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Anhui Liwei Chemical Co., Limited.

ELEVATE EM531AA Ethylene Vinyl Acetate Copolymer

    • Product Name: ELEVATE EM531AA Ethylene Vinyl Acetate Copolymer
    • 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 869014
    Density 0.938 g/cm³
    Melt Flow Rate 2.5 g/10 min at 190°C/2.16 kg
    Vinyl Acetate Content 18 wt%
    Melting Point 88 °C
    Crystallization Point 63 °C
    Vicat Softening Point 65 °C
    Glass Transition Temperature -40 °C
    Tensile Strength At Break 14.5 MPa
    Elongation At Break 780%
    Flexural Modulus 23 MPa
    Shore A Hardness 90
    Brittleness Temperature -70 °C

    As an accredited ELEVATE EM531AA Ethylene Vinyl Acetate Copolymer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Available in 25 kg sealed polyethylene-lined bags, supplied as free-flowing pellets, palletized and stretch-wrapped for safe transport.
    Container Loading (20′ FCL) 20′ FCL loading of ELEVATE EM531AA ethylene vinyl acetate copolymer in palletized bags, securely stowed, ventilated, and protected from moisture and heat.
    Shipping ELEVATE EM531AA Ethylene Vinyl Acetate Copolymer ships as solid pellets in moisture-resistant bags or bulk containers. Non-hazardous under transport regulations, it requires dry, covered conditions to prevent clumping and contamination. Avoid excessive heat and humidity during transit. Standard handling equipment recommended. Ensure secure palletization for safe loading and unloading.
    Storage Store ELEVATE EM531AA Ethylene Vinyl Acetate Copolymer in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and ignition sources. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid stacking excessively to prevent deformation. Maintain temperatures below 30°C. No special hazards; handle with standard industrial hygiene practices.
    Shelf Life Shelf life is typically two years when stored in a cool, dry area away from direct sunlight and moisture.
    Application of ELEVATE EM531AA Ethylene Vinyl Acetate Copolymer

    At What Application Temperature Does EM531AA Shift Open Time in Carton Sealing?

    Hot-melt packaging adhesives formulated with ethylene vinyl acetate copolymers rely on a vinyl acetate content between 18 wt% and 28 wt% to depress the polyethylene crystalline melting point into a window compatible with 160 °C180 °C slot-die application. In compounds where EM531AA — a 2.5 g/10 min melt flow rate grade measured by ISO 1133-1:2022 — is used as the high-viscosity polymer component, the adhesive backbone is blended at 15 wt%30 wt% with a lower-molecular-weight EVA or metallocene ethylene-octene copolymer, tackifier at 35 wt%45 wt%, paraffin or Fischer-Tropsch wax at 20 wt%30 wt%, and hindered phenolic antioxidant at 0.3 wt%1.0 wt%. The higher molecular weight of EM531AA raises cohesive strength and extends open time relative to adhesive grades with melt flow rates above 50 g/10 min; open time on corrugated board is therefore controlled through wax melting point and application temperature rather than by polymer concentration alone. Processing is carried out in a heated Sigma-blade mixer or co-rotating twin-screw extruder with L/D 30:1 at 140 °C170 °C under nitrogen blanketing, followed by delivery through heated hoses at 150 °C170 °C to slot-die or roller coaters. Compliance for food-contact carton sealing falls under FDA 21 CFR 175.105 and EU 10/2011 where applicable, with REACH registration documentation for monomer residues. Finished article types include corrugated carton seam closures, bookbinding hinge adhesives, and wrap-around label adhesives.

    Heated equipment must be flushed with low-melt-index LDPE before shutdown because residual EM531AA/tackifier blends can form crosslinked gels if held above 180 °C for more than 4 h under oxygen. Batch viscosity measured at 170 °C with a Brookfield Thermosel at 20 rpm typically falls between 8 Pa·s and 25 Pa·s, and the final adhesive is passed through 150 µm screen packs before application. This operational boundary directly affects nozzle plugging frequency on corrugated converting lines running at 300 m/min600 m/min.

