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TEREZ NatureGran PV 6930 Impact Modified Injection Molding Polylactic Acid

    • Product Name: TEREZ NatureGran PV 6930 Impact Modified Injection Molding Polylactic Acid
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 358936
    Base Polymer Polylactic Acid (PLA), Impact Modified
    Density 1.24 g/cm³
    Melt Volume Flow Rate Mvr 190 C 2 16 Kg 15 cm³/10 min
    Tensile Modulus 2200 MPa
    Tensile Strength 45 MPa
    Elongation At Break 15%
    Flexural Modulus 2500 MPa
    Flexural Strength 70 MPa
    Charpy Notched Impact Strength 23 C 10 kJ/m²
    Charpy Unnotched Impact Strength 23 C 40 kJ/m²
    Heat Deflection Temperature 0 45 Mpa 85°C
    Vicat Softening Temperature 60°C
    Glass Transition Temperature 60°C
    Melting Temperature 150-160°C
    Injection Molding Temperature 190-210°C
    Mold Temperature 20-40°C
    Drying Temperature 80°C
    Drying Time 4 h

    As an accredited TEREZ NatureGran PV 6930 Impact Modified Injection Molding Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied in 25 kg polyethylene-lined paper bags, palletized and shrink-wrapped; store dry in original sealed packaging.
    Container Loading (20′ FCL) Standard 20′ FCL container loading for TEREZ NatureGran PV 6930 Impact Modified Injection Molding Polylactic Acid: palletized, dry, secure stowage.
    Shipping TEREZ NatureGran PV 6930 is shipped as non-hazardous solid pellets in moisture-barrier bags, lined fiber drums, or octabins on pallets. Store and transport cool, dry, and ventilated, away from direct sunlight, heat, moisture, and strong oxidizers. Follow local transport regulations and prevent package damage.
    Storage Store TEREZ NatureGran PV 6930 in tightly sealed original packaging in a cool, dry, well-ventilated area. Protect from moisture, direct sunlight, heat, and ignition sources. Recommended storage is below 30°C with low humidity. Keep away from incompatible substances, food, drink, and animal feed. Do not store outdoors or near water. Observe shelf life using first-in, first-out.
    Shelf Life Shelf life is approximately 12 months when stored dry, below 25°C, in sealed original packaging; avoid moisture and direct sunlight.
    Application of TEREZ NatureGran PV 6930 Impact Modified Injection Molding Polylactic Acid
    On high-cavitation stack moulds running 32–64 cavities, the dominant failure mechanism in TEREZ NatureGran PV 6930 Impact Modified Injection Molding Polylactic Acid cutlery is crack initiation at the root of serrations and at the gate vestige ring, not gross handle breakage. The grade is processed as the neat resin at 100 wt%; a PLA-carrier color masterbatch is incorporated at 2–4 wt%, and a fatty acid ester lubricant is added at 0.1–0.2 wt% to reduce ejection friction on multi-cavity tools. Pre-drying in a desiccant wheel dryer at 80 °C for 4 h to residual moisture below 250 ppm is mandatory; the dryer dew point must remain below -40 °C. Barrel profiles are set at 195–210 °C with a nozzle temperature of 205 °C; mold temperature is maintained at 25–35 °C because higher settings extend cooling time without measurable reduction in residual stress. Injection speed is 80–120 mm/s, hold pressure 600–900 bar, and cooling time 8–12 s. In-line regrind of sprues, runners, and rejected parts is limited to 15 wt%; above 20 wt%, notched Izod impact tested according to ISO 180:2019 shows a progressive decline, and visible flow lines appear on serrations, though published data for PV 6930 above 20 wt% is limited. Routine quality control also uses ISO 527-2:2012 tensile testing; a deviation greater than 15% from the virgin baseline indicates processing-induced molecular degradation. The relevant compliance framework includes EU Regulation (EU) No 10/2011 for cold and ambient aqueous contact, with migration testing in simulant A (10% ethanol) at 40 °C for 10 days; US FDA clearance is supplier-specific through a Food Contact Notification for the base PLA, and the converter must verify the condition of use. Compostability claims are governed by EN 13432:2000, requiring ≥90% biodegradation within 180 days and disintegration after 12 weeks. Terminal products are disposable spoons, forks, knives, sporks, and beverage stirrers; these articles are not intended for hot-food contact above 50 °C.

    Why Does Gate Protrusion Generate Stress Concentrations in Cold-Fill Dairy Cups?

