| HS Code | 128462 |
| Product Name | Cabot HDPE CA6739 |
| Material Type | Electrically conductive high-density polyethylene compound |
| Color | Black |
| Form | Pellets |
| Density | 1.15 g/cm³ |
| Melt Flow Rate | 10 g/10 min (190°C/2.16 kg) |
| Carbon Black Content | 30% |
| Volume Resistivity | 1 × 10^3 ohm·cm |
| Surface Resistivity | 1 × 10^4 ohm/sq |
| Tensile Strength At Yield | 24.1 MPa |
| Tensile Strength At Break | 20.7 MPa |
| Elongation At Break | 200% |
| Flexural Modulus | 965 MPa |
| Hardness Shore D | 60 |
| Thermal Stability | 250°C |
| Moisture Content | 0.20% |
As an accredited Cabot HDPE CA6739 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Cabot HDPE CA6739 is typically packaged in 25 kg bags or 1,000 kg bulk bags for industrial handling and storage. |
| Container Loading (20′ FCL) | Cabot HDPE CA6739 is loaded into a 20-foot FCL container in 25 kg bags on pallets, shrink-wrapped and securely fastened. |
| Shipping | Cabot HDPE CA6739 (carbon black/polyethylene masterbatch) is not classified as dangerous goods for transport. Ship as a non-hazardous solid in sealed 25 kg bags or 1000 kg bulk bags. Protect from moisture and excessive heat. No UN number, hazard class, or packing group required. Always verify current SDS. |
| Storage | Store Cabot HDPE CA6739 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep original containers tightly closed to prevent moisture, dust, and contamination. Avoid static buildup and physical damage. Use first-in, first-out rotation. Maintain ambient conditions, generally below 50°C, and separate from strong oxidizers. Store in original packaging. Do not stack excessively high. |
| Shelf Life | Shelf life is typically 24 months from manufacture when stored in original, sealed packaging, cool, dry, and away from sunlight. |
Extruded conductive sheet from Cabot HDPE CA6739 is converted into thermoformed ESD trays, tote boxes and matrix frames for semiconductor back-end and PCB assembly lines. The sheet is produced on a 75–90 mm single-screw extruder with a 30:1 L/D barrier screw, a screen pack of 60/100/60 mesh, and a three-roll vertical stack set to 85–95 °C. Melt temperature measured at the die is restricted to 205–218 °C. Sheet thickness is normally maintained at 3.2–4.8 mm with a maximum thickness tolerance of ±0.12 mm. Roller gap and polishing pressure are adjusted to avoid surface gloss variation because gloss difference changes the four-point probe contact footprint. The formed tray is tested according to ASTM D257 on all vertical walls, bottoms and rib intersections after 48 h at 23±2 °C and 50±5% relative humidity per ISO 291. The acceptance band is a surface resistivity of 10⁴–10¹¹ Ω/sq under ANSI/ESD S20.20, but most semiconductor end users specify 10⁴–10⁷ Ω/sq on load-bearing surfaces. The most frequent process failure is not thermal degradation but regrind-induced electrical anisotropy. Edge trim and skeletal scrap may be reintroduced into the sheet line at a maximum 15 wt% with a single regrind pass. Above 20 wt% regrind, the carbon black network aligns in the machine direction and the cross-machine wall resistance can rise to 10¹⁰–10¹² Ω/sq. This failure is not fixable by increasing thermoforming heater dwell time. The electrical network is damaged in the extruder, not in the former. The thermoforming station uses a plug-assisted process with a plug temperature of 100–110 °C, a sheet surface temperature of 158–170 °C, and a draw ratio not exceeding 1.4:1 to avoid excessive sidewall thinning below 1.8 mm. Continuous service temperature is limited to 65 °C because the HDPE matrix softens above this point and allows carbon-rich phase relaxation with local resistivity drift.
