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Anhui Liwei Chemical Co., Limited.

WENEW Braskem America DVR 001A EVA Copolymer,60% Recycled Content,Foam & Footwear Grade

    • Product Name: WENEW Braskem America DVR 001A EVA Copolymer,60% Recycled Content,Foam & Footwear Grade
    • 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 690965
    Density 0.930 g/cm³
    Melt Flow Rate 190 C 2 16kg 6 g/10min
    Vinyl Acetate Content 15%
    Hardness Shore A 82
    Tensile Strength At Break 13 MPa
    Elongation At Break 600%
    Melting Point 75°C
    Vicat Softening Temperature 60°C
    Brittle Temperature -70°C
    Recycled Content 60%

    As an accredited WENEW Braskem America DVR 001A EVA Copolymer,60% Recycled Content,Foam & Footwear Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged as resin pellets in 25 kg polyethylene-lined paper bags, palletized and shrink-wrapped for transport.
    Container Loading (20′ FCL) 20′ FCL of WENEW DVR 001A EVA copolymer pellets, 60% recycled content, foam and footwear grade, packed in bags on pallets.
    Shipping This EVA copolymer ships as solid pellets in moisture-protective bags or bulk containers. Non-hazardous, it requires dry conditions to prevent clumping and moderate temperatures to avoid deformation. Standard freight handling applies, ensuring clean, contamination-free transit for foam and footwear manufacturing.
    Storage Store in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep in original, sealed packaging or compatible containers to prevent moisture absorption and contamination. Use proper palletization to avoid damage. Maintain moderate temperatures and low humidity, and separate from strong oxidizing agents or incompatible materials.
    Shelf Life Store in a cool, dry place away from sunlight and moisture. Shelf life is typically 12 months from date of manufacture.
    Application of WENEW Braskem America DVR 001A EVA Copolymer,60% Recycled Content,Foam & Footwear Grade

    Compression-moulded EVA midsoles produced with DVR 001A require a narrower processing window than virgin EVA because the recycled fraction introduces crosslinked gel domains, variable melt extensibility, and a slightly acidic residue profile. In a two-roll mill line, the compound is fluxed at 95–105 °C for 8–12 min before sheet-off, and dicumyl peroxide is added after the batch temperature drops below 90 °C to prevent premature decomposition. The peroxide level is set between 0.5 phr and 0.8 phr of 40 % active dicumyl peroxide; below 0.4 phr, compression set after 50 % deflection for 6 h at 50 °C per ISO 1856:2022 typically exceeds 30 %, and above 0.9 phr the crosslink density embrittles thin sidewall sections. Azodicarbonamide is maintained at 2.0–3.2 phr; above 3.5 phr, internal gas pressure during press cure generates split-level voids at the midsole centre. Zinc oxide at 0.8–1.2 phr and stearic acid at 0.3–0.5 phr are used to control blowing agent decomposition and release behaviour. Calcium carbonate at 5–15 phr functions as a nucleating agent and shrink compensator, but loadings above 20 phr raise foam density beyond the target range for athletic midsoles. Amine-based antistatic additives should be excluded from peroxide-cured DVR 001A formulations because they scavenge free radicals and suppress crosslink density.

    Formulation window for DVR 001A in compression-moulded midsole foam
    IngredientLoading rangeFunction and threshold constraint
    DVR 001A60–80 phrRecycled EVA base; gel variation requires incoming sieve control
    Virgin EVA, 18 % VA20–40 phrModifies melt strength and dilutes accumulated gel defects
    LDPE0–10 phrViscosity reducer; improves preform flow into deep cavity zones
    Dicumyl peroxide, 40 % active0.5–0.8 phrCrosslinking; below 0.4 phr compression set exceeds 30 %
    Azodicarbonamide2.0–3.2 phrGas source; above 3.5 phr causes internal splits
    Zinc oxide0.8–1.2 phrLowers ADC decomposition temperature and stabilises gas yield
    Stearic acid0.3–0.5 phrInternal lubricant and mould release; excess migrates to surface
    Calcium carbonate5–15 phrNucleation and shrinkage control; excess increases density

