| HS Code | 270066 |
| Density | 1.08 g/cm³ |
| Melt Flow Rate | 6.0 g/10 min (190°C/2.16 kg) |
| Carbon Black Content | 30% |
| Volume Resistivity | 100 ohm·cm |
| Tensile Strength | 15 MPa |
| Elongation At Break | 200% |
| Hardness Shore D | 55 |
| Vicat Softening Temperature | 90°C |
| Brittleness Temperature | -70°C |
| Melting Point | 110°C |
| Moisture Content | <0.1% |
As an accredited Cabot CABELEC® CA4918 LDPE, Conductive Compound factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
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Thermoformed matrix trays and wafer shipping carriers for semiconductor and PCB assembly lines are produced from Cabot CABELEC® CA4918 LDPE conductive compound by first extruding sheet of 0.5–3.0 mm thickness, followed by plug-assist forming at sheet surface temperatures of 120–150 °C and mold temperatures of 20–40 °C. The applicable ESD compliance framework is ANSI/ESD S20.20 in conjunction with IEC 61340-5-1; surface resistance is tested to IEC 61340-2-3 or ANSI/ESD STM11.11 at 12% ±3% RH and 23 °C, with a concentric ring probe at 10 V or 100 V depending on the resistance decade. The compound is loaded with a conductive carbon black network in LDPE, so the standard processing ratio is 100% neat resin without dilution; if sheet stiffness must be raised by blending with virgin LDPE, the addition ratio of CABELEC CA4918 should not fall below 80 wt% unless production trials have mapped the non-linear rise in surface resistance. Production problems in this segment concentrate in draw-ratio uniformity: deep thermoformed pockets with draw ratios above 3:1 can fracture the carbon black network enough to push local surface resistance from below 1×106 Ω into the dissipative-to-insulative transition, so post-forming testing should sample the corners, sidewalls, and bottom simultaneously. Sheet extrusion on 60–90 mm single-screw extruders with 24:1–30:1 L/D, a melt pump, flat die, and chill-roll stack is the preferred route; barrel zones from 170 °C to 210 °C are typical, but the melt should not exceed 230 °C to avoid polymer matrix degradation, carbon black plate-out, and processing odour. Finished parts include wafer shipping trays, PCB handling trays, component matrix trays, and stackable dunnage trays used in wafer fabs, PCB assembly, and third-party test houses.
| Verification point | Standard / method | Measurement condition | Instrument / electrode |
|---|---|---|---|
| Surface resistance of tray material | IEC 61340-2-3 | 12% ±3% RH, 23 °C | Concentric ring probe, 10 V / 100 V |
| Surface resistance of planar sheet | ANSI/ESD STM11.11 | 12% ±3% RH, 23 °C | Cylindrical 5 lb electrodes |
| Volume resistance | IEC 61340-2-3 or ASTM D257-14 | 500 V DC, 60 s electrification | Guarded electrode / picoammeter |
| Static decay | IEC 61340-2-1 | ±1000 V, 10% cut-off | Static decay analyser |
Because charge accumulation during solvent transfer is a fire and explosion hazard, blow molded conductive jerrycans and narrow-mouth drums made from CABELEC CA4918 LDPE conductive compound are used in solvent dispensing and flammable powder handling. The primary compliance path is IEC 61340-5-1 for ESD control, with surface resistance measured to IEC 61340-2-3 at 12% ±3% RH; in classified hazardous areas, the end user applies IEC 60079-32-2 for electrostatic hazard assessment. The formulation addition ratio is normally 100% neat compound because dilution with virgin LDPE at as little as 15 wt% can increase surface resistance by several orders of magnitude and must be validated before production. The downstream process is extrusion blow molding on an accumulator-head machine, typically fed by a 65–75 mm grooved-barrel extruder with L/D 25:1–28:1, using a die gap of 1.5–3.0 mm, parison melt temperature of 190–210 °C, mold temperature of 10–30 °C, and blow pressure of 0.5–0.8 MPa; the melt must retain sufficient strength during parison hang without drawing down under its own weight. Process conflicts arise between melt temperature, carbon black dispersion, and drop impact. At a melt temperature below 180 °C, carbon black agglomerates may remain as process-induced defects that reduce low-temperature impact strength; at a melt temperature above 220 °C, parison drawdown lowers wall thickness consistency, and weld lines at the pinch-off zone can show localized surface resistance spikes. Drop impact is tested to ASTM D5276-19 or a customer-specific container drop test; low-temperature brittleness is compared using ASTM D746-14. Terminal products include 5–25 L conductive jerrycans, narrow-neck reagent bottles, and 20–60 L conductive drums for solvent transfer and groundable flammable-powder containers.
