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Anhui Liwei Chemical Co., Limited.

Celanese Vinyl Acetate EVA Grade HQ 14-17

    • Product Name: Celanese Vinyl Acetate EVA Grade HQ 14-17
    • Factroy Site: Lingwu, Yinchuan, Ningxia, China
    • Price Inquiry: sales2@liwei-chem.com
    • Manufacturer: Anhui Liwei Chemical Co., Limited.
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    Specifications
    HS Code 335967
    Vinylacetatecontent 14-17 wt%
    Density 0.930 g/cm³
    Meltflowrate 2.5 g/10 min at 190°C/2.16 kg
    Meltingpoint 75°C
    Vicatsofteningpoint 50°C
    Tensilestrengthatbreak 14 MPa
    Elongationatbreak 800%
    Hardnessshored 38
    Glasstransitiontemperature -20°C
    Brittlenesstemperature -40°C
    Volumeresistivity 10^15 ohm·cm
    Waterabsorption 0.05%

    As an accredited Celanese Vinyl Acetate EVA Grade HQ 14-17 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Celanese Vinyl Acetate EVA Grade HQ 14-17 is packaged in 25 kg polyethylene-lined paper bags, palletized and stretch-wrapped.
    Container Loading (20′ FCL) 20′ FCL loading of Celanese Vinyl Acetate EVA Grade HQ 14-17: drums palletized, secured, vented, and labeled for safe transport.
    Shipping Celanese Vinyl Acetate EVA Grade HQ 14-17 ships in dedicated isotanks, stainless steel drums, or lined containers to preserve purity. Use nitrogen blanketing and keep away from heat, sparks, and UV to prevent polymerization. Ensure proper grounding, leak-proof seals, and hazardous material labeling per regulations.
    Storage Store Celanese Vinyl Acetate EVA Grade HQ 14-17 in tightly sealed, properly grounded containers in a cool, dry, well-ventilated area. Keep away from heat, sparks, open flames, direct sunlight, and incompatible materials such as strong oxidizers. Maintain recommended storage temperature to prevent polymerization. Use explosion-proof equipment, inspect containers regularly for leaks, and follow the Safety Data Sheet.
    Shelf Life Shelf life is typically 12 months from shipment date when stored in original, unopened packaging in a cool, dry area.
    Application of Celanese Vinyl Acetate EVA Grade HQ 14-17

    Closed-cell EVA foam for athletic footwear midsoles, insoles, and sheet goods is processed from formulations in which Celanese Vinyl Acetate EVA Grade HQ 14-17 is charged at 100 phr as the primary polymer, with azodicarbonamide at 2.5–5.0 phr, dicumyl peroxide at 0.7–1.2 phr, zinc oxide at 1.0–2.0 phr, zinc stearate at 0.5–1.0 phr, and calcium carbonate at 0–20 phr where higher hardness or sheet flatness is specified. The 14–17% vinyl acetate segment is used to control crystallinity and modulus after foaming; blends with a 26% VA EVA grade at ratios of 70/30, 50/50, or 30/70 are applied to shift Asker C hardness from approximately 55 to 70 in finished midsoles. Mixing is conducted in an intermeshing-rotor internal mixer with a 75 L chamber, 0.75–0.85 fill factor, rotor speed 35–45 rpm, and a drop temperature of 105–110 °C, followed by a two-roll mill at 90–100 °C with a nip gap of 2–4 mm to form sheets of 1.5–3.0 mm; the sheet is then pelletized. Foaming is performed in a hydraulic compression press at 165–175 °C under 150–200 bar platen pressure for 8–12 min, after which cooling plates stabilize cell structure. Batch-to-batch variance in density is typically correlated with residual moisture and peroxide dispersion; pre-drying of EVA pellets at 60–70 °C for 2–4 h is used when storage humidity exceeds 60% RH. Compliance for footwear foam exported to the EU is governed by REACH Regulation (EC) No 1907/2006, Annex XVII entry 50 for polycyclic aromatic hydrocarbons, and by EN 71-3 for heavy metal migration when articles are marketed for children; density and compression set are evaluated according to ISO 845 and ASTM D395-18, respectively. Terminal finished product types include compression-molded midsoles for running and court footwear, die-cut or injection-molded insoles, orthotic core layers, flip-flop soles, and closed-cell EVA foam sheets for protective packaging and sports mats.