Extrusion blow moulding of CA6739 into automotive fuel filler necks, vapour return lines and tank accessory bodies is carried out on a shuttle or accumulator-head machine with a 24:1 L/D barrier screw and a compression ratio of 2.5:1. The accumulator head is held at 210–225 °C and the parison drop time is maintained between 2.5 and 4.0 s for a target parison weight tolerance of ±1.5 g. Carbon black loading raises melt viscosity and shortens the sag window relative to unfilled HDPE. Operators therefore rely on die-gap adjustments of ±0.3 mm rather than melt temperature changes. Mould halves close at a clamp force of 150–250 kN for small filler necks, with a pinch-off land length of 1.5–2.5 mm and a mould temperature of 15–25 °C. The critical electrical specification is a surface resistivity of ≤10⁶ Ω/sq when measured according to SAE J1645 on the inner and outer wall after 24 h. Failures concentrate in the pinch-off weld line. If the melt temperature at the pinch-off falls below 195 °C, the carbon black network fails to bridge the parting line and resistance jumps to 10¹² Ω/sq. Raising the overall barrel temperature above 235 °C is not a valid corrective action because surface oxidation creates a high-resistance skin and degrades impact properties measured by ASTM D256. The accepted corrective action is to increase die gap by 0.4 mm and slow the parison drop so that the weld line compresses with higher melt thickness. Blow air pressure is held at 0.6–0.8 MPa with an exhaust time of 15–20 s. Early exhaust causes sidewall flexing and can fracture the conductive network in the hinge zone. All parts are shrink-wrapped in low-charging film after cooling to 30 °C.
ATEX containers and transfer hoppers for combustible powder handling are injection moulded from CA6739 using a 400–800 t hydraulic or toggle clamp machine, depending on shot weight. The screw is a 20:1 L/D low-shear design with a compression ratio of 2.0:1 and a back pressure of 0.6–1.2 MPa. Melt temperature is set to 210–232 °C, and mould temperature is controlled at 30–50 °C. The governing electrical criterion is resistance to earth ≤10⁶ Ω between any point on the article and a groundable insert, measured according to IEC TS 60079-32-1. Each production lot is sampled at 10 points per 40 parts, including rib bases and gate vestiges. A repeated failure mode is over-shear in valve-gated hot runners. When hot-runner pressure drop exceeds 20 MPa, residence time increases and the carbon black-particle network disperses further, shifting volume resistivity from 10² Ω·cm to 10⁴ Ω·cm and above. This is detected as a wider resistance distribution, not as a visual defect. The moulding shop therefore preselects hot-runner nozzle tips with a minimum bore of 2.0 mm and avoids 0.5 mm point gates. Cold-runner regrind from sprue puller systems is capped at 10 wt%. Higher fractions create filler orientation that produces conductive striping on the container floor. Demoulding is performed with air ejection where possible because scratches create insulating microgrooves that can raise surface resistance by half a decade. Finished containers are stored in closed polyethylene bags, not open cardboard boxes, because paper dust deposits on the carbon-rich surface after 72 h and causes local resistance to exceed 10⁸ Ω.
In spiral-wound multi-layer ducting for solvent vapour and explosive dust extraction, CA6739 is run as the inner conductive layer over a structural HDPE core. The coextrusion line is fitted with a 60–75 mm extruder for the structural layer and a 35–45 mm extruder for the conductive layer, both with barrier screws of 24:1 L/D. The conductive inner layer thickness is kept between 0.5 and 0.8 mm. Below 0.35 mm the corrugator motion draws the carbon black phase into machine-direction ribbons, producing non-conductive striping that is visible only under a four-probe resistivity map. Melt temperature of the conductive layer is set to 215–225 °C; the structural HDPE layer is run at 210–220 °C. The difference in melt viscosities between the two layers is kept below 15%, because a larger gap triggers interfacial instability and folds the conductive layer into isolated pockets. End-of-line electrical testing is performed with a cylindrical electrode set at 100 V DC. The acceptance value is ≤10⁶ Ω per ISO 8039 for flexible hoses, and ASTM D257 is commonly used for rigid duct sections. After corrugation, the part is cooled in a water bath at 20 °C and cut in 6 m lengths. The most serious field failure is caused by solvent absorption into the HDPE matrix. If the duct is used continuously with ketone-containing vapour at concentrations above 2%, the matrix swells and the conductive layer can debond from the structural core. The debonding is not detectable by visual inspection but appears as a surface resistance increase above 10⁹ Ω in monthly audits. For this reason the system is qualified only for vapour streams with limited aromatic and ketone exposure. Published data for this specific grade under immersion conditions is limited, so a 30-day compatibility dip test at 40 °C is specified before installation.
| Downstream process | Article tested | Electrical criterion | Relevant standard |
|---|---|---|---|
| Thermoformed ESD sheet | Trays, tote boxes | 10⁴–10⁷ Ω/sq surface resistivity | ASTM D257 / ANSI ESD S20.20 |
| Blow-moulded fuel system components | Filler necks, vapour return lines | ≤10⁶ Ω/sq surface resistivity | SAE J1645 |
| Injection-moulded ATEX containers | Powder hoppers, lids | ≤10⁶ Ω resistance to earth | IEC TS 60079-32-1 |
| Coextruded solvent vapour ducting | Conductive inner liner | ≤10⁶ Ω surface resistance | ISO 8039 / ASTM D257 |
Dry room containers for lithium-ion electrode foil and separator roll transport are injection moulded or thermoformed from CA6739. The room atmosphere is held below 1.5% RH and the surface resistance acceptance is ≤10⁷ Ω at 100 V DC after 24 h conditioning. The dominant field failure is condensation transfer when a cold bin exits the dry room into ambient air. A 12 h airlock dwell is specified before moving the bin into a dew point −40 °C chamber.
