| HS Code | 884047 |
| Va Content | 18% |
| Melt Index | 1.6 g/10 min (190°C/2.16kg) |
| Density | 0.940 g/cm3 |
| Melting Point | 88°C |
| Vicat Softening Point | 70°C |
| Tensile Strength | 21 MPa |
| Elongation At Break | 800% |
| Shore Hardness | 42 Shore D |
| Brittleness Temperature | -76°C |
| Halogen Content | Halogen-free (LSZH) |
| Lszh Grade | Yes |
| Wire Cable Grade | Yes |
As an accredited Ateva 1811 EVA Copolymer Resin,18% VA,1.6 MI,Wire & Cable Grade (LSZH) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Ateva 1811 EVA resin is supplied as pellets in 25 kg bags, palletized and stretch-wrapped, in the specified quantity. |
| Container Loading (20′ FCL) | A 20′ FCL of Ateva 1811 EVA resin, packed in 25kg bags on pallets, loaded safely for export. |
| Shipping | Ateva 1811 EVA resin ships as free-flowing pellets in moisture-resistant bags, palletized and stretch-wrapped for secure transport. Keep dry and avoid prolonged heat exposure to prevent clumping. Suitable for standard truck or container shipment; no hazardous classification required. Store in a cool, dry warehouse until processing. |
| Storage | Store Ateva 1811 EVA resin in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep original containers tightly sealed to prevent moisture pickup and contamination. Avoid generating dust; ground and bond containers when handling. Maintain moderate temperatures and low humidity to preserve properties and ensure optimal wire-and-cable processing performance. |
| Shelf Life | Shelf life is typically 2 years when stored in a cool, dry place, away from sunlight and moisture. |
Flame-retardant sheath compounds based on Ateva 1811 are formulated with the ethylene-vinyl acetate polymer fraction held at 30–36 wt% of the total halogen-free compound, of which 60–75 wt% is Ateva 1811 when co-blended with a 6–10 MI EVA grade for higher line-speed thin-wall extrusion. The filler package is dominated by surface-treated aluminium trihydrate at 130–160 phr per 100 phr resin, with magnesium dihydroxide at 20–30 phr to raise the onset of endothermic dehydration. Zinc borate at 5–8 phr and an amine-free hindered phenol/phosphite antioxidant system at 0.8–1.2 phr are used because the carbonyl-rich vinyl acetate fraction can generate acetic acid if the melt temperature exceeds 150°C during high-torque mixing. Compliance is tested under EN 50575:2014+A1:2016 Euroclass B2ca-s1,d0 with verification of smoke density by IEC 61034-2 and halogen acid gas by IEC 60754-2. In production, the compound is mixed on a co-rotating twin-screw extruder with 44:1 L/D, filler side-fed after 5–6 D to limit barrel wear and to keep the melt temperature at 135–145°C; the screw profile uses two high-shear kneading blocks before the vacuum port and one distributive mixing section after filler feeding. Screw speed is set at 280–360 rpm, and melt pump discharge pressure is capped at 80–90 bar to avoid local overheating at the strand die. Filler pre-drying at 80°C for 4 h is required when storage relative humidity exceeds 60% because surface moisture reduces coupling-agent efficiency and increases volatiles at the vacuum port. The finished compound is then jacketed onto twisted copper conductors using a 90-mm single-screw extruder with a compression ratio of 2.5:1 and a double-head die; terminal products are LSZH sheathing for commercial building power and control cables.