    When hot-melt adhesive softening point and substrate adhesion are governed by vinyl acetate distribution

    For hot-melt adhesive compounding used in packaging and graphic-arts bonding, Celanese Vinyl Acetate EVA Grade HQ 14-17 is charged at 20–40 wt% of total formulation mass, with a rosin ester or hydrocarbon tackifier at 30–50 wt%, a paraffin, microcrystalline, or Fischer-Tropsch wax at 5–15 wt%, and a hindered phenolic or phosphite antioxidant at 0.5–1.0 wt%. The 14–17% VA content provides polarity at the adhesive-substrate interface sufficient for fiber tear on coated paperboard while limiting low-temperature embrittlement relative to 9–12% VA grades. Mixing is performed in a vertical change-can mixer with a jacketed vessel at 150–170 °C under a nitrogen blanket, or in a twin-screw adhesive extruder with L/D 20–30 and barrel zones from 120 °C to 170 °C; batch mixing times of 20–40 min are typical until a clear, uniform melt is obtained. Viscosity is measured by ASTM D3236-88 at 177 °C and is typically adjusted to 800–2,500 mPa·s for slot-die and bead application, while lower-viscosity formulations below 800 mPa·s are used for wheel and spray lines; ring-and-ball softening point measured by ASTM E28-18 commonly falls between 80 °C and 105 °C. For food-contact packaging adhesives, formulations meet FDA 21 CFR 175.105 for indirect food additives, with migration limits meeting 21 CFR 175.300 where the adhesive is used in packaging that may contact aqueous or fatty foods; EU requirements are covered by Regulation (EC) No 1935/2004 and Regulation (EU) No 10/2011 for plastic layers. Downstream application comprises melting at 150–180 °C in heated hose and gun assemblies, then depositing through slot-die coaters, spiral spray nozzles, or wheel applicators at line speeds of 50–300 m/min depending on packaging configuration. Terminal finished product types include corrugated carton and case sealing, bookbinding adhesive layers, paper cup and bag seams, lamination for flexible food pouches, and assembly adhesives for nonwoven hygiene products.

    Heat-seal layer engineering in cast coextruded barrier laminates

    Because seal initiation temperature and hot-tack strength limit packaging line speed, cast coextruded barrier laminates incorporate Celanese Vinyl Acetate EVA Grade HQ 14-17 as the sealant web at 100% or as a blend at 10–30 wt% EVA in the surface layer, with the balance supplied by LDPE or LLDPE. This VA range lowers seal initiation temperature and extends hot-tack strength when compared with LDPE-only seal layers, while avoiding excessive surface tack and machine-direction stretch that higher-VA grades can introduce on chill-roll lines. The material is processed on a single-screw extruder with a barrier screw, L/D 30–36, screw diameter 45–90 mm, and barrel temperatures from 180 °C near the feed throat to 230 °C at the die, with a melt temperature measured by infrared pyrometry of 210–240 °C; the melt is cast through a flat die with 0.8–1.5 mm lip gap onto a polished chill roll held at 15–25 °C, and film thickness is controlled at 12–60 µm. Corona discharge at 1.0–2.5 kW may be applied downstream for lamination anchorage, but excessive treatment can increase coefficient of friction on the sealant side. Compliance for food-contact films is established under FDA 21 CFR 177.1350 for ethylene-vinyl acetate copolymers, with overall migration tested according to Regulation (EU) No 10/2011 and the 10 mg/dm² overall migration limit; seal strength and hot-tack are measured according to ASTM F88/F88M-21 and ASTM F1921/F1921M-20. Terminal finished product types include sealant webs in coextruded PP/EVOH/PE and PET/PE barrier laminates, lidding films for fresh produce and dairy, medical device pouches, and overwrap for hygiene products.

    Across twin-screw compounding lines producing color and additive masterbatches for polyolefin films, foams, and cable compounds, Celanese Vinyl Acetate EVA Grade HQ 14-17 functions as a carrier resin at 40–80 wt% of the compound, with organic or inorganic pigments and functional additives at 20–60 wt%, and a processing aid or polar dispersant at 2–5 wt%. Mixing is performed on a co-rotating twin-screw extruder with L/D 40–52:1, screw diameter 25–75 mm, and zone temperatures from 140 °C at the feed barrel to 190 °C at the die, with twin-screw side feeders used for pigments to minimize dusting and agglomeration. Melt filtration through screen packs at 100–250 µm aperture is applied before underwater or strand pelletizing; underwater pelletizing is preferred for high pigment loading because it reduces melt fracture and surface oxidation. Quality control includes MFR measurement according to ISO 1133-1:2022 and filter pressure value according to EN 13900-5 for pigment dispersion. Compliance for color and additive masterbatches sold in the EU is set by REACH Regulation (EC) No 1907/2006, and where the masterbatch is used in food-contact plastic articles, the final article must comply with Regulation (EU) No 10/2011 and 21 CFR 174–178 as applicable; RoHS Directive 2011/65/EU applies to masterbatches used in electrical and electronic applications. Terminal finished product types include color masterbatches for EVA footwear foam, UV stabilizer masterbatches for greenhouse films, antioxidant and processing-aid masterbatches for polyolefin film extrusion, and flame-retardant masterbatches for cable and construction sheet.

