| HS Code | 853209 |
| Product | Ateva 4030ACX EVA Copolymer Resin |
| Resin Type | Ethylene Vinyl Acetate (EVA) Copolymer |
| Vinyl Acetate Content | 40% |
| Melt Index | 55 g/10 min (190°C/2.16 kg) |
| Density | 0.970 g/cm³ |
| Melting Point | 65°C |
| Vicat Softening Point | 45°C |
| Brittleness Temperature | -60°C |
| Tensile Strength At Break | 8.0 MPa |
| Elongation At Break | 900% |
| Hardness | 70 Shore A |
| Low Gel Characteristics | Yes (low gel) |
| Grade | Insulation Shield |
As an accredited Ateva 4030ACX EVA Copolymer Resin,40% VA,55 MI,Low Gel,Insulation Shield Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Ateva 4030ACX EVA copolymer resin is supplied as pellets in 25 kg multi-wall paper bags, with quantities available per pallet. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Ateva 4030ACX EVA resin, 40% VA, 55 MI, low gel, insulation shield grade. |
| Shipping | Ateva 4030ACX is supplied as EVA copolymer pellets, typically packed in 25 kg moisture-resistant bags or 500 kg jumbo bags on pallets. Ship as non-hazardous, dry cargo in clean containers. Protect from rain, humidity, and direct sunlight; store below 50°C and keep sealed to prevent moisture absorption. |
| Storage | Store Ateva 4030ACX in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep the original sealed packaging intact to prevent moisture pickup and contamination. Avoid stacking excessively. Maintain temperatures below 40°C. Use within one year of receipt for optimal melt flow and gel-free performance. |
| Shelf Life | Shelf life is typically one year from shipment when stored unopened in a cool, dry environment. |
In medium-voltage power cable construction rated 6 kV to 35 kV under IEC 60502-2:2014, the outer semiconductive insulation shield is co-extruded over XLPE dielectric and must simultaneously prevent air void formation at the shield-dielectric interface during load cycling and allow clean, residue-free peel at termination. Ateva 4030ACX is selected as the base polymer for this layer because the 40% vinyl acetate comonomer content increases polarity sufficiently to wet conductive carbon black at loadings of 35–55 phr, while the melt mass-flow rate of 55 g/10 min determined at 190°C/2.16 kg by ISO 1133-1:2022 supports thin-gauge extrusion without excessive head pressure. The designation “low gel” refers to a reduced count of unmelted gel particles per unit area, not to a low crosslinked gel fraction after vulcanization; this is critical at insulation shield thicknesses of 0.8 mm to 1.2 mm, where a single protrusion can concentrate the electrical field and lower partial-discharge inception voltage. This grade is not used as the XLPE dielectric itself; moisture uptake and dielectric loss associated with 40% vinyl acetate exceed the limits for primary insulation in IEC 60502-2:2014.
Compliance for this application is evaluated against IEC 60502-2:2014, HD 620 S2:2020, and ICEA S-93-639/NEMA WC 74:2016. Non-metallic screen volume resistivity is determined by ASTM D257-14 and is typically held at or below 500 Ω·m at 90°C after cure; tensile elongation is tested per ASTM D638-14, and melt flowability is retested per ASTM D1238-20. Peel force is not defined as a single IEC requirement; utility specifications commonly derive peel force from 25 mm wide strips pulled at 180°, and published data for this specific configuration is limited, so strippability windows must be established on the target cable construction and conductor size. Moisture content above 0.05% warrants pre-drying at 60–70°C for 2–4 h before compounding.
A typical strippable shield formulation uses Ateva 4030ACX at 100 phr, corresponding to approximately 58–66 wt% of the finished compound. The remaining components and their dosage ranges are listed below.