At screw speeds above 120 min-1 during injection molding of CABELEC CA4918 LDPE conductive compound, the combination of shear heating and high carbon black loading can shift the melt temperature beyond the target range and alter the conductive network in stackable tote boxes and bins for ESD-protected electronics assembly. The applicable standard for end-user ESD control is ANSI/ESD S20.20 or IEC 61340-5-1, and surface/volume resistance is characterized to IEC 61340-2-3; surface resistance measurements use 10 V and 100 V constant voltage under 12% ±3% RH. The formulation addition ratio is 100% neat compound; if post-industrial regrind is added, the maximum regrind level should be kept at 15–20 wt% and the regrind must be sieved to remove degraded carbon black fines. Processing on hydraulic injection molding machines with clamping force from 2,500 kN to 8,000 kN is typical because wall thicknesses of 3.0–5.0 mm generate long flow lengths in tote-box tooling. Melt temperature is controlled at 190–220 °C, mold temperature at 15–40 °C, and injection speed at low to moderate to avoid frictional shear that orients carbon black and raises surface resistance. The main process failure mode occurs at knit lines: when multiple gates fill a tote-box base, the recombining flow fronts can produce a discrete band of higher resistance. Tooling should be configured with single sequential valve gates or post-mold surface resistance mapping of knit-line regions. Finished parts include stackable tote boxes, ESD bins, component transport boxes, and conductive KANBAN containers used in electronics assembly, repair, and logistics centers.
Blown film lines used for ESD protective packaging made from CABELEC CA4918 LDPE conductive compound operate within a narrow bubble-stability window because the carbon black level that produces surface resistance below 1×106 Ω/sq also reduces melt extensibility. Formulation addition ratio is 100% neat compound; if the film must be heat-sealed to a non-conductive LDPE inner layer, the conductive layer is typically a coextruded skin or the compound is laminated to a carrier, not dry-blended. The downstream production process is tubular film extrusion on a single-screw extruder with L/D 25:1–30:1, a spiral die of 150–300 mm diameter, blow-up ratio 2.0:1–2.8:1, and die gap 0.8–1.5 mm; melt temperature is held at 190–210 °C to maintain carbon black dispersion while avoiding bubble flapping. Because the carbon black network is shear-sensitive, an increase in screw speed above 100 min-1 can transfer excessive shear energy and raise local melt temperature, leading to thin spots that fail surface-resistance uniformity. The industry compliance framework for packaging is IEC 61340-5-1 and ANSI/ESD S20.20; verification uses IEC 61340-2-3 for surface resistance and IEC 61340-2-1 for charge decay on film specimens. Terminal products include ESD bags, moisture-barrier conductive shrouds, component retainer films, and interleave films for PCB kitting. Published data for this specific configuration is limited; therefore, film extrusion parameters and antistatic testing must be validated on production-scale lines, not transferred directly from compression-moulded plaque values.
In SMT lines and ESD-protected workstations, conductive component rails, edge protectors, and PCB transport guides are profile-extruded from CABELEC CA4918 LDPE conductive compound. The applicable compliance standards are IEC 61340-5-1 and ANSI/ESD S20.20, with surface resistance measured by IEC 61340-2-3 on the extruded profile at 12% ±3% RH and 23 °C. The compound is processed neat at 100%; because profile extrusion uses long die lands and back pressure, the addition of virgin LDPE to improve surface finish is not recommended without re-qualification of the conductive network. Downstream process conditions on a 45–65 mm single-screw extruder with L/D 24:1–28:1 include barrel temperature profiles from 160 °C near the feed zone to 200–210 °C at the die; vacuum sizing is preferred over pressure calibration because carbon black-loaded LDPE has lower melt strength than unfilled LDPE. The principal process bottleneck is die drool: carbon black and process-aid decomposition products can build at the die exit after 8–16 h of continuous production, leading to surface defects and inconsistent resistance along the profile. Periodic wiping with copper-brass tooling and avoiding zinc stearate-based cleaning compounds are common production measures. Terminal products include grounded PCB transport guides, SMT component rails, edge protectors for ESD benches, and snap-on conductive covers used in electronics manufacturing and optoelectronics assembly.
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