Solvent transfer pails and drum inserts are injection moulded from CA6739 at a melt temperature of 205–230 °C and a mould temperature of 20–40 °C. Pre-drying is not required if the original foil-lined bag is resealed and used within four hours at ambient humidity below 65% RH. Oil-based processing aids must not be added because they migrate to the surface and cause surface resistivity to drift above 10¹⁰ Ω/sq within 14 days.
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Designated by Cabot Corporation as Cabelec CA6739, the grade is a high-density polyethylene (HDPE) carrier compound in which a conductive carbon-black network is dispersed for permanent electrostatic-discharge control. The material is supplied as pelletized feedstock for direct melt conversion on injection molding and sheet extrusion lines; it is not positioned as a letdown masterbatch. Electrical classification is normally established by surface resistivity measurement according to IEC 62631-3-2 or ASTM D257-14, with volumetric resistance checked under IEC 60093. The polyethylene matrix imposes conditioning at 23 °C and 50 % RH in accordance with ISO 291 before electrical testing, because the conductive mechanism is electronic rather than moisture-dependent but thin insulating skins and laminate structures can show humidity-affected surface readings. The model suffix 6739 identifies a direct-molding conductive HDPE; this is a different product class from Cabot carbon-black masterbatches that require dilution into a virgin polymer.
Published product literature places CA6739 in the static-dissipative to conductive range. Because the carbon-black loading and the polymer molecular architecture are proprietary, single-lot certificates of analysis are required for release-critical dimensions. Tensile and flexural data are typically generated under ISO 527-2:2012 and ISO 178:2019, while melt mass-flow rate is reported under ISO 1133-1:2022 at 190 °C with a 5.0 kg piston load. Field experience on production-scale lines indicates that the melt viscosity is higher than that of an unfilled HDPE of equivalent flow class, and shot-to-shot resistivity variation can occur when the melt is held at barrel temperatures above 220 °C for longer than 10 min. Published data for this specific configuration is limited for long-term ultraviolet aging, and parts exposed to direct sunlight should be evaluated under ISO 4892-2 rather than assumed stable.
The conductive carbon-black phase influences both shear viscosity and pressure drop. Screw recovery should be set to maintain a consistent melt cushion, and the non-return valve should be of the free-flow type to avoid dead spots where conductive carbon black can accumulate and degrade. On injection molding machines with clamp force between 1000 kN and 2000 kN, the grade is normally processed with a gradual barrel profile from approximately 180 °C at the feed throat to 220 °C to 230 °C at the nozzle; the exact profile is lot-dependent because the carbon-black dispersion morphology affects melt compressibility. Mold temperatures from 20 °C to 60 °C are used, with the lower range favoring faster cycle times and the upper range reducing internal stress in thick sections.
A screw with an L/D ratio of 24:1 to 30:1 and a low-to-medium compression ratio is preferred because it provides dispersive mixing without excessive shear. Back pressure is often held at the low end of the HDPE range; hydraulic back-pressure settings above 0.7 MPa are not necessary and may contribute to electrical variability. Gate diameters should remain above 2.0 mm for multi-cavity tools to limit shear-induced temperature rise at the gate, because the carbon-black phase can orient during fast injection and create anisotropic resistance. Weld lines represent a discontinuity in the conductive network, so electrical qualification of multi-cavity tools or complex flow paths should be performed on the weakest weld line rather than on a flat plaque.
Moisture is not the primary volatile concern for HDPE, but carbon black can adsorb ambient moisture. When storage occurs at relative humidity above 60 %, pre-drying for 2 h at 80 °C in a desiccant dryer reduces surface splay and improves lot-to-lot electrical repeatability. Drying conditions more severe than 90 °C should be avoided because pellet surface oxidation can shift the surface resistivity and affect color uniformity.
Because the product is pre-compounded, in-house addition of natural HDPE or recycled HDPE should not be performed without a designed blend study. Even small additions can shift the conductive network below the percolation threshold and produce parts that pass visual inspection but fail surface resistance limits. If regrind is used, the regrind ratio should be controlled within a fixed band and logged for each batch. A change of 5 wt% in regrind content can alter the measured surface resistance by more than 1 order of magnitude in thin-walled sections.