| Component | Loading | Function / Processing Limit |
|---|---|---|
| Ateva 4030ACX | 100 phr | Base resin, 58–66 wt% of total compound |
| Conductive carbon black | 35–55 phr | Volume resistivity control; dispersion limited by carbon black aggregate size |
| Antioxidant | 1.5–2.5 phr | Heat aging resistance; excess increases surface bloom |
| Processing aid | 2–4 phr | Melt pressure reduction; excessive loading reduces tensile strength |
| Dicumyl peroxide | 1.0–2.0 phr | Thermal crosslinking; added in second mixing pass at 100–115°C |
Production-scale compounding is performed in a 160 L Banbury internal mixer or a co-rotating twin-screw extruder with 40:1 L/D, using side feed for carbon black. A two-pass mixing sequence is common: the first pass at 110–130°C disperses carbon black and antioxidant; the second pass at 100–115°C incorporates dicumyl peroxide and minimizes scorch. For this application, amine-based additives are avoided because they can interfere with dicumyl peroxide decomposition. Melt is filtered through 140–150 mesh screens before pelletizing to remove carbon black agglomerates and residual gel particles. The cable layer is applied on a triple-layer crosshead in a catenary continuous vulcanizing line; the shield extruder is typically a 60–75 mm single-screw machine with 24:1 L/D, barrier screw, and a melt pump. Melt temperature at the die is held between 115°C and 125°C; premixing lines and screw elements are cooled to avoid premature vulcanization. Cure proceeds at 180–250°C under 10–20 bar nitrogen or steam pressure. After cooling, stress-relief annealing is applied before rewinding to prevent layer shrinkage. Terminal finished product types include 6/10 kV, 12/20 kV, and 18/30 kV XLPE-insulated power cables used in wind farm feeders, underground residential distribution, and industrial medium-voltage feeders.
Low-smoke building and transit cables that must pass IEC 60332-1-2:2015 vertical flame testing place a different set of demands on Ateva 4030ACX than semiconductive shield layers: here the 40% vinyl acetate content is exploited for filler wetting and char formation rather than carbon black conductivity. The resin permits filler loadings of 120–180 phr alumina trihydrate and 0–50 phr magnesium dihydrate without the surface melt fracture seen in low-VA ethylene copolymers. The 55 g/10 min melt flow rate under ISO 1133-1:2022 maintains extrusion output on 60–90 mm sheathing extruders despite high filler volume fractions. Low gel count reduces pinhole formation in thin-wall sheaths down to 0.6 mm nominal thickness.
Compliance for this application is checked against IEC 60754-1:2011 and IEC 60754-2:2019 for halogen acid evolution, IEC 61034-2:2005 for smoke density, IEC 60332-1-2:2015 for vertical flame propagation, and EN 50363-7:2005 for halogen-free flame-retardant sheathing compounds. Regulatory status for EU shipments is documented under REACH (EC) No 1907/2006 and RoHS Directive 2011/65/EU. Hot set elongation after peroxide or silane crosslinking is evaluated per IEC 60811-507:2012; tensile and elongation before aging are determined by IEC 60811-501:2012. The formulation addition ratio starts with Ateva 4030ACX at 100 phr, with ATH at 120–180 phr, optional MDH at 0–50 phr, a vinyl silane or maleic anhydride compatibilizer at 1–2 phr, a hindered phenolic antioxidant at 0.5–1.5 phr, and a processing aid at 2–4 phr. On a total weight basis, the resin content is approximately 26–33 wt%.
Compounding is run on a co-rotating twin-screw extruder with 48:1 L/D and multiple side feeders to prevent filler bed compression. Melt temperature is controlled between 100°C and 140°C; the upper limit is set below the dehydration onset of ATH at approximately 180°C. Vacuum devolatilization is used to keep moisture below 0.05%, and the melt is filtered through 100–120 mesh screens. Cable sheathing is extruded on a 60–90 mm single-screw extruder with 25:1 L/D and a temperature profile of 120–150°C; a melt pump and profile gauge reduce wall-thickness variation. Batch-to-batch variation in filler particle size distribution can shift melt viscosity by 10–15%, so torque rheometer data are used to adjust shear rate and temperature profile before start-up. Terminal finished product types include building riser cables, mass transit rolling-stock cables, data center power distribution cables, and shipboard low-smoke cables.