    A recurring defect in cold-fill dairy pot production is a radial crack that runs through the gate land or along the sidewall weld line after filling and lid application. The crack path is governed by gate protrusion height: when the vestige exceeds 0.1 mm, the projection acts as a bending fulcrum during automated stacking, and the resulting stress concentration is sufficient to initiate cracking at the gate edge. For this application, PV 6930 is formulated at 96–98 wt% with a food-contact titanium dioxide white masterbatch at 1.5–3 wt% and a slip/antiblock system at 0.05–0.2 wt%; the masterbatch carrier and additives must fall within the same EU Regulation (EU) No 10/2011 migration envelope as the base resin. With neutral dairy desserts at pH ≥ 4.5, overall migration testing under EN 1186-1:2002 uses simulant A (10% ethanol) at 40 °C for 10 days; acidic fermented dairy products require simulant B (3% acetic acid) under the same time–temperature conditions. Thin-wall injection moulding is performed in stack moulds with valve-gated hot runners, wall thickness between 0.7 mm and 1.0 mm, injection speed 180–250 mm/s, mold temperature 20–40 °C, and cooling time 6–10 s. The operational window is narrow: below 20 °C mold temperature, sidewall flow marks and surface matting appear; above 40 °C, cycle time rises and differential shrinkage produces rim ovality. Terminal products include 120–250 ml portion cups, 500 ml dessert beakers, 150–200 g cold-fill dairy pots, and snap-on lids for refrigerated storage; hot-fill above 50 °C is outside the acceptable use range because of heat distortion.When PV 6930 is moulded into thick-walled cosmetic jars, the critical processing variable shifts from flow length to pack-and-weld line integrity. The front face of a 2–4 mm jar base tends to form sink marks unless hold pressure and cooling time are set specifically for the deeper rib intersections; the gate is often located beneath the base with a reverse-taper nozzle shut-off to prevent drool and gate stringing on polished surfaces. The formulation for cosmetic packaging is 98–99 wt% PV 6930, 0.5–1.5 wt% pearlescent or mineral pigment masterbatch, and 0.1 wt% processing stabilizer. Accelerated packaging-compatibility assessment is conducted at 45 °C and 75% RH for 4 weeks, followed by torque-retention and wall-integrity inspection; no direct food-contact migration test is applicable, but REACH Regulation (EC) No 1907/2006 Annex XVII restricts cadmium, lead, and phthalates in the colorant package, and California Proposition 65 documentation is required for listed heavy metals. Production on a reciprocating screw injection machine with a polished mold surface uses barrel temperatures of 200–215 °C, mold temperature 20–35 °C, injection speed 30–50 mm/s for gate-initiated flow, and cooling time 15–20 s because of the thicker cross-section. Ejection-induced micro-splitting at thread runouts is controlled by limiting undercut depth and by using uniform cooling near the interrupted thread. Terminal products are screw-cap jars, compact containers, caps with interrupted threads, and deodorant stick barrels.

    Cyclic Snap-Fit Deformation in Children’s Construction Sets

    Children's construction sets produce a specific failure mode that is not captured by a single Izod value: repeated snap-fit insertion and extraction cycles generate flexural fatigue at the base of snap-fit lugs, leading to stress whitening and eventual lug fracture. In this application, PV 6930 is used at 97–99 wt% with 1–3 wt% high-tint masterbatch; external lubricant is kept below 0.05 wt% because larger amounts reduce snap-fit friction and can allow assembly pull-out. The safety framework is EN 71-3:2019+A1:2021 for migration of 19 elements, together with Toy Safety Directive 2009/48/EC; for the United States, ASTM F963-23 and applicable consumer product safety rules apply. Moulding uses melt temperatures of 190–205 °C, mold temperature 30–50 °C, injection speed 60–100 mm/s, and cooling time 10–14 s for 2–3 mm wall sections. The higher mold temperature reduces residual stress at the base of snap-fit lugs, but it also increases cycle time by approximately 3–5 s compared with the cutlery process. Regrind above 10 wt% is not recommended for colored sets because multiple heat histories produce visible swirl and variable snap-fit retention; published data for PV 6930 in accelerated cyclic snap-fit testing is limited. Terminal products include construction blocks, toy vehicle chassis, figurines, and assembly puzzles.
    Table 1: Cross-scenario process-boundary reference for PV 6930
    ApplicationCritical control pointAcceptable rangeOutside-window result
    CutleryIn-line regrind content≤15 wt%Notched Izod decline and flow lines above 20 wt%
    Cold-fill dairy cupsMould temperature20–40 °CBelow 20 °C surface matting; above 40 °C rim ovality
    Cosmetic jarsCooling time at 2–4 mm wall15–20 sBelow 15 s sink marks at rib intersections
    Construction setsRegrind content≤10 wt%Snap-fit retention variability and swirl
    Electronic accessory housingsInjection speed at 0.8–1.2 mm ribs≤150 mm/sMelt fracture at rib entrance
    Greenhouse plant clipsResidual moisture before moulding<250 ppmHydrolysis in 60 °C/90% RH exposure
    For desktop electronic accessory housings, the design limit is not stiffness but dimensional tolerance retention at room temperature and repeated insertion of accessory tabs. PV 6930 is processed at 98–99 wt% with 1–2 wt% antistatic masterbatch where dust attraction is a concern; the antistatic package must be selected for compatibility with PLA and must not cause surface migration that could affect laser marking. The applicable standard for non-load-bearing indoor enclosures is UL 94 HB at 1.6 mm thickness, paired with IEC 62368-1:2023 for information equipment accessories where the product is not used as an enclosure requiring a fire-resistance rating. RoHS Directive 2011/65/EU applies to restricted substances in electrical equipment components. Moulding conditions include melt temperature 195–210 °C, mold temperature 25–35 °C, screw back pressure 5–10 bar, and injection speed limited to ≤150 mm/s for ribs of 0.8–1.2 mm thickness; above this speed, melt fracture appears at the rib entrance. Terminal products are cable management clips, electronic pen barrels, battery covers, and calculator housings. PV 6930 is not recommended for enclosures requiring UL 94 V-2 or higher, or for continuous service above 50 °C.