    What restricts ATH and MDH loading in halogen-free flame-retardant cable jacket compounds?

    Halogen-free flame-retardant cable jacket and insulation compounds formulated with Celanese Vinyl Acetate EVA Grade HQ 14-17 at 100 phr are modified with aluminum trihydrate at 80–150 phr, magnesium dihydroxide at 20–60 phr, a vinyl silane coupling agent at 0.5–1.5 phr, a hindered phenolic antioxidant at 0.5–1.5 phr, and dicumyl peroxide at 1.0–3.0 phr when a crosslinked insulation is required. The 14–17% VA content is at the lower end of the range typically used for high-filler HFFR compounds, so filler wetting and low-temperature flexibility are more sensitive to screw configuration and coupling-agent dose than for EVA grades with 18–28% VA; published data for this specific configuration is limited, and production-scale rheology validation is required before commercial use. Compounding is performed on a co-rotating twin-screw extruder with L/D 44–56:1, atmospheric vent at zone 5, side feeding of ATH and MDH at zone 5 or 6, barrel temperatures from 130 °C to 170 °C, and screw speed 250–400 rpm; melt temperature is kept below 180 °C to avoid premature peroxide decomposition. The mixed pellets are dried at 70–80 °C for 4–6 h before cable extrusion. Insulation is applied on a single-screw cable extruder with L/D 24–30, melt temperature 130–160 °C, and crosslinked by peroxide cure in a continuous vulcanization line; vulcanization kinetics are evaluated by ISO 6502-2:2018 moving-die rheometer, and tensile properties by ASTM D638-14. Flame spread is evaluated according to IEC 60332-1-2, halogen acid gas by IEC 60754-2, smoke density by IEC 61034-2, and automotive cable requirements by ISO 6722; EU-restricted substances are controlled under RoHS Directive 2011/65/EU. Terminal finished product types include halogen-free building riser cable jackets, solar PV cable insulation, railway transit cable sheathing, and automotive single-core battery cable insulation.

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    Certification & Compliance
    More Introduction

    Celanese Vinyl Acetate EVA Grade HQ 14-17 is a vinyl acetate–ethylene copolymer identified by a nominal vinyl acetate incorporation of 14–17 wt%. The product sits between low-density polyethylene and high-vinyl acetate EVA in terms of polarity, crystallinity, and low-temperature ductility. The grade designation is read as a composition window rather than a melt flow rate; the melt flow rate at 190 °C/2.16 kg must be obtained from the supplier datasheet and verified by ISO 1133-1:2022 or ASTM D1238. Within this composition interval, the polyethylene backbone retains enough linear ethylene sequence length for semi-crystalline strength, while acetate side groups disrupt crystallite growth, increase polarity, and reduce the brittle transition at low temperature. The polymer is normally supplied as free-flowing pellets for single-screw extrusion, coextrusion, injection molding, and compounding. Published lot-specific physical data for HQ 14-17 are limited in open industrial literature; production trials therefore use property envelopes established for EVA copolymers in the same vinyl acetate window, with datasheet confirmation for exact melt index and additive content.

    Where Does the 14–17 wt% Vinyl Acetate Window Sit Between LDPE and 18–28 wt% VA Copolymers?

    The property transition from non-polar LDPE to increasingly polar EVA is governed by comonomer mole fraction and short-chain branching distribution along the ethylene backbone. At 9 wt% VA, the copolymer retains a well-defined orthorhombic polyethylene crystallite population, which produces relatively high tensile modulus, higher heat deflection, and lower tack. From 14 wt% to 17 wt% VA, crystalline ethylene sequence length decreases; the melting peak is depressed from an LDPE range of 105–112 °C to a typical EVA melting peak of 86–95 °C as measured by ISO 11357-3 or ASTM D3418. This reduction lowers heat-seal initiation temperature while retaining sufficient mechanical integrity for rigid and semi-rigid parts. At 28 wt% VA, the material moves further into amorphous clarity and adhesive tack but sacrifices hardness, creep resistance, and heat resistance. The 14–17 wt% band is therefore an intermediate range: it provides better polar adhesion than LDPE and better dimensional stability at elevated temperature than 18–28 wt% VA grades.