    Closed-Cell EVA Foam Processing Windows for Footwear Midsoles

    In crosslinked foamed midsoles, EM531AA is specified at 30 phr70 phr of the total 100 phr polymer blend, with a higher vinyl acetate EVA or polyolefin elastomer making up the balance; the grade contributes stiffness while the higher-VA component improves flexibility and filler uptake. The blowing agent azodicarbonamide is added at 2.5 phr4.5 phr, dicumyl peroxide at 0.5 phr1.0 phr, zinc oxide at 1.5 phr3.5 phr, stearic acid at 0.5 phr1.0 phr, and calcium carbonate filler at 10 phr20 phr; the target foam density is 0.16 g/cm³0.25 g/cm³ measured by ISO 845. Processing starts in an internal mixer at 100 °C115 °C for 8 min12 min, followed by two-roll milling with nip gap 2 mm4 mm; expansion and crosslinking are then performed by compression molding at 155 °C165 °C under 10 MPa15 MPa for 5 min8 min. The critical thermal boundary is the dicumyl peroxide decomposition onset near 140 °C150 °C; if the mix discharge temperature exceeds 120 °C, premature crosslinking reduces cell uniformity. Compliance testing uses ASTM D638-22 tensile properties, ASTM D2240 Shore A hardness, and ISO 7214 cellular plastics compression set; REACH Annex XVII Entry 50 PAH limits apply to finished footwear articles. Finished products comprise athletic shoe midsoles, comfort sandals, and removable insoles.

    On production-scale internal mixers, the main failure mode is batch-to-batch viscosity drift caused by variable calcium carbonate moisture; material containing more than 0.3 % moisture should be pre-dried at 70 °C for 3 h before mixing. When azodicarbonamide content exceeds 4.0 phr, the decomposition gas pressure during molding can force flash from the tool unless the mould vents are maintained below 0.5 mm. These boundaries explain why EM531AA is often limited to 30 phr50 phr in high-expansion midsoles and can be increased to 70 phr only when density is raised above 0.20 g/cm³.

    Halogen-free flame-retardant sheathing compounds for low-voltage control and instrumentation cables are formulated with EM531AA as the polar ethylene copolymer component in a polymer matrix that also contains LLDPE or HDPE. In these compounds, the polymer fraction is loaded at 30 wt%40 wt% of the total formulation, aluminum trihydrate or magnesium dihydrate at 50 wt%65 wt%, zinc borate at 2 wt%5 wt%, organosilane coupling agent at 0.5 wt%1.5 wt%, and hindered phenolic antioxidant at 0.2 wt%0.5 wt%. EM531AA is incorporated at 60 phr80 phr of the polymer phase because its polar comonomer improves filler wetting over neat polyethylene and reduces melt-pressure fluctuation when the compound is discharged through a co-rotating twin-screw extruder with L/D 40:1; the temperature profile is maintained between 150 °C and 180 °C, and pre-drying at 60 °C70 °C for 4 h is required when storage relative humidity exceeds 60 %. Compliance is anchored to IEC 60332-1-2 for vertical flame propagation, IEC 60754-2 for pH and conductivity of evolved gases, and EN 50363-5 for LSZH sheathing compounds; tensile retention after ageing is evaluated by IEC 60811-501. Finished products include control cable sheaths, photovoltaic array cable jackets, and railway rolling stock wiring jackets requiring halogen-free performance.

    StandardPropertyTypical acceptance threshold
    IEC 60332-1-2Vertical flame propagationburn length ≤ 425 mm
    IEC 60754-2Gas pHpH ≥ 4.3
    IEC 60754-2Conductivity10 µS/mm
    EN 50363-5LSZH sheathing compoundtensile strength ≥ 9 MPa