Radiation-crosslinked heat-shrinkable sleeving for cable joints and terminations uses Ateva 4030ACX as a high-VA base because the polar comonomer broadens the radiation dose window and improves dimensional recovery after expansion. In production, gel fraction is a more reliable control variable than beam current. A formulation containing Ateva 4030ACX at 100 phr, conductive carbon black at 30–50 phr, a flame-retardant package at 60–100 phr, an antioxidant at 1.5–2.5 phr, a radiation sensitizer at 1–3 phr, and a processing aid at 2–4 phr produces a resin content of 38–50 wt% and a radiation response that reaches 50–65% gel fraction after 15–25 Mrad electron beam exposure. Gel fraction is measured by ASTM D2765-16.
Product specifications reference ASTM D2671-21 for heat-shrinkable tubing, IEC 60684-3:2019 for flexible insulating sleeving, and UL 224:2021 for extruded insulated tubing. Low-temperature flexibility is verified through ASTM D2671-21 test methods; hot set after crosslinking is evaluated per IEC 60811-507:2012. Production begins with twin-screw compounding at 110–140°C to disperse carbon black without degrading the vinyl acetate comonomer. The compound is extruded into tubing on a 30–60 mm single-screw extruder with a vacuum calibration sleeve; melt temperature is held at 120–140°C. The extruded tube is irradiated in an electron beam unit to an absorbed dose of 15–25 Mrad, targeting 50–65% gel fraction. After irradiation, the tubing is heated to 150–180°C in hot air or liquid medium, expanded onto a mandrel or by internal air pressure, and quenched to lock in the expanded shape. Because 40% vinyl acetate reduces crystalline melting point, storage of expanded tubing above 50°C may initiate premature recovery. Terminal finished product types include heat-shrinkable cable joint outer sleeves, termination kits, busbar insulation sleeves, and breakouts for medium-voltage accessories.
Where a cable compounder supplies multiple triple-layer lines, Ateva 4030ACX is also employed as the carrier resin in conductive carbon black masterbatch because the 55 g/10 min melt flow rate and 40% vinyl acetate permit carbon black loadings of 35–45 wt% with fewer carrier dilution problems than LDPE. The masterbatch route is preferred when site dust control and dispersion repeatability are more critical than direct compounding. Masterbatch quality is checked by melt flow rate per ISO 1133-1:2022, volume resistivity of compression-molded plaques per ASTM D257-14, and density per ASTM D792-20. If the masterbatch is intended for EU cable grades, documentation covers REACH (EC) No 1907/2006 and RoHS Directive 2011/65/EU.
Carrier resin content is set at 45–60 wt%; carbon black at 35–45 wt%; process aids at 2–5 wt%; antioxidant at 0.5–1.5 wt%. Typical let-down ratio into a finished semiconductive shield compound is 1:4 to 1:6 by weight, depending on the target final carbon black level of 35–45 phr. Published data for the exact let-down ratio in a specific compounder setting is limited; the stated range reflects typical equipment capability. Masterbatch is produced on a co-rotating twin-screw extruder with 40:1 L/D, side-fed carbon black, and a screw profile using high-shear kneading blocks followed by low-shear distributive elements. Melt temperature is maintained at 130–160°C; underwater pelletizing is followed by classifier and moisture control to below 0.05%. The pellets are metered into the cable compounder at the let-down ratio stated above; no additional pre-drying is required if sealed packaging is used and storage relative humidity remains below 60%. Terminal outputs are conductive black masterbatches used in insulation shield and conductor shield compounds for medium-voltage power cable, and in semi-conductive jackets for underground cable accessories.
On triple-layer extrusion lines, the inner semiconductive conductor shield is applied over stranded copper or aluminum conductors at nominal thicknesses of 0.5–0.8 mm before the XLPE insulation layer. Ateva 4030ACX provides the melt flow required to penetrate the outer strands and fill interstices without forming voids at the conductor-shield interface. The 55 g/10 min melt flow rate under ISO 1133-1:2022 allows extrusion at low melt pressure, but the same flow can reduce melt viscosity to the point where die drool increases; the extruder must therefore be configured with a melt pump and a screen pack of 100–150 mesh to stabilize output.