    Preform loading is set at 70–80 % of cavity volume to produce free expansion without excessive flash. Press cure is conducted at 160–165 °C under hydraulic pressure of 150 kg/cm²; moulding time is 8–10 min per 10 mm of unbounded thickness. After demoulding, the foam is stabilised at 60 °C for 24 h to release residual gases and allow dimensional relaxation. Final density is targeted at 0.18–0.25 g/cm³ per ASTM D792-20, Shore C hardness at 55–65 per ASTM D2240-15(2021), and rebound resilience at 40–50 % per DIN 53512. The recycled fraction in DVR 001A can contain crosslinked EVA chips from post-industrial footwear skiving and die-cut waste; these particles remain discrete in the melt phase and form visible pinholes in midsoles below 4 mm wall thickness. If incoming regrind is not sieved below 300 µm, surface pitting and reduced tear strength increase in production-scale runs. On continuous foamed sheet lines, a screen pack of 60/100/60 mesh is used, with pressure alarms set to trigger at a differential above 80 bar.

    Can DVR 001A Be Directly Injection Moulded Into Single-Piece Sandal Outsoles Without Losing Surface Finish?

    Direct injection moulding of DVR 001A into single-piece sandal outsoles is possible only when melt-viscosity variation is managed lot by lot. The grade is processed in a reciprocating-screw machine with L/D ratio 20:1–24:1 and compression ratio 2.0:1–2.5:1; the screw should have a lightly nitrided surface because the recycled fraction may carry mildly acidic residues. Nozzle melt temperature is held at 175–195 °C, with the front zone 5–10 °C lower than the nozzle to limit premature blowing agent decomposition. Mould water temperature is set between 25 °C and 45 °C. Pre-drying in a desiccant dryer at 80 °C for 4 h is required when ambient relative humidity exceeds 60 %; target moisture content is below 0.05 %. A vented barrel with vacuum at −0.08 MPa reduces splay caused by volatile residues from the recycled feedstock. Lot-to-lot melt mass-flow rate is measured per ASTM D1238-20 at 190 °C/2.16 kg; if the value shifts more than 15 % from the running virgin EVA reference, short shots or flash imbalance appear in multi-cavity tools.

    Fan gates of 1.5–2.0 mm depth with land length 3–5 mm are used for sole thickness of 4–6 mm. Injection speed is kept low to moderate to avoid shear heating that activates residual blowing agent prematurely at the gate. Hot runner needles with orifice below 0.5 mm are avoided because gel particles can block the valve. Mould shrinkage after 24 h is 1.2–1.8 %, and anisotropy increases when the post-industrial fraction exceeds 60 %; moving-core or dual-ejector set-ups compensate for this directional variation. Finished single-piece sandals, flip-flop soles, and clog shells are tested for Shore A hardness 55–75 per ASTM D2240-15(2021), tensile strength minimum 3.5 MPa per ISO 1798:2008, and elongation at break minimum 200 %. For children’s sandals sold in the U.S., CPSIA Section 108 limits DEHP, DBP, and BBP to 0.1 % each in accessible plastic components; converters should request phthalate-specific documentation from Braskem America for DVR 001A lots used in this segment.

