Barium Sulfate BaSO4 Polymer for X-ray Shielding BOPET Film
Semi-dull Barium Sulfate Polyester Masterbatch
Barium sulfate (BaSO₄) polyester chip is a concentrated composite material where ultrafine BaSO₄ particles are uniformly dispersed within a polyester carrier resin.
Key Advantages
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Superior Density & Weighting
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Boasts density up to 4.0 g/cm³ (vs. 1.3-1.4 g/cm³ for pure polyester)
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Ideal for counterweights, vibration damping, and balance components.
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X-ray & Gamma Ray Shielding
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The high atomic mass of barium provides exceptional radiation attenuation
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Critical for:
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Medical equipment (aprons, CT scanner parts)
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Nuclear shielding
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Aerospace components
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Enhanced Mechanical Properties
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Improves stiffness (+30-50%) and dimensional stability
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Reduces warpage in thin-walled parts
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Chemical Resistance
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Resists acids, alkalis, and solvents better than mineral-filled composites
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Aesthetics & Surface Quality
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Delivers bright white coloration and high gloss finish
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Minimal impact on transparency at low loadings (<15%)
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Production Methods
Two production methods are twin-screw extrusion granulation and polymerization process addition (in-situ polymerization).
▶ 1. Twin-Screw Compounding Process
Process Flow:
Feedstock Prep: Dry polyester (PET/PBT) chips/recyclate + surface-treated BaSO₄ powder (silane/titanate coupling agents) + additives.
Pre-mixing: Dry-blend components uniformly.
Extrusion: Melt-mix in a co-rotating twin-screw extruder → high shear disperses BaSO₄.
Devolatilization: Remove moisture/VOCs via vacuum vents.
Melt Filtration: Screen impurities.
Pelletizing: Strand-cut into masterbatch pellets.
Drying/Packaging.
Advantages:
✅ Mature & flexible technology
✅ Lower CAPEX (vs. polymerization)
✅ Fast production (continuous process)
✅ Easy formula adjustments (filler: 30-85%)
✅ Accepts recycled polyester
✅ Quick product changeovers
Disadvantages:
⚠️ Limited dispersion (agglomeration risk)
⚠️ Weaker polymer-filler interface bonding
⚠️ Potential polymer degradation (MW loss)
⚠️ High energy consumption
⚠️ Demands ultra-fine BaSO₄ powder
Specs:
| Testing Items | Unit | Standard | Test Value | Testing Method |
| Value of Chromatism | △E | ≤1.0 | ≤0.40 | Q/XLM03-2022 |
| Melting Point | ℃ | 252±3 | 252 | GB/T14190-2017 |
| Intrinsic Viscosity | dl/g | 0.20±0.02 | 0.201 | GB/T14190-2017 |
| Filtration Pressure Difference (DF) | MPa | ≤1.50 | 0.80 | Q/XLM03-2022 |
| Weight of 100 particles | g | 3.0±0.15 | 3.06 | Q/XLM03-2022 |
| Moisture Content | % | ≤0.30 | 0.15 | GB/T14190-2017 |
| Irregular Chip | % | ≤0.20 | 0.09 | Q/XLM03-2022 |
| Ash Content | % | 60%±2% | 60.1 | Q/XLM03-2022 |
| Remark | 60% BaSO4 Content | |||
▶ 2. Polymerization (In-situ) Process
Process Flow:
Feedstock Prep: Polyester monomers (PTA/DMT + MEG) + catalyst + specialty BaSO₄ slurry (in MEG) / soluble barium salts.
Esterification: Add BaSO₄ during the reaction.
Polycondensation: Synthesize polymer around BaSO₄ particles.
Pelletizing: Cut polymer melt into chips.
Advantages:
✅ Superior dispersion (nano-level)
✅ Stronger interfacial bonding
✅ Minimal polymer degradation
✅ Higher melt flow at equal loading
✅ Higher product purity
Disadvantages:
⚠️ Complex process control
⚠️ Very high CAPEX/OPEX
⚠️ Low flexibility (fixed formulas)
⚠️ Catalyst poisoning risk
⚠️ Byproduct removal challenges
⚠️ Requires ultra-pure BaSO₄ slurry
Specs
| Items | Unit | Standard (low IV) | Standard (High IV) | |
| Intrinsic Viscosity | dl/g | 0.65±0.015 | 0.72±0.020 | |
| COOH Value | mmol/Kg | ≤ 35 | ≤ 30 | |
| Melting Point | ℃ | ≥ 259 | ≥ 259 | |
| Color Value | L | ≥ 54 | ≥ 70 | |
| b | 4.0±2.0 | 2.0±2.0 | ||
| Water Content | % | ≤ 0.4 | ≤ 0.4 | |
| Irregular Chip & Powder | % | ≤ 0.4 | ≤ 0.4 | |
| BaSO4 Content | ppm | 2700±250 | 2700±250 | |



