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Anhui Liwei Chemical Co., Limited.

Elvax 3170 EVA Copolymer Resin,Photovoltaic Grade

    • Product Name: Elvax 3170 EVA Copolymer Resin,Photovoltaic 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 423546
    Vinyl Acetate Content 18%
    Melt Flow Rate 8 g/10 min (190°C/2.16 kg)
    Density 0.940 g/cm³
    Melting Point 90°C
    Vicat Softening Point 81°C
    Tensile Strength 18 MPa
    Elongation At Break 750%
    Shore A Hardness 90
    Refractive Index 1.49
    Volume Resistivity 1 × 10¹⁴ Ω·cm
    Water Absorption 0.1%
    Glass Transition Temperature -40°C

    As an accredited Elvax 3170 EVA Copolymer Resin,Photovoltaic Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Elvax 3170 photovoltaic EVA resin pellets are supplied in 25 kg sealed moisture-resistant bags, ensuring clean handling and protection.
    Container Loading (20′ FCL) 20′ FCL loading of Elvax 3170 EVA Resin: palletized, moisture-protected cartons, stowed securely to prevent shifting during transit.
    Shipping Elvax 3170 EVA Copolymer Resin (Photovoltaic Grade) ships as non-hazardous pellets in moisture-barrier bags, sealed within sturdy woven or fiber drums. Store away from heat, ignition sources, and direct sunlight. Ensure dry conditions during transit to prevent clumping or degradation. Standard freight methods apply; keep containers upright.
    Storage Store Elvax 3170 in a cool, dry, well-ventilated area below 30°C (86°F), away from direct sunlight, heat, and ignition sources. Keep in original sealed packaging to prevent moisture absorption, which can degrade performance. Avoid high humidity and extreme temperature fluctuations, and use within recommended shelf life to maintain photovoltaic-grade quality.
    Shelf Life Shelf life is typically two years from shipment date when stored unopened in a cool, dry place away from heat and direct sunlight.
    Application of Elvax 3170 EVA Copolymer Resin,Photovoltaic Grade

    Photovoltaic-grade ethylene-vinyl acetate copolymer resin containing 28 wt% vinyl acetate comonomer and a melt flow rate of 6.0 g/10 min per ASTM D1238 at 190°C/2.16 kg is first converted into extrusion-grade encapsulant film for monofacial glass/backsheet crystalline silicon modules. Compounding is generally performed by feeding resin pellets together with a pre-dispersed additive masterbatch into a twin-screw extruder with L/D of 30:1 to 44:1 and barrel temperatures controlled between 65°C and 90°C; die temperatures are limited to 85–95°C because the peroxide initiator, typically tert-butylperoxy-2-ethylhexyl carbonate, begins to decompose measurably above 110°C and the cast film must retain active peroxide for the subsequent module lamination step. The film is produced at 0.45–0.76 mm nominal thickness and chilled on a textured roll to reduce blocking. For this formulation, silane coupling agent, vinyltrimethoxysilane or methacryloxypropyltrimethoxysilane, is added at 0.3–0.6 phr to promote wet adhesion to soda-lime glass and conventional backsheet. Lamination takes place in a vacuum diaphragm laminator with heated platens at 145–155°C; the recommended vacuum pump-down is 5–7 min to remove air from the cell and ribbon interface, followed by diaphragm compression at 0.1–0.2 MPa and cure time of 12–20 min. The resulting encapsulant gel content is controlled at 75–90% as measured by ASTM D2765-16, with T-peel adhesion to glass normally specified above 40 N/cm per ASTM D1876-15 after lamination and after 1000 h damp heat at 85°C/85% RH according to IEC 61215-1:2021. Terminal products are conventional framed glass/backsheet modules that require no additional edge encapsulation beyond the backsheet lamination seal, but film moisture content before lamination must be maintained below 0.03%; pre-drying at 70°C for 4 h is required whenever storage relative humidity exceeds 60%.

    Why Does CdTe and CIGS Module Lamination Demand a Moisture Edge Seal Before EVA Encapsulation Is Viable?