    Calendered EVA foam sheet is produced by mixing DVR 001A in an internal mixer at 110–120 °C, then discharging the batch to a two-roll mill fitted with chilled rolls at 80–90 °C to sheet off at 2.0–3.5 mm thickness before the blowing agent is fully activated. The sheet is then passed through a continuous hot-air oven or press lamination line at 180–200 °C to trigger azodicarbonamide decomposition; the foam expands to 0.12–0.20 g/cm³ and is calibrated in a three-roll stack at 0.5–0.8 MPa nip pressure. Because the recycled fraction contains low levels of ester-based monomers and oxidised particles, calendering release is improved with 0.3–0.5 phr stearic acid and a chilled release roll, but excessive stearic acid above 0.8 phr migrates and reduces adhesion of the waterborne polyurethane lamination applied later. Die-cut foam sheets are laminated to polyester or cotton canvas using a waterborne polyurethane adhesive applied at 30–50 g/m² dry coat weight by a roll coater with a patterned roller. Nip pressure is held at 0.2–0.4 MPa, and the laminate is cured for 24 h at 23 °C and 50 % relative humidity before peel testing. T-peel strength after ISO 11339:2018 is commonly specified above 2.0 N/mm for removable footbeds; if adhesion falls below 1.5 N/mm, corona treatment of 38–42 mN/m surface energy is applied to the foam side.

    Finished footbeds for prolonged skin contact must comply with REACH Annex XVII entry 50 regarding polycyclic aromatic hydrocarbons: benzo[a]pyrene must not exceed 1 mg/kg and the sum of eight restricted PAHs must not exceed 10 mg/kg. Since DVR 001A is derived partly from post-industrial EVA footwear scrap, a batch-specific PAH extraction test before production is considered non-negotiable for EU shipments. Published data for this specific calendered configuration using DVR 001A is limited; converters should qualify each incoming lot with a statistically valid pilot run rather than transferring parameters from virgin EVA sheet lines.

    Crosslinked Block Skiving and the Relationship Between Gel Content and Skive Blade Temperature

    Crosslinked EVA blocks are produced by compression moulding or autoclave expansion, then slit into 0.8–4.0 mm sheets on a horizontal skiving machine. When DVR 001A constitutes 50–70 % of the block compound, the incoming recycled gel content must be measured by ASTM D2765-16 method A before the peroxide cure is specified. If the pre-cure gel fraction exceeds 15 %, the final gel content after 0.6 phr DCP cure can exceed 75 %; at that level the cutting zone temperature rises to 120–140 °C and the skived surface develops fusion tails and irregular thickness. Chilled-air cooling of the blade and a reduced table speed of 0.5–1.0 m/min are used to hold the cutting temperature below 100 °C. The recycled fraction may also contain trace metal particulate from upstream shredding; a 1.0 mm magnetic trap and 0.5 mm stainless steel mesh screen are placed before the internal mixer to protect skiving blades from chattering fractures.

    The product range includes orthotic shells, heel lifts, arch pads, and shoe counters that are assembled into orthopedic footwear or sports shoes. For orthotic applications, ISO 10993-5 cytotoxicity and ISO 10993-10 skin irritation data are frequently requested by device assemblers; DVR 001A is not marketed as a medical-grade material, so the final compound must be tested after all additives and lamination steps are fixed. Published data for DVR 001A in ISO 10993 configurations is limited, and biocompatibility cannot be assumed from generic EVA data. Dimensional tolerance on skived sheet is held at ±0.2 mm; below 0.8 mm, the recycled gel fraction increases the reject rate due to blade deflection and surface pull-out.

    When Post-Industrial EVA Replaces Virgin Copolymer in High-Tear Protective Mat Foaming

    Protective mats, martial-arts flooring, and closed-cell cushioning pads are typically produced at densities from 0.10 g/cm³ to 0.15 g/cm³ with a high tearing strength requirement. DVR 001A is introduced as a partial replacement of 30–50 % of the virgin EVA resin in a blend that may also contain polyolefin elastomer. The compound is mixed in a Banbury internal mixer at 110 °C, dropped at 115 °C, and moved to a two-roll mill at 85–95 °C before azodicarbonamide and dicumyl peroxide are added. The slab preform is cured in a hydraulic press at 160–165 °C and 150 kg/cm²; for parts thicker than 20 mm, the cure cycle uses a slow temperature ramp of 3–4 °C/min to avoid internal scorch. The recycled fraction in DVR 001A can contain metal residues from post-industrial cutting; eddy-current separators and rare-earth magnetic grids of 12,000 gauss are placed upstream of the internal mixer to protect barrel screws and to prevent pinch-point burns during press loading.