    Rapid verification of vinyl acetate content in the 14–17 wt% window is commonly performed by FTIR per ASTM D5594; exact comonomer sequence distribution requires carbon NMR or DSC crystallinity analysis. Sequence distribution, not solely average VA content, controls seal initiation temperature, low-temperature impact, and optical clarity.

    Representative property gradient for EVA copolymers by nominal vinyl acetate content
    Property9 wt% VA14–17 wt% VA (HQ 14-17 designation)28 wt% VAReference method
    Density0.930–0.935 g/cm³0.935–0.945 g/cm³0.950–0.960 g/cm³ISO 1183-1:2019, ASTM D1505
    DSC melting peak95–100 °C86–95 °C70–78 °CISO 11357-3, ASTM D3418
    Shore D hardness42–4835–4222–30ISO 868, ASTM D2240
    Tensile strength at yield16–28 MPa15–25 MPa8–15 MPaISO 527-2, ASTM D638-14
    Crystalline fraction trendHigherModerateLowDSC enthalpy ratio

    Table values are representative cross-grade ranges from polymer science literature and EVA datasheet aggregates; they are not a guarantee for HQ 14-17 because additive packages, MFR, and production site can influence final properties. For incoming quality control, the property gradient should be supplemented by melt flow rate ratio or screw-recovery data from the actual molding cell, because values can shift by ±10% with additive package changes. The crystallisation peak measured during cooling by ISO 11357-3 is also used to track nucleation packages; some masterbatches shift the crystallization onset by 3–5 °C and affect dimensional stability in injection-molded parts.

    Under production-scale extrusion conditions, the process window for a 14–17 wt% VA EVA grade is narrower than for LDPE because shear heating, residence time, and metal contact must be balanced against the onset of vinyl acetate deacetylation. Single-screw extruders with L/D ratios of 24:1 to 30:1 and three-zone barrier screws are commonly used; barrel setpoints in the 150–200 °C range are typical, with die temperature maintained between 180 °C and 210 °C depending on melt flow rate. Sustained melt temperatures above 230 °C should be avoided because deacetylation releases acetic acid and increases the risk of autocatalytic oxidation. The exact profile must be adjusted to the grade MFR; the HQ 14-17 designation does not encode MFR, so a lot with a lower MFR may require a higher upstream temperature ramp and higher head pressure. Pre-drying at 60–70 °C for 2–4 h is recommended when storage relative humidity exceeds 60%. In injection molding, clamping force requirements typically fall near 3–5 kN/cm² of projected area, but tool geometry, wall thickness, and gate size shift the practical requirement. Head-pressure variation should be held within ±5% of baseline; fluctuations outside this band can indicate feed bridging, melt-index drift, or dispersion instability in compounded lots. MFR drift outside ±10% of the datasheet value should trigger screw speed or temperature correction before startup.

    In twin-screw compounding, a machine with L/D 40:1 to 48:1 and temperature zones not exceeding 210 °C at the mixing segments is preferred for filler concentrates. Reactive amine-based additive packages are not recommended in dry blends unless the process is pH-buffered, because residual acetic acid formed during processing can react with basic amines and produce volatile by-products or die-lip plate-out. This limitation is operational rather than a regulatory prohibition, and it becomes more significant when regrind is reused above 20 wt%. During grade changes from LDPE to HQ 14-17 on a shared extrusion line, purging is more demanding than LDPE-to-LDPE changes because residual EVA can degrade under the higher barrel temperatures used for subsequent engineering resins. The recommended purge procedure uses a lower-MFR LDPE or a commercial barrel-cleaning compound, with the screw pulled only after the melt temperature drops below 180 °C.

    When a 14–17 wt% VA Grade Is Used in Sealing Layers, Molded Components, and Compounded Concentrates Instead of LDPE or 18–28 wt% VA Resins

    Extrusion lamination and heat-seal packaging lines benefit from the intermediate seal initiation temperature, which is lower than LDPE but higher than 18–28 wt% VA copolymers. In flexible packaging coextrusions, a sealing layer containing HQ 14-17 can be run on existing high-speed lines without the excessive smoke and die-lip buildup often associated with high-VA grades. Because vinyl acetate content remains below 18 wt%, the resin retains enough crystallinity to control coefficient of friction and blocking resistance in film processes. In foam extrusion, the 14–17 wt% window balances melt strength and blowing-agent solubility; high-VA grades increase solubility of isobutane or carbon dioxide but reduce melt strength enough to cause cell coalescence. This grade sits in a region where cell size distribution is easier to control on tandem foam lines.