For sheet extrusion, a single-screw extruder with a grooved feed section and L/D of 25:1 to 30:1 is frequently used; a restrictive screen pack is not recommended because it can shear the carbon-black network. The die gap and draw ratio interact with the conductive phase. A polished chrome die lip reduces carbon-black buildup, and a melt temperature at the upper end of the HDPE window improves melt homogeneity. If sheet is to be thermoformed, the surface resistance of the formed part should be measured after the draw, because thinning in corners can increase the resistance path and move the part from conductive to static-dissipative. Thermoforming trials should measure corner resistance with a two-pin probe and a defined electrode distance under IEC 62631-3-2.
Coextrusion with an insulating HDPE skin is sometimes used to preserve surface aesthetics, but a thick skin can create an insulating barrier that defeats the conductive function. If a cap layer is used, the total skin thickness must be lower than the percolation-dominated surface detection range; otherwise the part will appear insulative even when the core is conductive. Published data for this specific configuration is limited on coextruded structures, and a designed experiment is required to qualify each layer ratio.
The carbon-black loading in CA6739 is above the percolation threshold for the HDPE matrix, but final resistance depends on processing shear and cooling rate. Rapid cooling freezes the conductive network in a less ordered state, which can lower or raise resistance depending on orientation. Processors should not alter mold temperature or cycle time without repeating electrical qualification because the skin-core morphology in conductive HDPE is a critical variable. Resistance measurements on the surface cannot substitute for volume resistance when the part has a thick skin; both measurements are required for transferable approval.
Electrical performance of CA6739 is evaluated on the finished part, not on pellets, because the conductive network forms only after correct melt processing. The surface resistance is measured after conditioning at 23 °C and 50 % RH, and the result is expressed in Ω/sq. For packaging used in an electrostatic protected area, IEC 61340-5-1 defines conductive packaging as having a surface resistance below 1.0 × 104 Ω and static-dissipative packaging as between 1.0 × 104 Ω and 1.0 × 1011 Ω. CA6739 is intended to fall within the conductive or static-dissipative range, but exact classification depends on part thickness, ribs, weld lines, and surface roughness. The product should not be considered an electromagnetic shielding material merely because it is conductive; carbon-black-filled HDPE does not attenuate high-frequency fields sufficiently for a Faraday cage.
Surface resistivity testing is influenced by electrode geometry, contact pressure, and surface contamination. Silver-paint electrodes and conductive rubber electrodes can produce different readings on the same part. Test reports should state the electrode type and conditioning history; comparative data across suppliers should be normalized under IEC 62631-3-2 rather than compared using vendor-specific probe readings. Volume resistance measured on plaques under IEC 60093 is less sensitive to surface finish but is more sensitive to specimen thickness and internal void content.
Product-defining metrics for a conductive HDPE of this class are summarized below. The table is not a release specification; critical dimensions should be taken from the Cabot certificate of analysis for the specific lot.
| Property | Test method | Expected class or range | Conversion relevance |
|---|---|---|---|
| Density | ISO 1183-1 | 0.95 g/cm³ to 0.99 g/cm³ | Higher than natural HDPE due to carbon black |
| Melt mass-flow rate | ISO 1133-1:2022 at 190 °C / 5.0 kg | 1.0 g/10 min to 5.0 g/10 min | High-load measurement reflects filled-viscosity behavior |
| Tensile yield stress | ISO 527-2:2012 | 18 MPa to 26 MPa | Compared to unfilled HDPE at 23 °C |
| Flexural modulus | ISO 178:2019 | 800 MPa to 1200 MPa | Stackable containers and tray stiffness |
| Notched Izod impact | ISO 180/A | 5 kJ/m² to 15 kJ/m² | Lower than unfilled HDPE; test at 23 °C and low temperature |
| Surface resistance | IEC 62631-3-2 or ASTM D257-14 | 10^3 Ω/sq to 10^6 Ω/sq | Finished-part classification, not pellet acceptance |
| Volume resistance | IEC 60093 | 10^1 Ω·cm to 10^4 Ω·cm | Plaque measurement; thickness must be documented |
Where published data for this specific configuration is limited, the ranges above are derived from the general class of carbon-black conductive HDPE compounds and must be verified for the actual lot. They should not be used as design allowables without first-article data.
HDPE exhibits a comparatively high mold shrinkage. Addition of carbon black increases thermal conductivity slightly, which can reduce cycle-time variation but also influences crystallinity gradients. Multi-cavity injection tools should be instrumented with pressure sensors to confirm cavity-to-cavity fill balance, because conductivity is sensitive to packing pressure. Mold shrinkage in the flow direction is normally higher than in the transverse direction, and parts with large flat panels may require form tolerances verified under ISO 294-4 after 48 h of dimensional stabilization at 23 °C. For conductive tote boxes, warpage control is not solely cosmetic; out-of-flat panels can change the contact surface between stacked parts and alter the resistance path in a stack.