    When the same photovoltaic-grade EVA is evaluated for thin-film CdTe or CIGS devices, the encapsulated cell stack is not tolerant of acetic acid generation from vinyl acetate hydrolysis. The lamination formulation is modified by introducing acid-scavenging zinc oxide or hydrotalcite masterbatch at 0.2–0.4 phr, and the peroxide level is reduced to keep gel content between 70% and 85% because high crosslink density reduces stress-relaxation capacity around the brittle transparent conductive oxide layer. Amine-based adhesion promoters are excluded because basic nitrogen species interfere with peroxide decomposition and can leave low gel-content regions at the encapsulant surface. Process temperatures are lowered to 130–145°C and cure time extended to 15–20 min so that the peroxide decomposition profile remains in the safe range below the degradation onset of cadmium telluride or copper indium gallium diselenide junction interfaces. Vacuum laminators for thin-film modules require a two-step pressure profile: 300 s at 50 kPa to remove volatile additives and residual moisture, then 0.1 MPa diaphragm pressure for bonding. Because EVA does not provide a sufficient moisture barrier, the module perimeter must include desiccant-loaded edge tape or butyl edge seal with water vapor transmission rate below 0.01 g/m²·day when tested at 38°C/90% RH; without this, damp heat at 85°C/85% RH per IEC 61215-1:2021 may cause acetic acid accumulation at the TCO interface and series-resistance drift. Terminal thin-film modules using EVA are therefore limited to configurations with fully encapsulated edge seals, and published data for long-term CIGS encapsulation with standard EVA remains limited; polyolefin elastomer or ionomer films are frequently substituted when moisture exclusion is the dominant requirement.

    Extending Elvax 3170 into glass-glass bifacial module construction shifts the critical quality variable from rear backsheet adhesion to optical uniformity and gel content balance between the front and rear encapsulant plies. In this architecture, two plies of 0.45–0.76 mm cast film are laid up on either side of the cell string, and the rear side is laminated against heat-tempered or heat-strengthened low-iron glass instead of a composite backsheet. Because the rear side is optically active, the film must retain luminous transmittance above 90% after lamination as measured by integrating-sphere spectrophotometry per ASTM E903, and the additive package replaces light-scattering nucleants with clarifying antioxidants at 0.05–0.15 phr. The lamination program uses a slow ramp from 120°C to 150°C over 8–12 min followed by a cure plateau of 15–22 min; this prevents the glass-to-glass edge void defects that occur when the diaphragm reaches full pressure before the EVA melt front has closed around the cell edges. Diaphragm pressure is staged at 0.06 MPa during the first 5 min, then raised to 0.15 MPa. Cure performance is checked by differential scanning calorimetry residual enthalpy and by gel content per ASTM D2765-16, with front and rear samples required to fall within ±5% absolute gel content of the target 78–92%. Terminal products are glass-glass bifacial modules qualified under IEC 61215-1:2021 and IEC 61730-2:2016; rear-side UV exposure makes UV absorber addition at 0.1–0.3 wt% necessary to prevent ethylene-vinyl acetate photodegradation, but excessive UV absorber must be avoided because it reduces rear-side conversion efficiency in the 300–400 nm band.

    Module architectureFilm thicknessLamination temperatureCure timeTarget gel contentGoverning test method
    Monofacial glass/backsheet c-Si0.45–0.76 mm145–155°C12–20 min75–90%ASTM D2765-16
    CdTe/CIGS with edge seal0.45–0.60 mm130–145°C15–20 min70–85%ASTM D2765-16
    Glass-glass bifacial0.45–0.76 mm per side120–150°C ramp15–22 min plateau78–92%ASTM D2765-16
    BIPV autoclave0.76–1.52 mm total135–145°C30–60 min80–95%ASTM D2765-16
    Flexible ETFE/polymer backsheet0.30–0.45 mm120–130°C18–25 min70–80%ASTM D2765-16
    TOPCon / heterojunction0.45–0.76 mm140–150°C12–16 min80–90%ASTM D2765-16

    Building-code impact resistance and curved glass lamination with EVA encapsulant in BIPV façades

