| HS Code | 716933 |
| Density | 1.10 g/cm³ |
| Melt Flow Rate | 4.0 g/10min |
| Tensile Strength | ≥12.0 MPa |
| Elongation At Break | ≥200% |
| Volume Resistivity | ≤100 Ω·cm |
| Thermal Aging | 135°C × 168h |
| Crosslinking Degree | ≥75% |
| Oxygen Index | ≥30% |
| Appearance | Black granules |
| Packaging | 25 kg/bag |
| Volatile Content | ≤0.5% |
| Moisture Content | ≤0.1% |
As an accredited Wanma Macromolecule XLPE WM-ZRBDPE factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg moisture-proof bags, Wanma Macromolecule XLPE WM-ZRBDPE is supplied in palletized quantities for industrial use. |
| Container Loading (20′ FCL) | 20′ FCL loading: Wanma Macromolecule XLPE WM-ZRBDPE packed in bags on pallets; container kept dry, clean, ventilated, and moisture-protected. |
| Shipping | Wanma Macromolecule XLPE WM-ZRBDPE is shipped in sealed, moisture-proof bags or drums on pallets, clearly labeled per SDS/GHS requirements. Transport in clean, dry vehicles away from heat, ignition, moisture, and contamination. Store ventilated, shaded, and dry; handle according to supplier SDS and local regulations. |
| Storage | Store in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, sparks, and flames. Keep original packaging sealed and off the floor to prevent moisture and contamination. Avoid prolonged stacking or heavy loads; follow manufacturer stacking limits. Maintain good housekeeping, use FIFO, segregate from incompatible chemicals, and check containers regularly for damage. Comply with local regulations and SDS. |
| Shelf Life | Wanma Macromolecule XLPE WM-ZRBDPE has a shelf life of about 12 months when stored dry, cool, and protected from sunlight and moisture. |
Wanma Macromolecule XLPE WM-ZRBDPE is specified in downstream processing environments where silane-grafted polyethylene reacts with moisture to form a three-dimensional Si–O–Si network. The application entries below define the compliance boundary, the compounding or extrusion addition window, the production equipment stage at which crosslinking is initiated, and the final article class. Where data are drawn from public standards rather than from proprietary grade testing, the test designation is cited without implying a certificate of conformity.
For 0.6/1 kV low-voltage distribution cable insulation, WM-ZRBDPE enters the process as a moisture-crosslinkable compound that must remain below a melt-temperature ceiling during extrusion because silane-grafted polyethylene can undergo premature silanol condensation at the die lip. On production lines using a 65 mm to 90 mm single-screw extruder with an L/D 30:1 barrier screw, the barrel profile is maintained between 135 °C and 170 °C, while head pressure is recorded continuously; a pressure rise greater than 10% over a 30 min run at constant screw speed indicates viscosity build-up from crosslinking and requires a purge with non-grafted PE. The insulation layer must be pre-dried at 70–80 °C for 2–4 h when storage relative humidity exceeds 60%; moisture entering the hopper contaminates the silane-grafted melt and produces pinholes at the die exit.
The addition window for the insulation layer is governed by the desired hot-set elongation after curing. In a two-step Sioplas masterbatch formulation, 100 phr silane-grafted base resin is combined with 3–5 phr catalyst masterbatch, 0.2–0.5 phr hindered phenolic antioxidant, and 1–3 phr colour masterbatch; the base resin density is 0.928–0.940 g/cm³ and melt flow rate is 0.6–1.5 g/10 min at 190 °C under 2.16 kg load. Amine-based additives are not introduced because they can shift silanol condensation kinetics during storage and create batch-cure inconsistency. Moisture cure follows in a steam bath at 85–95 °C for 6–24 h, and gel content is verified at not less than 70% by ASTM D2765-16 or IEC 60811-507.
Material compliance is defined by IEC 60502-1:2021 for low-voltage extruded insulation cables; insulation mechanical properties are evaluated under IEC 60811-501, thermal ageing under IEC 60811-401, and long-term pressure behaviour at a conductor temperature of 90 °C. The final articles are low-voltage distribution and industrial feeder cables in building and plant installations where the XLPE insulation temperature does not exceed 90 °C.
The accelerated ageing protocol for EN 50618:2014 and IEC 62930:2017 forces the halogen-free sheath compound to retain tensile properties after 20,000 h at 120 °C, while the same cable must pass IEC 60332-1-2 within 60 s flame application and deliver smoke density below the limits of IEC 61034-2. This dual requirement constrains flame-retardant loading: treated magnesium hydroxide is incorporated at 50–65 phr, zinc borate at 3–8 phr, antioxidant masterbatch at 0.4–1.0 phr, UV stabiliser at 0.2–0.5 phr, and catalyst masterbatch at 5 phr equivalent to 0.02–0.05 phr dibutyltin dilaurate. Above 65 phr metal hydrate addition, tensile strength falls below the 10 MPa sheathing threshold commonly applied, and elongation-at-break becomes sensitive to dispersion defects.