Thin-wall fibre-optic distribution cable jackets impose a different set of shear and wall-thickness constraints than building-wire sheathing. The compound uses Ateva 1811 at 100 phr as the primary resin; the melt index of 1.6 g/10 min measured under ISO 1133-1:2022 at 190°C/2.16 kg is low enough to prevent melt fracture at draw-down ratios above 20:1. The 18% vinyl acetate content improves filler wetting and permits aluminium trihydrate loadings of 110–140 phr without the surface bloom observed in lower-VA EVA grades. A secondary silicone-acrylate processing aid at 1.0–2.0 phr is included to suppress shark-skin at line speeds of 300–600 m/min. Compliance targets are IEC 60332-1-2 for single-cable flame propagation, IEC 61034-2 for smoke density, IEC 60754-1 for halogen acid content, and Telcordia GR-409-CORE for indoor/outdoor optical fibre cables. Compounding is carried out on a 40:1 L/D co-rotating twin-screw extruder with the first six barrel zones kept at 105–125°C because the lower wall thickness of the finished jacket is more sensitive to unmelts; filler is side-fed at 45% of the screw length, and the vent is run at −0.08 MPa to strip moisture from the ATH before the final melt seal. The extrudate is filtered through a 80/120/80 mesh screen pack and pelletised underwater at 20°C. The jacket is then applied in a 65-mm single-screw line with a 1.5:1 screw compression and a pressure-controlled die; terminal products include LSZH outer jackets for distribution and drop fibre cables.
Photovoltaic cable compounds built on Ateva 1811 are formulated for crosslinking during continuous vulcanization; the 18% vinyl acetate content accelerates free-radical abstraction at the secondary carbon, producing a tightly bound network with hot-set elongation below 175% and permanent set below 20% when tested under EN 60811-507. The formulation uses Ateva 1811 at 100 phr, surface-coated aluminium trihydrate at 120–150 phr, dicumyl peroxide at 1.8–2.2 phr, triallyl cyanurate at 0.5–1.0 phr, and an antioxidant package at 0.6–1.0 phr selected to avoid amine-based species that would decompose the peroxide before the CV line. Compliance is governed by EN 50618:2014 and IEC 62930:2017, with additional restriction of lead, cadmium, and hexavalent chromium under RoHS 2011/65/EU Annex II. The compounding step is performed below 115°C in a 36:1 L/D twin-screw extruder with a low-shear screw profile because dicumyl peroxide has a critical decomposition onset near 120°C and must not scorch before the vulcanization tube. Pelletised compound is then extruded onto tinned copper conductors at 110–130°C in a 70-mm single-screw machine with the head pressure held at 120–150 bar; the coated conductor passes into a pressurised steam CV tube at 1.2–1.6 MPa and 220–260°C for 3–6 min. Terminal products are single-core photovoltaic wire insulation and sheath layers rated for 1,500 V DC outdoor arrays.
| Application segment | Ateva 1811 loading | Flame retardant package | Critical extrusion limit | Required standard |
|---|---|---|---|---|
| Building power cable sheathing | 100 phr in polymer fraction; 30–36 wt% of compound | 130–160 phr ATH, 20–30 phr MDH | melt < 150°C; SME 0.25–0.30 kWh/kg | EN 50575, IEC 61034-2 |
| Fibre-optic drop/distribution jacket | 100 phr | 110–140 phr ATH, 1.0–2.0 phr silicone-acrylate | vent −0.08 MPa; line speed 300–600 m/min | IEC 60332-1-2, GR-409-CORE |
| Photovoltaic cable insulation/sheath | 100 phr | 120–150 phr ATH, DCP 1.8–2.2 phr | compounding < 115°C; steam CV 220–260°C | EN 50618, IEC 62930 |
| Industrial bedding/filler layer | 100 phr | 80–110 phr MDH | SME 0.22–0.26 kWh/kg | IEC 60811-501, IEC 61034-2 |
| EV charging cable sheath | 100 phr | 100–130 phr MDH, 5–8 phr zinc stannate | compound < 135°C; low-temperature impact −40°C | EN 50620, IEC 62893-1 |
Halogen-free bedding and filler compounds for multi-core industrial cables represent the low-filler end of the Ateva 1811 processing window; the resin is used at 100 phr with precipitated magnesium dihydroxide at 80–110 phr instead of aluminium trihydrate to allow the finished bedding layer to remain deformable around twisted cores. The vinyl acetate groups in Ateva 1811 provide sufficient polar interfacial contact with the hydroxide platelets to keep tensile strength above 9 MPa and elongation at break above 150% when tested under IEC 60811-501. Plasticiser-free compounding is maintained to preserve low smoke density under IEC 61034-2 and low acid gas conductivity under IEC 60754-2. The compound is produced on a 48:1 L/D co-rotating twin-screw extruder at 115–135°C but with a screw design that limits specific mechanical energy input to 0.22–0.26 kWh/kg, because excessive shear breaks the hydrocarbon backbone adjacent to the VA comonomer and reduces melt strength. Pellets are then applied in a 120-mm single-screw extruder with a pressure channel die; the die land is set at 12 mm and back pressure is controlled to 90–110 bar to avoid core collapse. The terminal product is a halogen-free bedding and filler layer in multicore industrial control and instrumentation cables.