    When EM531AA Acts as a High-Tolerance Carrier in Additive Masterbatches

    When EM531AA is selected as a carrier resin for additive masterbatches, the selection is based on the balance between polyolefin compatibility and polar pigment wetting provided by the vinyl acetate comonomer. In pigment or additive concentrates, the carrier loading is 30 wt%75 wt% depending on dispersive demand: inorganic TiO₂ concentrates may require 60 wt% carrier, while carbon black concentrates run at 40 wt%55 wt% carrier with wax and dispersant additions up to 10 wt%; the final concentrate is let down in polyolefin articles at 2 wt%5 wt%. Downstream compounding is carried out on a co-rotating twin-screw extruder with L/D 36:1 to L/D 44:1, with side feeding at the 40 % barrel length position for mineral fillers, vacuum devolatilization at -0.08 MPa, and melt temperature held at 140 °C170 °C; strand pelletizing produces granules with bulk density of 550 kg/m³700 kg/m³. Compliance for masterbatches entering food packaging is assessed under FDA 21 CFR 177.1350 and EU 10/2011, while general products are documented against REACH and RoHS 2011/65/EU. Finished product types include white masterbatches, flame-retardant concentrates, and slip/anti-block concentrates for film extrusion.

    In masterbatch production, the limiting step is not melting but filler induction at the side feeder. When CaCO₃ or TiO₂ is fed above 65 wt%, screw speed must be reduced to 250 rpm350 rpm on a 75 mm machine to avoid over-torque; specific energy input above 0.25 kWh/kg can cause polymer degradation and die-lip build-up. Carrier resin melt temperature should not exceed 170 °C during compounding, and pelletizing water temperature is maintained at 10 °C20 °C to prevent pellet blocking. These parameters result in final masterbatch filter pressure values below 0.5 MPa when tested on a 14 µm screen pack.

    In cast coextruded pouch films, EM531AA is placed in the sealant skin layer because the vinyl acetate comonomer reduces heat-seal initiation temperature to a range not attainable with unmodified LDPE. The sealant layer formulation uses EM531AA at 80 wt%100 wt% of the skin resin, optionally blended with LDPE at 10 wt%20 wt% or with polybutene for lower modulus; target skin thickness is 15 µm30 µm in a total film thickness of 70 µm120 µm. The cast film line runs at melt temperatures of 190 °C230 °C, die gap 0.8 mm1.2 mm, and chill roll temperature 15 °C25 °C; heat seal strength is measured under ASTM F88/F88M-21. Compliance for food contact films is established by FDA 21 CFR 177.1350 and EU 10/2011, with overall migration below 10 mg/dm² for the EVA layer. Finished article types include retort pouch inner sealants, lidding film heat-seal layers, and medical device packaging lamination film where ISO 11607-1 sealing integrity documentation is required.

    Tuning Injection Moulding Parameters for Flexible EM531AA Components

    Injection-moulded flexible components are produced from EM531AA as a neat resin or in blends with LDPE or EPDM at 60 wt%80 wt% EM531AA. The material is processed at melt temperature 150 °C190 °C and mould temperature 20 °C40 °C, with injection pressure 60 MPa100 MPa and holding pressure 40 MPa70 MPa; shrinkage allowance is 1.0 %2.0 % measured by ISO 294-4, tensile properties are evaluated under ISO 527-2, hardness under ISO 868 Shore D, and environmental stress crack resistance under ASTM D1693. Compliance for electrical components uses RoHS 2011/65/EU; REACH documentation applies to European Union shipment. Finished product types include wire grommets, protective end caps, and appliance feet.

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    Certification & Compliance
    More Introduction

    ELEVATE EM531AA Ethylene Vinyl Acetate Copolymer is a free-flowing pelletized polyolefin copolymer with a nominal vinyl acetate content of 18 wt% measured by ASTM D5594. Melt index at 190°C under 2.16 kg load is 2.5 g/10 min in accordance with ASTM D1238 and ISO 1133-1:2022. Density measured by ASTM D1505 is 0.940 g/cm³. The DSC melting peak is approximately 86°C under ASTM D3418, and the Vicat softening temperature is approximately 64°C under ASTM D1525. These values are representative and are not specification limits.

    Vinyl acetate incorporation suppresses crystalline order relative to LDPE, reducing modulus and heat-seal initiation while increasing adhesion to polar surfaces and filler uptake. The melt index of 2.5 g/10 min provides an intermediate flow path suited to cast film sealant layers, injection molding of flexible components, and compounding with fillers and tackifier resins. Processing above 230°C should be avoided because pendant acetate groups begin eliminating acetic acid, causing downstream metal corrosion and discoloration. Unlike LDPE of equivalent melt index, the product exhibits greater environmental stress crack resistance under ASTM D1693 and improved adhesion in coextruded sealant layers. The material is not intended for sustained service above 60°C under load unless crosslinked.

