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Select By Viscosity Target

Match fumed silica grade and loading level to your exact viscosity target — from light anti-settling at 1% to structural anti-sag putty at 12%.

Match fumed silica grade and loading level to your exact viscosity target — from light anti-settling at 1% to structural anti-sag putty at 12%.

1–2%
Anti-settling range
4–6%
Thixotropic paste zone
8–12%
Anti-sag putty range
200–380 BET
m²/g span

Low Loading (1–2%): Anti-Settling and Light Thixotropy

At 1–2 wt% loading, fumed silica provides enough hydrogen-bonded network to prevent pigment settling without significantly raising application viscosity. A grade like SEMISIL 200 (BET 200 ± 25 m²/g, primary particle ~12 nm) delivers 500–2,000 mPa·s viscosity build in epoxy systems — sufficient for storage stability while preserving sprayability. In polyester gelcoats, 1.5% of a 200 m²/g hydrophilic grade raises Brookfield viscosity from ~800 to ~3,000 mPa·s at 20 rpm. The network is fully shear-thinning: viscosity drops 80–90% under spray shear (\>10,000 s⁻¹), then rebuilds within 30–90 seconds at rest.

Moderate Loading (3–5%): Thixotropic Pastes and Adhesives

Between 3–5 wt%, fumed silica transforms liquid resins into structured thixotropic pastes suitable for gap-filling adhesives and brush-applied coatings. Higher surface area grades (300–380 m²/g, primary particle ~7 nm) achieve the same viscosity build at lower loading than 200 m²/g grades — typically 3% vs 4.5% to reach 25,000 mPa·s in a bisphenol-A epoxy. This matters for formulation cost and filler space. In silicone sealants, 4% of a hydrophobic (dimethylsilyl-treated) grade at 300 m²/g BET yields a non-slump bead with yield stress above 200 Pa. See our viscosity build curves for grade-by-grade comparisons across binder families.

High Loading (6–8%): Anti-Sag Coatings and Thick-Film Systems

Loading fumed silica to 6–8 wt% creates strong anti-sag behavior for vertical-surface coatings and thick-film systems that must resist flow before cure. At 7% loading of a 200 m²/g hydrophilic grade in unsaturated polyester, Brookfield viscosity exceeds 80,000 mPa·s at 20 rpm while remaining trowelable under moderate shear. The silanol-driven network creates a yield stress of 400–800 Pa — enough to hold 3–5 mm wet film thickness on vertical surfaces. Hydrophobic grades require ~15% higher loading to match the same yield stress because surface methyl groups reduce inter-particle hydrogen bonding density.

Extreme Loading (8–12%): Structural Putty and Body Filler

Above 8 wt%, fumed silica produces non-flowing putties and body fillers with yield stresses exceeding 1,500 Pa. At 10% of a 200 m²/g grade in epoxy, the system behaves as a soft solid at rest (G′ \> 50 kPa) but flows under spatula pressure. Dispersion becomes critical at these loadings — incomplete wetting leaves agglomerates that act as stress concentrators, reducing final mechanical strength by 20–40%. High-speed dissolvers (tip speed ≥18 m/s) or three-roll mills are mandatory. For formulators needing extreme thixotropy at lower loading, switching to a 380 m²/g grade achieves putty-like rheology at 7–8% instead of 10–12%, freeing volume for functional fillers.

Grade vs. Loading: Quick Selection Matrix

The table below maps common fumed silica grades to the loading range needed for each viscosity target in a standard liquid epoxy (EEW 185–192). Actual values vary with resin chemistry, dispersion quality, and temperature — always validate with your specific system. Higher BET grades deliver more viscosity per percent loading but cost more per kilogram; total formulation cost often favors the higher grade because you use less.

Grade (BET m²/g)Anti-Settle (mPa·s)Thixo Paste (mPa·s)Anti-Sag (mPa·s)Putty (mPa·s)
150 m²/g2.0–2.5%: ~2,0005–6%: ~20,0008–9%: ~70,00011–12%: >150,000
200 m²/g1.5–2.0%: ~3,0004–5%: ~25,0006–7%: ~80,00010–11%: >150,000
300 m²/g1.0–1.5%: ~3,5003–4%: ~30,0005–6%: ~90,0008–9%: >150,000
380 m²/g0.8–1.2%: ~4,0002.5–3.5%: ~35,0004–5%: ~100,0007–8%: >150,000

For most industrial formulations, start with a 200 m²/g hydrophilic grade at the midpoint of the loading range for your viscosity target, then adjust ±0.5% based on actual dispersion results — switching to a 300 m²/g grade only when formulation volume constraints demand lower silica loading.

FAQ

How does BET surface area affect the loading needed for a given viscosity?

Higher BET surface area means more silanol groups per gram, producing a denser hydrogen-bonded network at lower loading. A 300 m²/g grade typically needs 25–35% less loading than a 200 m²/g grade to reach the same viscosity in the same resin system. The relationship is not linear — doubling BET does not halve the required loading.

Why does hydrophobic fumed silica need higher loading than hydrophilic for the same thixotropy?

Hydrophobic surface treatment replaces silanol (Si-OH) groups with methyl or dimethylsilyl groups, reducing inter-particle hydrogen bonding. This weakens the thixotropic network, requiring 10–20% more loading to match the yield stress of an untreated hydrophilic grade at the same BET surface area.

What dispersion equipment is recommended above 6% fumed silica loading?

Above 6 wt%, high-speed dissolvers with tip speeds of 18–25 m/s are the minimum. For loadings above 8%, three-roll mills or high-pressure homogenizers deliver better deagglomeration. Incomplete dispersion at high loading wastes material and creates weak points in cured films.

How long does viscosity recovery take after shear in a fumed silica thixotropic system?

Recovery to 80% of rest viscosity typically takes 30–120 seconds depending on grade and loading. Higher surface area grades and higher loadings recover faster because the denser silanol network re-forms hydrogen bonds more quickly. Full recovery to 95%+ can take 5–15 minutes.

Can I mix two fumed silica grades to fine-tune viscosity?

Yes, blending a 200 m²/g and a 380 m²/g grade is a practical way to hit an intermediate viscosity target without changing total loading. A 50:50 blend behaves roughly like a 280 m²/g single grade. Pre-blend the powders dry before adding to the resin for uniform distribution.

Does temperature affect fumed silica thixotropy performance?

Hydrogen bonding weakens with rising temperature, so viscosity at rest drops 5–15% per 10°C increase between 20–60°C. The shear-thinning ratio remains largely unchanged. Formulators targeting hot-climate anti-sag performance should validate at 40–50°C, not just at 25°C lab conditions.

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