The extrusion stage uses a low-shear screw with compression ratio 1.8:1 and temperature zones from 130 °C to 165 °C to avoid dehydroxylation of the hydrate filler before the die. Melt filtration through 60/80/60 mesh screens controls agglomerates. The cable is moisture-cured at 80–95 °C and 85–95% relative humidity for up to 24 h; thicker sheaths above 1.5 mm require staged cure to prevent a crosslinked skin that slows water diffusion. The final article class is H1Z2Z2-K photovoltaic cable, from 1.5 mm² to 16 mm² conductor cross-section, used on rooftop and utility-scale DC strings.
For direct-current rooftop strings, short-circuit current and ambient heat raise conductor temperature, so the compound is also tested for long-term heat resistance using IEC 60216-1, and for cold impact at -40 °C under IEC 60811-506. The sheath must survive mechanical abuse without cracking, which places a minimum elongation-at-break after ageing of 50% on the jacket. Production runs on vertical sheathing lines show that batch-to-batch melt-flow variation outside ±5% is associated with wall-thickness drift at line speeds near 200 m/min, and dimensional control requires a sheath wall tolerance of ±0.05 mm. Material-level conformity is assessed under RoHS Directive 2011/65/EU and REACH Regulation (EC) No 1907/2006.
A production-scale extrusion line running thin-wall automotive insulation at >600 m/min exposes the compound to less than 15 s residence time in the barrel, but the combination of high shear and moisture ingress can still trigger localized crosslinking if the melt exceeds 180 °C. The process therefore uses a 45 mm single-screw extruder with L/D 30:1, a barrier screw with tip/die ratio 1.6:1, and a crosshead die sized for an insulation wall thickness of 0.20–0.50 mm. Draw-down ratio is maintained between 2.5:1 and 3.5:1; excessive draw ratio causes eccentricity beyond the limits of ISO 6722-1:2011.
For Class C and D automotive conductor insulation, the compound is modified with 20–35 phr treated magnesium hydroxide, 0.3–0.6 phr hindered amine stabiliser, and 0.1–0.3 phr copper inhibitor; the silane-grafted base resin remains the main phase with 5 phr catalyst masterbatch. Curing is completed at 85 °C and 85–95% RH for 8–16 h, after which hot-set elongation under 0.2 MPa load is evaluated. The terminal parts are thin-wall single-core automotive wires and 0.35 mm wall battery-management-system leads rated for 600 V under LV 112-1 and ISO 6722-1.
PEX-b pipe conforming to ISO 15875-2 and DIN 16892 is extruded on a 45–60 mm single-screw line at 150–190 °C with a 95/5 parts-by-weight ratio of silane-grafted HDPE to catalyst masterbatch; moisture cure in 85 °C water for 10–24 h produces hot- and cold-water plumbing pipe and floor-heating circuits. Hydrostatic pressure testing at 95 °C under 4.4 MPa is applied to the final dimension series, and published data for this specific grade in municipal heat distribution pipe is limited.
The compliance chain for public-area jacketing begins with EN 50575:2014, IEC 60502-1, and IEC 60332-3-24, where a 3.5 m vertical ladder test demands that flame spread not exceed 2.5 m after 20 min of burner exposure. To meet this while retaining tensile strength above 10 MPa, the compound is formulated with a polyolefin base of 100 phr, ATH or MDH at 60–80 phr, zinc borate at 3–8 phr, and a silane coupling agent at 0.3–0.8 phr; filler particle size is controlled below 5 µm median diameter to reduce moisture uptake and die-lip build-up.
| Assessment | Standard designation | Acceptance boundary |
|---|---|---|
| Vertical bundle flame spread | IEC 60332-3-24 | char height ≤ 2.5 m after 20 min |
| Smoke density | IEC 61034-2 | light transmittance ≥ 60% |
| Acid gas evolution | IEC 60754-2 | pH ≥ 4.3, conductivity ≤ 10 µS/mm |
Compounding is performed on a co-rotating twin-screw extruder with L/D 44:1 and barrel temperatures of 140–170 °C, using side feeding for the hydrate filler after the polymer melting zone. Vacuum venting at -0.08 MPa is applied to remove moisture released by ATH; if the melt temperature before the die exceeds 170 °C, micro-voids reduce smoke-density performance under IEC 61034-2. Sheathing extrusion follows on a single-screw line at 130–160 °C with a tube-on pressure die. The moisture-cured jacket is tested for smoke density under IEC 61034-2 and acidity under IEC 60754-2; final articles are low-smoke zero-halogen sheathed power cables for airports, hospitals, and rail tunnels where escape-route visibility is regulated.
Where appliance internal wire must pass a 60 s flame test under IEC 60332-1-2 or the VW-1 vertical flame procedure under UL 758 AWM, WM-ZRBDPE is extruded without further filler modification as ready-to-use pellets; when multiple regrind passes are anticipated, an additional 0.4–0.8 wt% antioxidant masterbatch is used. Extrusion through a crosshead die at 140–170 °C and moisture cure at 80–90 °C produce 0.5–2.5 mm² crosslinked internal wires for household appliances and power tools.
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