    Injection-molded footwear parts, cable jackets, and automotive trim benefit from low-temperature impact retention without excessive softness. The difference from 18–28 wt% VA EVA is most evident in Shore D hardness; the 14–17 wt% product remains harder and more dimensionally stable under load, while higher-VA grades offer higher elongation and better filler acceptance. Compared with LDPE, HQ 14-17 adds polar adhesion to inks, primers, and polar substrates, but it may require higher antioxidant loading when processed near the upper temperature boundary. Surface energy increases from 31 mN/m for LDPE to approximately 34–36 mN/m for the 14–17 wt% VA band, which improves polar ink and primer wetting. Compared with lower-VA EVA grades in the 9–12 wt% range, HQ 14-17 has lower flexural modulus and improved low-temperature crack resistance, but lower tensile strength and a reduced upper service temperature. These trade-offs make the grade suitable as a compounding base for semicrystalline adhesive and sealant concentrates, although the final formulation must be evaluated under ISO 527-2 and ISO 868 rather than inferred from the base resin.

    Processors replacing LDPE with HQ 14-17 in an existing die must check backpressure and layer distribution. The VA comonomer increases adhesion to metal at elevated temperatures, so die-lip cleaning intervals may shorten if the die exit temperature is not reduced by 5–10 °C compared with LDPE. In extrusion coating, melt draw resonance can be suppressed by maintaining an air gap below 20 cm and adjusting the chill-roll temperature to 15–20 °C. Published data for this specific configuration is limited; these operating ranges are starting conditions, not a substitute for line-specific optimisation.

    At the molecular level, the acetate side group affects solubility parameter and migration kinetics in polymer matrices. The vinyl acetate unit has a higher dipole moment than ethylene, which increases solubility of polar processing aids and allows controlled migration of tackifiers in adhesive compounds. In food-contact sealing layers, migration testing under 21 CFR 177.1350 typically focuses on total non-volatile extractives and residual vinyl acetate monomer; resin suppliers can provide the current certificate of analysis, but the final film composite must be tested because migrated species may originate from tie layers or printing inks. These matrix effects are not unique to HQ 14-17 but are a direct consequence of the 14–17 wt% VA chemistry.

    Compliance documentation for Celanese Vinyl Acetate EVA Grade HQ 14-17 must be verified against the actual production lot, because polymerisation additives, carrier resins, and external stabilizers affect the final regulatory profile. A routine verification matrix applied to such a grade includes melt flow rate under ISO 1133-1:2022, density under ISO 1183-1:2019, tensile properties under ISO 527-2, hardness under ISO 868, and thermal transitions under ISO 11357-3. For food-contact use, ethylene-vinyl acetate copolymers may be evaluated under 21 CFR 177.1350 when the formulation does not contain non-listed additives or processing aids. RoHS compliance is generally assessed by screening restricted substances according to IEC 62321 series methods; typical acceptance limits are ≤ 0.1 wt% for lead, mercury, hexavalent chromium, PBB, and PBDE, and ≤ 0.01 wt% for cadmium. REACH obligations apply under Regulation (EC) No 1907/2006; users must confirm whether the grade contains candidate-list SVHCs above 0.1 wt% per article.

    Compliance and test matrix for EVA grade HQ 14-17 under typical industrial verification
    Verification areaReference standard or regulationMeasured/assessed parameterTypical acceptance basis
    Melt flow rateISO 1133-1:2022 / ASTM D1238MFR at 190 °C / 2.16 kgData sheet ± 10% or agreed specification
    DensityISO 1183-1:2019 / ASTM D1505Mass density at 23 °CGrade specification range
    Tensile propertiesISO 527-2 / ASTM D638-14Yield stress, break stress, elongationMFR-specific specification
    HardnessISO 868 / ASTM D2240Shore D at 15 sGrade specification range
    Thermal transitionsISO 11357-3 / ASTM D3418Melting peak, crystallization peakNo unexplained second peak
    Food contact21 CFR 177.1350Formulation and extractives limitsCompliance if no non-listed additives are used
    RoHSIEC 62321 seriesPb, Cd, Hg, Cr(VI), PBB, PBDE≤ 0.1 wt% for each restricted substance, Cd ≤ 0.01 wt%
    REACH SVHCRegulation (EC) No 1907/2006Candidate list substances≤ 0.1 wt% per article if applicable

    This matrix is a verification framework only; the legal interpretation and final compliance decision require lot-specific documentation from the material supplier and the finished-article manufacturer.