Because long vehicle service life and frequent flexing limit the use of migratory plasticisers in EV charging cable sheathing, compounds based on Ateva 1811 exploit the 18% vinyl acetate content to achieve low-temperature impact resistance down to −40°C without external plasticiser. The compound uses Ateva 1811 at 100 phr, precipitated magnesium dihydroxide at 100–130 phr, zinc stannate at 5–8 phr, and a high-molecular-weight silicone processing additive at 2–3 phr. Compliance targets are EN 50620:2017 and IEC 62893-1, with halogen acid gas limited under IEC 60754-2 and smoke density measured under IEC 61034-2. The compounding operation is run on a 44:1 L/D co-rotating twin-screw extruder with the first zones at 110–120°C and the final zones below 135°C; filler is side-fed after 40% of the screw length to delay viscosity increase. The sheath is then applied on a 90-mm single-screw line with a double-layer head that co-extrudes a filled LSZH inner layer and a slightly harder outer layer from the same pellet feed but different back-pressure settings. The terminal product is the outer sheath of flexible electric vehicle charging cables used for Mode 2 and Mode 3 charging connections.
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Ateva 1811 ethylene-vinyl acetate copolymer resin is supplied as a pelletized low-smoke zero-halogen wire and cable feedstock with a specified vinyl acetate content of 18 wt% and a melt index of 1.6 g/10 min determined at 190 °C under a 2.16 kg load in accordance with ISO 1133-1 / ASTM D1238. Typical density is 0.940 g/cm³ by ISO 1183-1 / ASTM D1505. The grade is positioned for extrusion jacketing and insulation compounds in which the finished cable must satisfy halogen acid gas release, smoke density, and flame spread criteria under IEC 60754, IEC 61034, and IEC 60332. The combination of polar comonomer content and moderately low melt viscosity places the product between slower-flowing high-molecular-weight EVA grades and higher-index, thin-wall extrusion resins.
The acetate comonomer at 18 wt% reduces ethylene sequence length and overall crystallinity relative to low-density polyethylene. Differential scanning calorimetry by ISO 11357-3 / ASTM D3418 typically returns a peak melting endotherm near 86 °C. The reduction in crystallinity lowers flexural modulus and increases filler-loading capacity, which is critical for LSZH compounds containing aluminum trihydroxide or magnesium hydroxide at loadings from 150 phr to 180 phr. Polar acetate groups interact with the hydroxyl surfaces of metal hydrates, reducing gross particle agglomeration during mixing. The acetate group is thermally labile above approximately 210 °C and degrades by deacetylation above approximately 230 °C, releasing acetic acid. This boundary constrains both compounding and cable extrusion temperatures.
Low-smoke zero-halogen performance is a property of the finished compound rather than the base resin. In a representative formulation, Ateva 1811 is compounded with 150–180 phr of surface-treated aluminum trihydroxide and often 10–30 phr of magnesium hydroxide to broaden the endothermic decomposition range. Aluminum trihydroxide evolves water from approximately 180 °C to 230 °C; magnesium hydroxide decomposes from 300 °C to 340 °C. The released water dilutes combustible gases and cools the flame zone. Smoke obscuration is evaluated on the finished cable by IEC 61034-2:2019, while halogen acid gas content is assessed by IEC 60754-1:2011 and aqueous effluent pH and conductivity by IEC 60754-2:2019. Published oxygen index values for EVA/aluminum trihydroxide systems in ISO 4589-2 testing frequently fall between 30 and 38, though published data for Ateva 1811-specific configurations is limited.