    How Do Melt Index and Vinyl Acetate Content Set the Heat-Seal, Adhesion, and Compounding Window?

    The heat-seal initiation temperature in cast coextruded structures typically falls within 85–90°C when measured by ASTM F2029. This is lower than LDPE sealants of comparable melt index by approximately 15–25°C and permits shorter sealing dwell times on packaging lines. The comonomer also improves filler wetting of calcium carbonate, magnesium hydroxide, and aluminum trihydrate. Practical addition level is governed by viscosity rise in continuous mixing rather than by gross incompatibility. At filler loading above 30 wt%, the copolymer exhibits lower melt viscosity than LDPE at equivalent loading, permitting twin-screw side-feed operation at screw speeds near 300 rpm. However, filler levels above 50 wt% reduce melt strength sufficiently to destabilize strand pelletizing unless a high-melt-strength EVA or low-melt-index grade is blended at 10–20 wt%.

    PropertyRepresentative valueTest method
    Vinyl acetate content18.0 wt%ASTM D5594
    Melt index2.5 g/10 minASTM D1238 (190°C, 2.16 kg)
    Density0.940 g/cm³ASTM D1505
    Tensile strength at break15 MPaASTM D638 Type IV, 500 mm/min
    Elongation at break750%ASTM D638 Type IV
    Shore A hardness91ASTM D2240
    DSC peak melting temperature86°CASTM D3418
    Vicat softening temperature64°CASTM D1525

    In flexible packaging sealant layers, the material is coextruded at 2–8 wt% of total structure thickness on cast film lines using a set temperature profile from 150°C at the feed throat to 205°C at the die. Adhesion to oriented polyester under heat-seal testing at 120°C and 0.5 s dwell is often limited by cohesive failure in the EVA layer rather than interfacial separation, indicating that the bond interface exceeds the yield strength of the sealant. On aluminum foil, the polar acetate group provides hydrogen-bonding character, reducing the need for an acid primer. Peel strengths measured by ASTM D903 commonly fall from 4 N/15 mm to 1 N/15 mm when the foil is contaminated with 0.1 mg/m² of hydrocarbon processing oil.

    In injection molding of flexible cleats, caps, and footwear sidewalls, melt temperatures of 170–190°C and mold temperatures of 15–25°C are sufficient to fill multi-cavity tools on presses with clamp forces from 80 t to 250 t. Long flow-length-to-thickness ratios above 150:1 can exhibit sink marks unless packing pressures above 60 MPa are maintained.

    When EM531AA Replaces Higher-VA EVA or Low-Density Polyethylene in Multi-Layer Structures

    Relative to a 12 wt% vinyl acetate EVA, EM531AA lowers seal initiation by roughly 8–10°C, increases softness, and improves adhesion to polyester and paper. Relative to a 28 wt% vinyl acetate EVA, EM531AA reduces pellet blocking, lowers surface tack, and retains sufficient thermal stability for processing at approximately 20°C higher melt temperature without rapid acetic acid evolution. This places the grade in the intermediate adhesion and tack window that suits sealant films and filled compounds rather than high-tack hot-melt adhesives. Compared with ethylene methyl acrylate copolymers of equivalent melt index, EM531AA generates acetic acid during processing, whereas EMA generates methanol; this difference influences corrosion control and odor management in coating lines. EM531AA generally offers lower resin density and higher filler acceptance than EMA of similar comonomer content.