    Tear strength is tested after ISO 8067:2018, with a minimum specification of 4–6 N/mm for high-use martial-arts mats measured on 2 mm skived test pieces. Compression set after 50 % deflection for 24 h at 23 °C per ISO 1856:2022 is held below 10 % for landing mats. The recycled content may reduce rebound resilience by 2–5 percentage points compared with the same formulation using virgin EVA; resilience is measured on a DIN 53512 rebound pendulum. The mat surface is textured by mould release paper or engraved steel plate, and final mat products are tested for tear propagation and skin-contact PAH compliance under REACH Annex XVII entry 50. Published data for DVR 001A in high-impact sports mats is limited; the above ranges are starting points for pilot-scale trials rather than certified specifications.

    Solvent-Free Compression Lamination and Shore C Drift in Orthotic Footbeds

    Orthotic footbeds built from a textile top layer, a DVR 001A foam core, and a rubber or TPU bottom layer are assembled by reactive hot-melt compression lamination. The adhesive is a moisture-curing polyurethane applied at 40–60 g/m² with a roll coater at 120–140 °C; open time before pressing is 60–90 s. The stack is pressed at 0.3–0.6 MPa and 50 °C for 30 s, then cold-stabilised at 23 °C for 48 h. The foam core is die-cut from crosslinked sheet at 1.5–2.5 mm thickness, with edge skiving tolerance of ±0.2 mm to prevent visible ridge lines through the top fabric. Because the recycled fraction can exude low-molecular-weight esters and process oils, Shore C values may drift by 2–4 points between demoulding and 7 days of ambient ageing; final hardness is recorded at day 7, not at press time.

    Adhesion durability is evaluated by washing cycles in water at 40 °C for 50 cycles followed by T-peel per ISO 11339:2018; the target is retention above 70 % of the original peel strength. For overseas shipments, the moisture content of the foam core before lamination is held below 0.05 % to prevent bubbling under the hot-melt film. The finished footbed is tested for pH and formaldehyde if it is to be sold in direct skin-contact categories; absent a formal EU Ecolabel claim, standard specifications under REACH Annex XVII entry 50 and CPSIA Section 108 still apply when the foam is used in children’s footwear. Because the recycled fraction in DVR 001A originates from multiple footwear production streams, converters must establish incoming lot-specific Shore C, moisture, and PAH profiles; published data for this exact solvent-free lamination configuration is limited, and process windows should not be transferred from one adhesive grade to another without a statistically valid pilot run.

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    Certification & Compliance
    More Introduction
    WENEW Braskem America DVR 001A is an ethylene-vinyl acetate copolymer grade supplied in pelletized form for foam and footwear manufacturing. The grade carries a recycled content fraction of 60% by mass, classified under ISO 14021:2016 as recycled material from declared pre-consumer and post-consumer sources; the exact split is retained in supplier mass-balance records. The vinyl acetate comonomer content falls within 18–28 wt%, which controls crystallinity, flexibility, gas diffusion, and compatibility with chemical blowing agents. Melt mass-flow rate, tested at 190°C with a 2.16 kg load under ASTM D1238 or ISO 1133-1:2022, is controlled between 1.5 g/10 min and 3.0 g/10 min; this range supports thick-section expansion and thin-wall flow in injection-molded footbeds. Density, determined by ASTM D792, is 0.938–0.947 g/cm³. The material is not supplied with a single hardness specification because final hardness depends on crosslinking density, blowing agent loading, and filler content; common midsole compounds may target Shore A 55–75 after cure, but lot-specific certificates should be used for design. The DVR 001A designation identifies the recycled-content EVA within the Braskem America WENEW circular product line. Its intended processing routes include compression molding, injection molding, sheet extrusion, and hot/cold foam expansion for midsoles, outsoles, sandals, slippers, and protective sports foam.

    What separates DVR 001A from virgin EVA and broad-spec recycled feedstocks?