Compared with ethylene homopolymer matrices, the 18 wt% vinyl acetate level improves mineral filler wetting without the pellet-blocking tack that can characterize EVA grades in the 25–28 wt% vinyl acetate range. This difference is relevant in sheet-fed compounding operations where higher-VA resins may require cooled pneumatic conveying and chilled pellet storage. Ateva 1811 retains sufficient polarity for metal hydrate dispersion while remaining a free-flowing pellet under normal warehousing conditions below 50 °C.
On single-screw extrusion lines with L/D ratios from 24:1 to 30:1, barrel temperatures are commonly profiled from 130 °C at the feed throat to 190 °C at the metering section, with a die temperature near 180 °C. The 1.6 g/10 min melt index is high enough to reduce head pressure in thin-wall cable jackets but low enough to retain melt strength for tube-on or pressure extrusion. In heavily filled compounds, melt temperature measured at the die should not exceed 210 °C, and the resin must remain below 230 °C to limit acetic acid formation. Pre-drying of fresh pellets is generally unnecessary, but material stored above 80 % relative humidity or exposed to cold-shock condensation should be dried at 60–70 °C for 2–4 h before compounding.
Compared with a 0.7 g/10 min EVA grade at the same 18 wt% vinyl acetate content, Ateva 1811 develops lower melt pressure and requires less torque at a given screw speed. This permits higher line speeds on crosshead cable lines but can reduce melt strength for very thick jackets, where sag may be controlled by drawing or by blending with 5–20 wt% of a lower-index EVA. Relative to higher-index grades in the 2.5–3.0 g/10 min range, Ateva 1811 retains a longer relaxation time, improving melt extensibility in crosshead tooling and reducing die-lip build-up. Relative to EVA grades containing 25–28 wt% vinyl acetate, the 18 wt% comonomer content provides lower tack and better pellet handling, while still imparting sufficient polarity for metal hydrate wetting.
In cable jacketing, the grade is used where the compounder requires a single resin that can accept high mineral loading while pumping through a 60 mm single-screw extruder at commercial output. Thin-wall data-cable jackets extruded at line speeds of 200–600 m/min generally favor the 1.6 g/10 min flow; thicker-wall power-cable sheathing may require blending with a 0.7 g/10 min EVA or high-density polyethylene to prevent draw-down and wall-thickness eccentricity. In comparison with linear low-density polyethylene, which can accept only limited aluminum trihydroxide before tensile elongation deteriorates, Ateva 1811 maintains elongational capacity at filler loadings above 150 phr. Ethylene-butyl acrylate copolymers of similar comonomer content may offer a higher thermal ceiling, but EVA generally provides higher tensile strength at equivalent filler loading and is more readily available in LSZH compound supply chains.
| Property | Test method | Value |
|---|---|---|
| Melt index | ISO 1133-1 / ASTM D1238 | 1.6 g/10 min |
| Vinyl acetate content | Supplier FTIR calibration | 18 wt% |
| Density | ISO 1183-1 / ASTM D1505 | 0.940 g/cm³ |
| Peak melting temperature | ISO 11357-3 / ASTM D3418 | 86 °C |
| Vicat softening temperature | ISO 306 / ASTM D1525 | 75 °C |
Deacetylation of the acetate group is the limiting kinetic event. At melt temperatures above 230 °C, the rate of acetic acid elimination becomes consequential, leading to corrosive condensate on the downstream calibrator, die lip, and vacuum pump. Extruder screws and barrels should be constructed from nitrided or bimetallic surfaces for extended campaigns. The recommended melt temperature window for Ateva 1811 in mineral-filled LSZH formulations is 150–210 °C. At the lower end, unmelted pellets create dispersion defects; at the upper end, yellowing and odor increase. The processing window is therefore suitable for conventional single-screw cable jackets but not for high-temperature engineering resin conditions.