    Grade or materialVinyl acetate contentMelt indexDensityProcessing and application distinction
    ELEVATE EM530AA18 wt%0.7 g/10 min0.940 g/cm³High melt strength; profile extrusion, heavy-wall sheet, thick foam plank
    ELEVATE EM531AA18 wt%2.5 g/10 min0.940 g/cm³Balanced flow; cast film sealants, injection molding, filled compounds
    ELEVATE EM532AA18 wt%5.0 g/10 min0.940 g/cm³High flow; thin-wall injection, low-viscosity compounding
    Reference LDPE0 wt%2.0 g/10 min0.920 g/cm³Higher seal initiation and stiffness; lower adhesion to polar substrates
    Reference high-VA EVA28 wt%3.0 g/10 min0.950 g/cm³Lower thermal stability, higher tack, lower hardness

    Continuous compounding of EM531AA on a corotating twin-screw extruder with L/D 40:1 and segmented kneading blocks typically operates at barrel temperatures of 160–190°C, screw speed of 250–350 rpm, and specific energy input of 0.15–0.25 kWh/kg. At screws with L/D below 24:1, unmelted polymer pellets can persist in the melt stream and produce surface defects. In foam expansion, azodicarbonamide blowing agent decomposes at 200–215°C. The 2.5 g/10 min melt index maintains bubble stability at density reductions from 0.940 g/cm³ to approximately 0.15–0.25 g/cm³ when crosslinked with dicumyl peroxide at 0.5–1.0 phr. Published data for this specific foam density response in EM531AA is limited; the range represents typical processing windows for 18 wt% vinyl acetate EVA.

    Foam expansion is process-critical because azodicarbonamide decomposition begins at 200°C, only 10°C below the temperature at which acetic acid elimination accelerates in EVA. Plant trials on a 26:1 L/D extruder with a melt pump and underwater pelletizer have shown that a die melt temperature of 195–205°C and a residence time under 3 minutes prevent pre-foaming while allowing complete blowing agent decomposition. The 2.5 g/10 min melt index provides sufficient melt strength to retain closed cells at densities as low as 0.20 g/cm³. When density falls below 0.15 g/cm³, cell walls thin beyond the extensional strength of the melt, producing open-cell formations and surface collapse unless the melt is crosslinked before expansion.

    Thermal Stability Boundaries, Acetic Acid Elimination, and Extrusion Equipment Requirements

    Thermal stability is governed by the pendant acetate groups. At melt temperatures above 210°C, acetic acid elimination accelerates; sustained operation above 230°C generates corrosive volatiles that attack chrome-plated die lips, aluminum cooling rolls, and ventilation ductwork. Barrel residence time should not exceed 10 minutes at temperatures above 200°C. The extrusion processing window is therefore maintained between 170°C and 210°C, with the die temperature held below 215°C.

    Moisture uptake above 60% relative humidity can result in hydrolysis and splay. Pre-drying in a desiccant hopper at 60–70°C for 4 hours to a dew point of -40°C is required for cast film and injection molding when packaging has been opened for more than 8 hours in humid conditions. Addition of zinc stearate or other acid scavengers can reduce acetic acid evolution but may alter peroxide crosslinking efficiency; such additive changes should be validated by oscillating rheometry at 150°C and 1.67 Hz using ASTM D4440.

    Incoming resin specification should include melt index ratio I21.6/I2.16 to detect lot-to-lot molecular weight distribution shifts. For EM531AA, the melt index ratio is typically 60–75 when measured by ASTM D1238 at 190°C. A shift above 80 can indicate high-molecular-weight tails that increase die swell and reduce melt flow in thin-gage film. A shift below 55 can indicate molecular weight reduction that lowers melt strength and changes bubble stability in blown film.

    For food contact applications, the resin is supplied under the conditions of 21 CFR 177.1520 and may be used in contact with food types under the temperature and thickness limitations applicable to olefin copolymers in the relevant paragraph. Compliance with REACH and RoHS 2011/65/EU Annex II is documented through supplier safety data sheets and product stewardship declarations. Verification of specific migration for vinyl acetate monomer under Regulation (EU) No 10/2011 is required for final packaging structures.

    In peroxide-crosslinked foam applications, dicumyl peroxide half-life is approximately 1 hour at 150°C; the cure cycle between 150°C and 180°C must allow complete decomposition before the temperature reaches the azodicarbonamide decomposition range. Residual peroxide above 0.05 phr can produce odor and discoloration in finished foam. The material is not recommended for continuous service above 60°C without crosslinking, nor for contact with strong oxidizing acids or ketone solvents that can swell or attack the acetate group.