Conductor shield compounds are validated under IEC 60502-2:2014 and HD 620 S2:2020; volume resistivity is measured by ASTM D257-14 and is typically required to remain below 500 Ω·m at 90°C. Pre-cure scorch time is assessed by a moving-die rheometer at 125°C to confirm safe residence time before the die. The formulation addition ratio uses Ateva 4030ACX at 100 phr, conductive carbon black at 40–60 phr, antioxidant at 0.8–1.5 phr, processing aid at 1–3 phr, and dicumyl peroxide at 0.8–1.8 phr. Resin content is approximately 52–60 wt% of the final compound.
The conductor is preheated to 90–110°C before entering the triple-layer crosshead; shield melt temperature is controlled at 115–125°C, while the XLPE insulation extruder runs higher. The crosshead is designed to maintain draw ratio between 1.2:1 and 1.6:1 to prevent layer necking. The line is purged with nitrogen at start-up; any resin stagnation above 130°C can initiate premature peroxide crosslinking and generate gel particles in the screen pack. After crosslinking and cooling, the cable is tested for partial discharge, layer thickness, and conductor adhesion. Terminal finished product types include 1 kV to 35 kV XLPE-insulated power cables for overhead line conversion, industrial plant feeders, and wind turbine tower and nacelle cabling.
Competitive Ateva 4030ACX EVA Copolymer Resin,40% VA,55 MI,Low Gel,Insulation Shield Grade prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8615380400285 or mail to sales2@liwei-chem.com.
We will respond to you as soon as possible.
Tel: +8615380400285
Email: sales2@liwei-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Ateva 4030ACX is an ethylene-vinyl acetate copolymer resin supplied for medium-voltage cable insulation shield compounds. The nominal vinyl acetate content is 40 wt% and the melt flow rate is 55 g/10 min at 190 °C under a 2.16 kg load when determined according to ISO 1133-1:2022 or ASTM D1238-23. The low-gel designation distinguishes this grade from standard EVA copolymers used in film, adhesive, or hot-melt applications: gel populations in the resin are controlled for thin-wall cable shield extrusion, where a single gel domain can become a stress concentration and a partial discharge initiation site. The intended use is as a carrier resin in peroxide-cured or thermoplastic semiconductive insulation shield compounds used in medium-voltage XLPE-insulated cables rated between 5 kV and 35 kV under IEC 60502-2:2014 or ICEA S-94-649.
The 40 wt% vinyl acetate content corresponds to approximately 18 mol% acetate comonomer in the ethylene backbone, which strongly suppresses polyethylene crystallinity. In differential scanning calorimetry performed according to ISO 11357-3:2018, EVA copolymers of this composition typically exhibit a broad melting endotherm with a peak below 80 °C and a glass transition below −30 °C; the exact values for Ateva 4030ACX are lot-dependent and are not published as single-point specifications. The shorter crystalline ethylene sequences reduce room-temperature stiffness and increase segmental mobility relative to 18–28 wt% VA grades. For semiconductive shield compounding, this morphology improves carbon black wetting. Conductive furnace blacks with nitrogen surface areas between 60 m²/g and 1000 m²/g are dispersed with lower mixing torque than in lower-VA EVA grades, and the polar acetate groups contribute to filler–polymer interaction. The compounded shield layer is formulated to achieve volume resistivity in the range of 10^0–10^2 Ω·cm at 23 °C when measured by ASTM D4496-21, with higher values permitted at operating temperature only if the cable design controls stress distribution.
The higher polarity of the 40 wt% VA grade also influences interfacial adhesion to peroxide-cured XLPE insulation. During continuous vulcanization, the semiconductive shield layer is co-extruded directly onto the insulation, and polar acetate groups provide greater interfacial compatibility than a 28 wt% VA grade. Published single-point peel adhesion data for this specific resin configuration are limited; cable material suppliers generally qualify adhesion by internal cable-specific peel procedures after hot-set cure, because adhesion depends on peroxide type, cure temperature, cooling rate, and carbon black loading.
Low gel content is not an absolute property but a lot-to-lot cleanliness specification relevant to extrusion of shield layers as thin as 0.4 mm to 1.5 mm on continuous vulcanization lines. Gel origins in EVA include crosslinked polymer formed in high-temperature finishing zones, oxidized material accumulated on reactor walls, and contaminant particles introduced during pelletizing. In cable shielding, a gel domain can create a localized thickness irregularity or a protruding defect. The resulting electric field enhancement at the insulation–shield interface is evaluated by partial discharge testing; cable manufacturers commonly reject defects that produce partial discharges above 5 pC to 10 pC at the specified test voltage. The low-gel designation therefore reduces the frequency of such defect-related failure modes, but it does not eliminate the need for melt filtration on the compounding or cable line.