In twin-screw compounding with a co-rotating 40:1 L/D extruder, aluminum trihydroxide is typically side-fed after polymer melting to avoid excessive abrasion on the first kneading blocks. Specific energy input rises as filler loading increases from 120 phr to 180 phr; screw speed is often trimmed to keep compound melt temperature below 200 °C. Surface-treated aluminum trihydroxide with a median particle size of 1–2 µm is preferred for tensile-elongation retention. The filler-polymer interface dominates low-temperature elongation. When tensile elongation at break drops below 150 % on finished insulation, dispersion quality or additive selection is typically the cause rather than the base resin.
Batch-to-batch variance of the base resin is monitored by melt index and vinyl acetate content. Variations in melt index outside ±0.3 g/10 min can alter head pressure and cable concentricity. Variations in vinyl acetate content outside ±1 wt% may shift filler wetting and low-temperature brittleness. These limits reflect typical cable compounder incoming inspection criteria and should be confirmed against the supplier certificate of analysis.
Low-temperature flexibility is assessed by IEC 60811-506 cold bend and cold elongation tests on finished cables. Because Ateva 1811 has a peak melting temperature near 86 °C and a Vicat softening point near 75 °C, it retains flexibility in heavily filled compounds at low temperatures when the compound is not under stress. For applications requiring formal cold bend certification at −40 °C, compounders often blend EVA with polyolefin elastomers to pass cold wind and bending tests. The base resin itself is not usually the limiting factor; mineral filler loading above 150 phr can increase low-temperature modulus and should be assessed by ISO 527-2 / ASTM D638 at the specified service temperature.
LSZH qualification cannot be certified on Ateva 1811 alone. The resin contains no halogenated comonomer and is supplied without halogenated flame retardants, but halogen exclusion depends on the total formulation and any recycled material. Compliance with IEC 60754-1:2011 and IEC 60754-2:2019 is evaluated on the extruded cable compound. Smoke density is assessed by IEC 61034-2:2019 on a 3 m cube; flame spread is evaluated by IEC 60332-1-2:2015 for single cables. Supplier documentation for Ateva 1811 typically includes a RoHS statement confirming that lead, mercury, cadmium, hexavalent chromium, polybrominated biphenyls, and polybrominated diphenyl ethers are not intentionally added. REACH review of the safety data sheet remains necessary because the polymer may contain process residues.
| Framework | Relevant test or declaration | Typical audit status |
|---|---|---|
| RoHS Directive 2011/65/EU | Pb, Hg, Cd, Cr(VI), PBB, PBDE | Not intentionally added |
| REACH 1907/2006 | Candidate list SVHC | Supplier SDS review required |
| IEC 60754-1:2011 | Halogen acid gas release | Finished-compound test |
| IEC 60754-2:2019 | pH and conductivity | Finished-compound test |
| IEC 61034-2:2019 | Smoke density | Finished-cable test |
| ISO 1133-1:2022 | Melt flow rate | 1.6 g/10 min |
For shipboard and rail cable jackets, processors typically pre-dry filled compounds, not the neat resin, at 70–80 °C for 4 h to remove surface moisture from aluminum trihydroxide. The resin should be kept away from direct sunlight and stored below 50 °C to prevent pellet blocking. When the product is used in foamed insulation or as a coupling-layer tie resin, higher-VA grades are often preferred for adhesion; Ateva 1811 is therefore specified for the jacket rather than the conductor adhesion layer. In thick-wall low-voltage power cable, a blend of 70–80 wt% Ateva 1811 with 20–30 wt% lower-index EVA or high-density polyethylene is used to control melt sag. The material is not designed for continuous exposure to hot mineral oil or to concentrated oxidizing acids.