and achieve lighter saturation

This bead size-to-colour relationship assumes constant dye bath concentration and temperature. When establishing a new colour standard, blast a reference coupon at two bead sizes (one coarser, one finer), dye both in the standard bath, and measure colour depth with a spectrophotometer to identify which size delivers the target ΔE from the colour standard.

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Related Reference Color Consistency and Dye Preparation for SLS Parts After Ceramic Bead Blasting

Bead size to colour depth relationship data, pre-dye blast protocols by colour target, and batch colour consistency measurement methodology.

Часто задаваемые вопросы

The 0.15 to 0.25 mm size range (approximately 60–100 mesh) is the most widely used for standard PA12 SLS production with moderate geometric complexity. It delivers Ra 6–11 µm at standard blast pressures of 55–70 PSI, with cycle times of 5–10 minutes for medium-complexity parts. This range balances cleaning effectiveness, surface finish quality, and cycle time efficiency — making it the default starting point for most PA12 operations and the baseline in the cycle time table in this article.

Apply the one-quarter rule: the maximum safe bead diameter equals one-quarter of the smallest internal channel dimension that needs cleaning. For a 2 mm channel, use beads ≤ 0.5 mm; for a 1 mm channel, ≤ 0.25 mm; for a 0.6 mm channel, ≤ 0.15 mm; for a 0.4 mm channel, ≤ 0.10 mm. Beads above this threshold bridge the channel entrance — accumulating at the opening rather than entering and impacting the interior wall — leaving the channel interior unblasted and powder-filled despite an apparently clean exterior.

Reducing bead size by one class — for example, from 0.15–0.25 mm to 0.10–0.15 mm — typically increases cycle time by 30 to 60% to achieve equivalent cleaning coverage, because smaller beads deliver less energy per impact and cover less area per pass. Moving from 0.15–0.25 mm all the way to 0.05–0.10 mm typically adds 120–150% to cycle time. The exact increase depends on part geometry and blast pressure. For operations where surface finish Ra is the primary driver, the longer cycle at finer bead size is worth the throughput trade-off. For operations where throughput matters and Ra 7–11 µm is acceptable, stay with the 0.15–0.25 mm range.

Blending two size fractions is generally not recommended for SLS depowdering. A mixed charge produces a Ra value between the two grades, which may not satisfy either requirement adequately. Fine beads in the mix may bridge fine channels while coarse beads are too large to enter; and the mixed charge makes Ra monitoring unreliable as the size ratio shifts over time with differential degradation rates. The better approach: set bead size for the finest feature requiring cleaning and accept the longer cycle time on simpler parts, or run separate blast cycles for complex and simple groups.

Related Articles in This Series

Return to the Ceramic Beads for SLS Powder Removal — Complete Guide for the full overview.

Blast Pressure and Cycle Time Optimization

Once bead size is set, this guide optimises pressure, nozzle setup, and cycle time.

Surface Finish Ra Values After Ceramic Bead Blasting

Full Ra dataset by bead grade, size, and pressure — with measurement protocol.

PA12 SLS Depowdering Protocol

PA12-specific protocol applying the size selection principles in this article.

Ceramic Bead Blasting for TPU Flexible SLS

Fine bead selection and low-pressure protocol for flexible SLS materials.

Color Consistency and Dye Preparation

How bead size selection controls colour depth in dyed PA12/PA11 SLS parts.

Wet vs. Dry Ceramic Bead Blasting

How wet blasting modifies the Ra-to-bead-size relationship for SLS nylon.

Get ISO-Classified Ceramic Beads for Your SLS Bead Size Specification

Jiangsu Henglihong Technology Co., Ltd. supplies ZS and ZrO₂ ceramic blasting beads in ISO-classified size ranges from 0.05 mm to 0.60 mm with full PSD documentation. Tell us your channel dimensions and Ra target — we will specify the right size range and supply a calibrated sample for first-article qualification.

Request Samples & PSD Data
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