    Building-integrated photovoltaic modules in façade and skylight applications use Elvax 3170 encapsulant film not as a single 0.45 mm layer but as multiple plies, typically 0.76–1.52 mm total thickness, to achieve laminated safety-glass behavior under impact and post-breakage retention requirements. The formulation for BIPV includes a silane adhesion promoter at the upper end of the normal range, 0.4–0.6 phr, because peel strength to heat-treated glass and to the rear ceramic frit band must remain above 45 N/cm after simulated weathering. Lamination is carried out in a vacuum-bag autoclave rather than a flat-plate laminator when the glass is curved or oversized; the autoclave profile consists of heating to 135–145°C under 0.8–1.0 MPa nitrogen pressure for 30–60 min, which drives dissolved air back into solution and suppresses bubble formation at the concave glass surface. The peroxide masterbatch is adjusted to a lower initiator loading so that the extended high-pressure cycle produces gel content of 80–95% and a residual peroxide level below 5% of the original loading to prevent post-lamination outgassing inside the building cavity. The encapsulant must remain electrically insulating under wet conditions; insulation resistance is verified per IEC 61215-1:2021 and IEC 61730-2:2016, while the glass structure itself is assessed according to the applicable safety-glass classification in the installation region. Terminal products include curtain-wall modules, spandrel panels, and overhead glazing units in which the EVA layer contributes to load transfer and laminate ductility, but the lower shear modulus of EVA at temperatures above 60°C requires finite-element verification of creep deflection for overhead spans.

    StandardProperty or testRelevant architecture
    IEC 61215-1:2021Damp heat, thermal cycling, insulation resistanceAll crystalline-silicon and thin-film modules
    IEC 61730-2:2016Module safety qualificationBuilding-applied and utility modules
    IEC TS 62804-1:2015Potential-induced degradationTOPCon, heterojunction, glass-glass
    IEC 62715Flexible photovoltaic module qualificationETFE/polymer backsheet lightweight modules
    ASTM D2765-16Gel content by solvent extractionAll crosslinked EVA encapsulant films
    ASTM D1876-15T-peel adhesion to glass/backsheetGlass/backsheet and BIPV modules
    ASTM D1238-20Melt flow rateIncoming resin lot release
    ISO 1133-1:2022Melt mass-flow rateIncoming resin lot release alternative

    In lightweight modules using ETFE front sheets and polymer backsheets, Elvax 3170 is processed as a 0.30–0.45 mm cast film at barrel temperatures not exceeding 90°C and die temperatures of 85–95°C to preserve the peroxide activity required for low-temperature lamination. Because the ETFE front sheet does not tolerate the 145–155°C conventional lamination window, the film is designed to cure at 120–130°C with a cure time of 18–25 min. The lower cure temperature demands a faster peroxide initiation system, and the gel content achievable is limited to 70–80% rather than the 75–90% typical of glass-based modules. Prior to lamination, the ETFE surface is corona-treated to a wetting tension of 48–52 dyn/cm and primed with an aminosilane or acrylic primer; without this surface activation, EVA adhesion to fluoropolymer remains below 20 N/cm and delamination occurs after 500 h of damp heat at 85°C/85% RH per IEC 61215-1:2021. The terminal product is a semi-flexible module without glass, but the operational boundary of this EVA in flexible service is significant: the copolymer exhibits pronounced creep and softening above 50–60°C as measured by dynamic mechanical analysis per ASTM D4065, and flexural cycling under IEC 62715 or internal manufacturer protocols can exceed the strain capacity of the crosslinked vinyl acetate network. Consequently, flexible-module designs using this resin are ordinarily restricted to low-flex, fixed-radius installations, and polyolefin elastomer films are often substituted when high cycle fatigue or hot-spot temperatures above 65°C are specified.