Weld-line conductivity is a critical field failure mode. In assembled totes, a conductive path must cross the weld line formed at the meeting of two melt fronts. The weld line is generally weaker and electrically more resistive than the bulk material. First-article validation should include surface resistivity measurements perpendicular to the weld line using IEC 62631-3-2, and the acceptance limit should be tighter than the bulk specification because post-molding flexural load can open microcracks along the weld and further increase resistance. If the part is loaded in repeated flexure, the test should be repeated after 1000 flexural cycles to check for fatigue-related resistance drift.
Secondary operations such as hot-plate welding, vibration welding, and ultrasonic welding can be used, but joint strength must be characterized before use. Carbon black increases the heat-transfer rate at the weld interface, so hot-plate welding temperatures should be adjusted downward relative to natural HDPE. Adhesive bonding requires surface treatment such as corona or plasma; flame treatment is possible but may ignite surface carbon black if the flame is oxidizing. Published data for this specific configuration is limited on ultrasonic welding, so initial welding trials should use amplitude and down-speed settings from the low end of the HDPE range.
Compared with carbon-filled polypropylene, the HDPE matrix provides a different low-temperature impact response and lower density. Polypropylene conductive grades often have higher heat deflection temperatures, whereas CA6739 remains within the HDPE continuous-use envelope. For refrigerated logistics or outdoor handling, impact testing at -20 °C under ISO 180/A is required to confirm that the grade meets the required energy absorption; published data for this specific configuration is limited below -10 °C.
Replacing metal machined components with conductive HDPE reduces part mass and eliminates corrosion pathways, but it does not provide electromagnetic interference shielding. If an enclosure must meet IEC 61000-4-2 or similar immunity criteria, a separate metal shield or conductive coating is required; carbon-black-filled polyethylene does not function as a Faraday cage at high frequencies. The material is also not intended for direct contact with strong oxidizing acids, aromatic solvents, or chlorinated hydrocarbons; chemical resistance testing under ASTM D543 is necessary for each fluid stream because the carbon-black phase can swell or degrade in aggressive environments.
Compared with external antistatic coatings or migratory additives, the carbon-black network in CA6739 is intended to provide conductivity that is not dependent on relative humidity and does not rub off onto packaged devices. However, the conductive surface can exhibit carbon-black sloughing under abrasion if not properly formulated, so dynamic component testing under simulated transit abrasion is required. The grade is normally opaque and black; colorability is limited because additional pigments may disrupt the conductive network and raise surface resistivity beyond the static-dissipative upper limit.
Compliance documentation for a conductive HDPE compound of this class is usually assembled from the following standards and regulations. Absent a product-specific declaration, none of these entries should be interpreted as an automatic approval for finished medical, food, or explosion-proof applications.
| Requirement category | Reference | Applicability to CA6739 |
|---|---|---|
| ESD packaging classification | IEC 61340-5-1 | Conductive or static-dissipative trays, boxes, and totes |
| Surface resistance | IEC 62631-3-2 / ASTM D257-14 | Finished-part acceptance, not pellet acceptance |
| Volume resistance | IEC 60093 | Plaque or disk; electrode geometry must be documented |
| Melt mass-flow rate | ISO 1133-1:2022 | Lot release at 190 °C / 5.0 kg |
| Tensile properties | ISO 527-2:2012 | Type 1A test specimen; 5 mm/min for modulus, 50 mm/min for yield |
| Impact resistance | ISO 180/A | Notched Izod at 23 °C and -20 °C |
| Chemical resistance | ASTM D543 | Fluid-specific; not a general chemical approval |
| Food-contact matrix | 21 CFR 177.1520 | HDPE matrix may comply; conductive carbon black requires separate clearance |
| Regulatory status | REACH 1907/2006, RoHS 2011/65/EU | Requires product-specific declaration from Cabot |
In service, the operational boundary is set by the HDPE matrix rather than by the conductive filler. Continuous exposure to strong oxidizing acids, aromatic hydrocarbons, or chlorinated solvents can stress-crack the part and change the surface resistance irreversibly. For applications involving intermittent contact with detergent solutions, environmental stress-crack resistance should be evaluated under ASTM D1693 before production. The compound is not recommended for continuous load-bearing service above 65 °C, and it is not a replacement for conductive engineering resins in hot underhood or autoclave environments.