    Generic virgin EVA feedstocks are sold with tight melt-index tolerance and low gel counts. DVR 001A differs because its recycled content introduces additional sources of variability: residual crosslinked elastomer particles, inorganic fragments from footwear compounds, and variable thermal history. These are managed through feedstock sorting, melt filtration, and blending, but the grade is not a drop-in replacement for virgin EVA in formulations requiring optical clarity or very low gel counts. Compared with broad-spec recycled EVA, DVR 001A is selected specifically for foam cell nucleation, footwear cycle-time requirements, and control of vinyl acetate content. Compared with compounds containing 30% recycled content, DVR 001A increases the circular feedstock share but may require higher stabilizer addition and finer screen filtration to maintain surface quality in expanded sheet. The recycled fraction also shifts the carbonyl index, measurable by Fourier-transform infrared spectroscopy under ASTM D5576, relative to virgin EVA; this index is used in incoming inspection to detect oxidation that reduces melt strength. Batch-to-batch variation in gel count can influence melt viscosity. On production-scale twin-screw lines, changes in screw torque and die pressure between virgin EVA and DVR 001A are expected; if torque variation exceeds 10%, screen pack replacement or feedstock blending is indicated. The material is not intended for high-clarity film, cable jacketing, or food-contact parts unless specific validation is performed. For crosslinked foam manufacturing, DVR 001A is typically compounded with azodicarbonamide-based blowing agents, dicumyl peroxide crosslinking agents, zinc oxide activators, and stearate processing aids. The compounding step on a co-rotating twin-screw extruder with an L/D ratio of 40:1 to 52:1 requires barrel temperatures below the decomposition onset of the blowing agent, commonly 155°C for pure azodicarbonamide but reduced to 135–145°C when activators are present. The grade should be pre-dried at 60–70°C for 2–4 h when sacks have been stored at relative humidity above 60%. The recycled fraction can contain trace thermoplastic degradation products that act as nucleating sites, producing finer cell size at equivalent blowing agent loading compared with virgin EVA; this effect is useful for midsoles but requires stable die pressure to prevent cell coalescence. Injection-molded foam articles are produced with injection pressures in the 80–120 MPa range, while gas counterpressure at 0.5–1.5 MPa is applied to control surface defects. Screen-pack blockage from gel particles is the primary production failure mode; operators monitor pressure rise and replace packs when pressure exceeds 3.5 MPa above baseline. Die steel should be corrosion-resistant because traces of acetic acid can appear at processing temperatures approaching 220°C.

    Melt rheology, foam cell nucleation, and extruder load thresholds

    Melt viscosity and elasticity under processing conditions determine cell nucleation density, cell wall stability, and final foam density. Capillary rheometry under ISO 11443 at 190°C and shear rates from 100 s⁻¹ to 1000 s⁻¹ is used to characterize DVR 001A across the shear regime encountered in extrusion and injection molding. The elongational viscosity, which controls bubble growth resistance, is influenced by the 18–28 wt% vinyl acetate content and by lightly crosslinked recycled particles; these particles can act as high-melt-strength domains that reduce collapse of expanding foam cells. However, the same particles may increase melt pressure at the breaker plate by 5–15% relative to virgin EVA, necessitating screen packs from 40 to 80 mesh depending on gel size distribution. Screens are placed upstream of the die to trap particles larger than 100 µm, preventing surface pinholes in sheet foam lines running at thicknesses of 1–10 mm. In crosslinking foam systems, the cure curve is measured by moving die rheometry under ASTM D5289; DVR 001A formulations are typically adjusted to achieve a scorch time TS2 greater than 1.5 min at molding temperature and a cure time T90 below 8 min for acceptable cycle times. At extruder load thresholds, the specific energy input may vary from virgin EVA due to gel particles; melt pump inlet pressure should be maintained above 2 MPa to avoid cavitation. Mechanical property retention in DVR 001A depends on the ratio of recycled to virgin EVA, the degree of crosslinking, and the presence of crosslinked particles. Tensile strength and elongation of unreinforced plaques can be measured under ASTM D638 or ISO 527-2, and tear strength under ASTM D624 or ISO 34-1. At equivalent vinyl acetate content, the recycled grade may show tensile strength within 10–20 MPa and elongation at break above 500%; these values are formulation-dependent and should not be used as resin specifications. The recycled fraction can reduce low-temperature flexibility, but the effect is minor within footwear service temperatures from -10°C to 40°C. For foam compression set, compounds based on DVR 001A can be formulated to achieve values below 30% under ASTM D395 Method B at 50°C for 6 h, provided that crosslink density is controlled. Hardness, measured by ASTM D2240 or ISO 868, is typically adjusted by modifying filler content and blowing agent ratio rather than by selecting a different EVA base resin.