    If passivated-contact cell stacks are encapsulated, acetic acid generation and PID susceptibility override the default lamination recipe

    The selection of Elvax 3170 for TOPCon and silicon heterojunction cell architectures is governed less by lamination throughput than by hydrolytic stability of the vinyl acetate comonomer. Under damp-heat exposure, vinyl acetate hydrolysis releases acetic acid, which corrodes the transparent conductive oxide and passivation stacks associated with high-efficiency n-type cells; for this reason, the encapsulant formulation is modified with acid-scavenging hydrotalcite at 0.2–0.5 phr and zinc oxide at 0.1–0.3 phr, while film moisture is held below 0.02% before lamination by vacuum drying at 70°C. Lamination temperatures are maintained in the narrower 140–150°C band with cure times of 12–16 min, and gel content is controlled to 80–90% per ASTM D2765-16 so that the encapsulant network restricts ionic transport without becoming so rigid that it transfers thermomechanical stress to thin passivation layers. The terminal module is tested not only for standard damp heat according to IEC 61215-1:2021 but also for potential-induced degradation under IEC TS 62804-1:2015 at system voltages of 1000 V or 1500 V, with leakage current limits defined by the module manufacturer. EVA remains qualified only for designs that pass the specified extended damp-heat and PID protocol; where the cell supplier specifies maximum acetic acid concentration at the cell surface or where the module warranty demands 2000 h damp-heat performance, published process windows for standard EVA are limited and polyolefin encapsulants or hybrid EVA-POE structures are typically required. This constraint is not a resin defect but a boundary condition for vinyl acetate chemistry under photovoltaic service.

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    Certification & Compliance
    More Introduction

    DuPont™ Elvax® 3170 EVA copolymer resin is an ethylene-vinyl acetate feedstock controlled for photovoltaic encapsulant film manufacture. The nominal vinyl acetate comonomer content is 33 wt% when determined by Fourier-transform infrared spectroscopy per ASTM D5594 or ISO 8985. Melt mass-flow rate is 15 g/10 min as measured by ISO 1133-1:2022 at 190 °C under a 2.16 kg load. Density is 0.96 g/cm³ per ASTM D792. Differential scanning calorimetry in accordance with ISO 11357-3 produces a peak melting temperature of approximately 62 °C. Vicat softening temperature is approximately 36 °C when tested per ASTM D1525. These are typical property values, not contractual specification limits.

    The high vinyl acetate content increases the amorphous phase fraction relative to EVA resins with lower comonomer levels. This shift lowers crystallinity and melting point while improving light transmission and interfacial adhesion to glass and polyvinyl fluoride backsheet. It also increases moisture uptake and compounded sheet tack. The resin is therefore formulated with anti-blocking agents, processing stabilizers, and controlled cooling conditions to permit roll-to-roll handling after slot-die extrusion.

    The grade is intended for compounding with peroxide crosslinking agents, silane coupling agents, ultraviolet absorbers, and hindered amine light stabilizers before film extrusion. Because photovoltaic encapsulant performance depends on gel content and optical uniformity, lot selection emphasizes low gel count, controlled ionic residue, and consistent vinyl acetate distribution. Particulate gels in the raw resin are minimized to limit pinhole defects in thin encapsulant sheet. Sodium and chloride residues are controlled because they influence volume resistivity and potential-induced degradation. Published numeric gel-count specifications for this specific configuration are limited; incoming resin is typically released against melt-flow and compositional tolerances rather than a universal gel metric.

    What Processing Window Governs Slot-Die Extrusion of Photovoltaic Encapsulant Sheet?

    On a cast film line equipped with a single-screw extruder with 30:1 L/D and a barrier screw with Maddock mixing sections, the feed throat is maintained below 50 °C to prevent pellet bridging. Barrel zone set points are typically distributed between 80 °C and 110 °C. Melt temperature at the die inlet is limited to 115–120 °C when a peroxide masterbatch is present. This upper limit is imposed because common peroxide initiators used in EVA encapsulation, such as tert-butyl peroxy-2-ethylhexyl carbonate with a 10 h half-life at 97 °C, can initiate premature crosslinking in hot spots. Screw speed is adjusted to hold melt pressure before the screen pack at 8–15 MPa; pressure fluctuation greater than ±1 MPa frequently indicates gel accumulation on the screens or inconsistent feed.