Resin producers typically assess gel level by extruding a thin film on a laboratory single-screw extruder and counting gel domains above a defined size threshold. The exact procedure for Ateva 4030ACX is an internal supplier method; no single ASTM or ISO standard governs cable-grade EVA gel counts. For downstream compounding, screen packs of 80/120/325 mesh are commonly installed before the crosshead to remove agglomerates and incidental contaminants. The resin’s low melt viscosity at 55 g/10 min reduces pressure drop across fine screen packs, allowing tighter filtration without excessive melt temperature rise.
| Parameter | Value or designation | Test method |
|---|---|---|
| Vinyl acetate content | 40 wt% | FTIR per ASTM D5594-18 or equivalent |
| Melt flow rate | 55 g/10 min | ISO 1133-1:2022, 190 °C, 2.16 kg |
| Gel level | Low gel, insulation shield grade | Internal optical gel count; no single ASTM method governs cable-grade EVA gels |
| Food-contact status | Not supplied as food-contact grade | FDA 21 CFR 177.1350 not implied |
Selection of 55 g/10 min melt flow rate instead of a 25 g/10 min grade changes extrusion pressure, melt strength, and filler dispersion in compounding. In a co-rotating twin-screw extruder with 40:1 L/D and downstream carbon black side feeding at 30–40 wt%, the low melt viscosity of the 4030ACX matrix reduces specific energy input and permits lower melt temperatures, typically maintaining a compound melt temperature below 180 °C under normal screw speeds. The trade-off appears in tube-on support during triple-layer co-extrusion: lower melt strength can cause sag in a molten semiconductive melt curtain unless vacuum sizing or pressure tooling is used. Therefore, 4030ACX is specified where high filler loading and high line speed are prioritized over unsupported tubular drawdown. By contrast, a 25 MI 33 wt% VA grade may provide better melt integrity for thick or unsupported shield layers but requires higher torque and may raise melt temperature at the same output.
Compared with a general-purpose 28 wt% VA, 6 MI EVA, the 55 MI grade shows substantially lower melt strength and is not appropriate for applications requiring high unsupported tubular form. However, the 40 wt% VA content provides markedly better carbon black acceptance than the 28 wt% VA grade at equivalent filler loading. The lower-melt-index grade often requires higher processing temperatures to achieve the same degree of dispersion, which accelerates deacetylation and can form additional gel particles during extended runs. The Ateva 4030ACX grade therefore occupies a narrow processing window: low melt viscosity supports high carbon black loadings and fine-screen filtration, while low melt strength demands controlled die-to-cooling distances and mechanical support in cable extrusion.
For compounds formulated with hygroscopic conductive carbon black and Ateva 4030ACX, pre-drying at 60–70 °C for 4 h in a desiccant dryer with a −40 °C dew point is recommended when ambient relative humidity exceeds 60 %. Moisture uptake in carbon black can create steam-induced porosity in the shield layer during continuous vulcanization, and acetic acid released from EVA deacetylation above 230 °C can corrode downstream tooling. Storage contact with copper or brass should be avoided if free acetic acid is present; purging with low-MI EVA or LDPE after production reduces resin residence time in hot barrels. Prolonged contact with strongly alkaline or amine-based additives should also be avoided because such materials accelerate ester hydrolysis.
Published data for 4030ACX in direct current high-voltage cable shields operating above 320 kV are limited, and qualification must be performed against IEC 62895:2017 or the specific cable system test program. The resin alone is not a semiconductive compound; final volume resistivity, surface smoothness, and heat-age performance depend on carbon black type, dispersion, peroxide selection, and extrusion conditions. The low-gel designation does not eliminate the need for melt filtration in the cable manufacturer’s line, and compounding trials should include carbon black dispersion testing according to ASTM D2663-14 or equivalent microtome-based methods to confirm that agglomeration remains below the cable shield surface-smoothness limit.