    When recycled content exceeds 50% in ethylene-vinyl acetate feedstock

    At recycled content levels above 50%, the melt is more sensitive to thermal history and residual contamination than virgin EVA. DVR 001A therefore requires stricter handling limits: melt temperature should be held between 105°C and 125°C in compounding for chemically blown foam to prevent premature blowing agent decomposition, while injection barrels may be set to 110–145°C with nozzle temperatures not exceeding 160°C. Above 220°C, vinyl acetate degradation releases acetic acid; in closed molding areas this promotes corrosion of unplated steel tool surfaces and can reduce crosslinking efficiency of peroxide cure systems. The recycled fraction can contain trace zinc, calcium, or silica residues from footwear compounds, which may catalyze uneven decomposition of azodicarbonamide; therefore the activator package is adjusted on a lot basis after evaluating blowing agent gas yield by thermogravimetric analysis under ASTM D3850. When combining DVR 001A with other polyolefins, compatibility should be assessed by differential scanning calorimetry under ASTM D3418 because the effective vinyl acetate content may shift the crystallization peak below 75°C and affect demolding shrinkage. Storage should be in sealed containers at ambient temperatures below 30°C and relative humidity below 60%; opened material should be re-dried before processing if exposure exceeds 4 h. Quality control for DVR 001A is based on melt flow rate, vinyl acetate content, density, gel count, and retained recycled content. Because the feedstock includes recycled EVA from foam and footwear scrap, the certificate of analysis should be reviewed for lot-specific melt index and gel count, not only product data sheet nominal values. Recycled content validation is conducted through supplier mass balance under ISO 14021:2016 and, where applicable, ISCC PLUS chain-of-custody certification. Regulatory conformance for the final article is assessed against EU REACH Regulation (EC) No 1907/2006 and Directive 2011/65/EU (RoHS); DVR 001A is not granted direct food-contact status under 21 CFR 177.1350 unless specifically confirmed by the supplier for a defined application and recycling stream. For inventory control, the recycled share is tracked by lot; this prevents commingling with virgin EVA and supports downstream claims under ISO 14021.
    Characterization and compliance matrix for WENEW Braskem America DVR 001A
    ParameterTest method or basisControl range or reference
    Recycled contentISO 14021:2016 / mass balance60% by mass
    Melt mass-flow rateASTM D1238 / ISO 1133-1:20221.5–3.0 g/10 min at 190°C, 2.16 kg
    DensityASTM D7920.938–0.947 g/cm³
    Vinyl acetate contentASTM D5594 / internal18–28 wt%
    Melting peakASTM D3418 / ISO 1135775–95°C
    Regulatory boundary21 CFR 177.1350Not granted without supplier confirmation
    Life cycle inventory calculations for recycled EVA generally follow ISO 14040 and ISO 14044, with cut-off or mass-allocation rules documented in supplier case studies. The carbon footprint reduction attributable to the 60% recycled content is not a fixed percentage because it depends on collection radius, scrap yield, and electricity grid; published data for this specific configuration is limited. Downstream converters should request the supplier’s lifecycle assessment report and allocation method before making comparative environmental claims under ISO 14025 or ISO 14067.