    If the resin has been exposed to relative humidity above 60%, pre-drying in a desiccant dryer at 50–60 °C for 4 h is required to reduce moisture below 0.05 wt%. Residual moisture hydrolyzes silane coupling agents during compounding and generates microvoids in the cast sheet. A screen stack of 60/80/100 mesh is typical; optional gear pump delivery stabilizes die pressure but increases shear heating, so the pump inlet melt temperature is monitored. The slot-die gap is commonly held at 0.8–1.2 mm to produce sheet in the 0.40–0.60 mm thickness range. Draw ratio is kept below 2:1 to limit residual stress and thickness variation. Chill rolls are held at 10–20 °C. Lower chill roll temperatures reduce blocking but can condense moisture; higher temperatures increase tack and may cause roll blocking in storage. Edge trim and recycled film are reincorporated at 5–15 wt%; higher recycle fractions can raise gel count and increase optical haze.

    The melt is shear-thinning; increasing screw speed reduces apparent viscosity but raises melt temperature. Therefore, shear heating rather than barrel set points often defines the practical maximum output. Processors monitor specific energy input and keep it below approximately 0.12 kWh/kg when peroxide-containing masterbatch is present. If specific energy exceeds this value, the melt temperature can enter the peroxide decomposition region and produce localized crosslink gels that appear as fisheyes in the cured encapsulant.

    Vacuum Lamination Cure Kinetics and Long-Term Module Qualification

    The compounded EVA sheet is laminated between glass, cell strings, and backsheet in a vacuum laminator. A typical cure profile uses heated platens at 150 °C, evacuation at 50–100 Pa for 5 min, followed by pressing at 0.08–0.10 MPa for 12–15 min. The peroxide decomposes to form radicals that abstract hydrogen from the ethylene sequences of the EVA backbone, producing crosslinks. Gel content after lamination is commonly specified between 75% and 85% when measured by solvent extraction per ASTM D2765. Gel content below 70% is associated with creep and cell movement during field service; gel content above 90% can reduce elongation and increase brittleness.

    Silane coupling agents, typically vinyltrimethoxysilane at 0.3–0.5 phr, are added to promote adhesion to glass and cell surfaces. The alkoxy groups react with surface silanols, while the vinyl group participates in the peroxide cure. Peel adhesion to glass after lamination is often specified by module manufacturers at not less than 40 N/cm when measured by a 180° peel test. Ultraviolet absorber packages commonly include benzotriazole at 0.1–0.3 phr and hindered amine light stabilizer at 0.1–0.2 phr to control yellowing under xenon-arc weathering. Luminous transmittance of cured 0.45 mm sheet is typically greater than 91% per ASTM D1003; yellowness index is typically below 1.5 per ASTM E313.

    Bubble formation during lamination is a primary failure mode. If vacuum evacuation is too short or if moisture in the sheet exceeds 0.05 wt%, bubbles nucleate at cell gridlines and busbar edges. These bubbles reduce optical coupling and can delaminate under thermal cycling. Press pressure must be high enough to flow the melt into the cell spacing but low enough to avoid squeezing the melt away from cell edges. A two-step pressure ramp from 0.03 MPa to 0.10 MPa is used to balance fill and squeeze-out.

    For module qualification, the encapsulated laminate is subjected to damp heat at 85 °C and 85% RH for 1000 h and thermal cycling between -40 °C and 85 °C for 200 cycles under IEC 61215-1:2021. The encapsulant must maintain adhesion and optical clarity through these exposures. Acetic acid generated by hydrolysis of vinyl acetate units during damp heat can corrode busbars and gridlines; therefore, acid scavengers and low-acid resin variants are used. Volume resistivity of cured encapsulant is typically specified above 1×1014 Ω·cm per IEC 60093 to limit potential-induced degradation. Amine-based processing aids or colorants should be avoided because they can scavenge radicals, discolor the sheet, and destabilize the silane coupling reaction.

    Referenced test methods and qualification standards for photovoltaic-grade EVA encapsulant
    StandardParameter or requirement
    ISO 1133-1:2022Melt mass-flow rate at 190 °C, 2.16 kg
    ASTM D5594 / ISO 8985Vinyl acetate comonomer content
    ASTM D792Density
    ISO 11357-3Peak melting temperature by DSC
    ASTM D2765Gel content after peroxide cure
    ASTM D1003Luminous transmittance of cured sheet
    IEC 61215-1:2021Photovoltaic module qualification sequence

    Incoming resin quality control for photovoltaic encapsulant lines typically includes verification of vinyl acetate content by FTIR within ±1 wt% of nominal and melt mass-flow rate within a lot-to-lot control window of approximately ±2 g/10 min. A shift of 1 wt% vinyl acetate alters the peak melting temperature and peel adhesion behavior; therefore, blending of lots with divergent VA content is avoided unless pilot-scale lamination confirms equivalent cure and adhesion. Film thickness is measured by beta gauge or laser profilometry across the web. Thickness variation is typically limited to ±5% of nominal because low spots can leave cells unencapsulated and high spots can increase lamination cycle time.

    Automated optical inspection systems classify gels and black specks in the cast sheet. Acceptable gel levels are set by module manufacturers and are not universally standardized; published data for this specific configuration is limited. The resin should not be dry-blended with ionomers, acid-modified ethylene copolymers, or amine-containing masterbatches. Such contamination shifts pH, creates optical haze, and can interfere with peroxide cure or silane adhesion. Metal detectors with ferrous sensitivity of 1.0 mm are installed after granulation of recycled edge trim and before the feed hopper to protect the extruder screw from metal fines.

    Storage of bulk pellets is recommended below 25 °C and below 60% RH to limit moisture uptake and blocking. If silo storage exceeds 30 days, re-verification of moisture content and melt-flow stability is common practice.

    When an 18 wt% or 28 wt% Vinyl Acetate Grade Is Substituted in Photovoltaic Encapsulant Lines

    Substitution of a lower-vinyl-acetate EVA into a photovoltaic encapsulant line changes the melting, adhesion, and optical profile. A 28 wt% VA grade with melt flow of 6 g/10 min melts at approximately 73 °C; its lower melt flow increases head pressure and shear heating at equal screw speed, so barrel temperatures may need to be reduced by 5–10 °C to hold the die-inlet melt below the peroxide half-life threshold. Its lower VA content raises crystallinity and reduces equilibrium moisture uptake but also lowers glass and backsheet adhesion after cure. An 18 wt% VA grade melts near 85 °C and exhibits further reduced adhesion and transparency below 400 nm, making it unsuitable for most glass-glass photovoltaic laminates without additional adhesion promoters.

    Compared with a high-flow 33 wt% VA grade with melt flow of 43 g/10 min, Elvax 3170 has greater melt strength and improved gauge stability in cast film, but it develops higher head pressure and may require a wider die gap for thin-gauge encapsulation. The melt flow of 15 g/10 min balances extrusion output, web stability, and rapid flow into the cell gaps during lamination. In multi-layer encapsulant structures, Elvax 3170 is often placed adjacent to the glass to maximize adhesion, while a lower-flow or higher-melting EVA or polyolefin elastomer forms the backside layer to reduce blocking and improve dimensional stability.

    Typical comparative profile of EVA resin grades used in film extrusion
    ParameterElvax 3170 photovoltaic grade28 wt% VA EVA18 wt% VA EVA
    Vinyl acetate content (wt%)332818
    Melt mass-flow rate (g/10 min at 190 °C, 2.16 kg)1568
    Density (g/cm³)0.960.950.94
    Peak melting temperature (°C)627385
    Vicat softening temperature (°C)364560

    The choice of photovoltaic-grade resin also affects lamination cycle time. Lower-melting grades such as Elvax 3170 flow and wet the cell interconnects at lower platen temperature, but they require controlled lamination pressure to avoid bubble entrapment. If platen temperature exceeds 155 °C, volatile additives or moisture can form bubbles before the cure network sets. Conversely, if platen temperature is below 140 °C, the peroxide half-life extends and full gel content may not be reached within the standard 15 min cycle. These boundaries define the operational window for encapsulant production and module assembly.