    Plant Clips in Cyclic Greenhouse Humidity

    Greenhouse installation of injection-moulded plant clips exposes the material to repeated condensation, fertilizer salts, and temperature cycles from 5 °C to 40 °C, making hydrolysis the dominant aging mechanism rather than UV degradation alone. For this non-food-contact application, PV 6930 is processed at 98–99 wt% with 0.5–1.5 wt% carbon black or earth-tone masterbatch; hygroscopic bio-fillers are deliberately excluded because they accelerate chain scission in humid storage. The applicable standard is EN 13432:2000, with heavy metal limits under REACH Annex XVII; the material is intended for industrial composting, not soil burial, because soil temperatures are too low for certified disintegration. Moulding uses melt temperature 195–205 °C, mold temperature 25–30 °C, and cooling time 8–12 s for clip arms of 1.5–2.0 mm. The gate is placed away from the flexing arm to prevent brittle molecular orientation at the hinge point. In accelerated humid-aging at 60 °C and 90% RH for 240 h, impact-modified PLA exhibits severe hydrolysis unless residual moisture before moulding is below 250 ppm; published data for PV 6930 under this exact test configuration is limited. Terminal products are plant support clips, vine clips, seedling pot labels, and nursery stake tags.
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    Certification & Compliance
    More Introduction

    TEREZ NatureGran PV 6930 is an impact-modified polylactic acid injection moulding compound. The model designation PV 6930 identifies a specific impact-modifier architecture and melt-flow balance within the NatureGran portfolio; the polymer matrix is PLA, the processing route is injection moulding, and the modification is intended to reduce room-temperature notch sensitivity relative to unmodified PLA. The grade is supplied as cylindrical pellets and is processed on conventional three-zone screw injection moulding machines with non-return valves and general-purpose screws having an L/D of at least 20:1. Published lot-independent datasheet values for this specific configuration are limited, so downstream qualification should rely on a lot-specific certificate of analysis and first-article inspection against the intended part geometry.

    A complete incoming-material inspection protocol for this product should reference the following property-reporting matrix. Unless otherwise stated, test specimens are conditioned at 23 °C and 50 % relative humidity for at least 40 h according to ISO 291. Impact-modified PLA grades in this class commonly shift the tensile failure mode from brittle fracture toward ductile yielding, but the exact lot values must be obtained from the certificate of analysis.

    PropertyStandard designationSpecimen or conditioning detail
    Melt mass-flow rateISO 1133-1:2022Dried granules, 190 °C, 2.16 kg, reported in g/10 min
    Tensile strength at breakISO 527-2Type 1A specimen, 1 mm/min test speed
    Tensile modulusISO 527-2Type 1A specimen, 1 mm/min test speed
    Notched Charpy impact strengthISO 179-1/1eAEdgewise notched specimen, 23 °C
    Unnotched Charpy impact strengthISO 179-1/1eUEdgewise unnotched specimen, 23 °C
    Heat deflection temperatureISO 75-2/BFlatwise, 0.45 MPa flexural stress
    Vicat softening temperatureISO 306A50 method, 10 N load, 50 °C/h
    DensityISO 1183-1Method A, immersion in distilled water
    Water absorptionISO 62Immersion at 23 °C, 24 h
    Moulding shrinkageISO 294-4Parallel and normal to flow, 60 mm × 60 mm plaque

    Which Processing Parameters Govern Sink-Mark Formation and Weld-Line Strength?

    Impact-modified PLA compounds exhibit shear-thinning behaviour at injection moulding shear rates. Melt viscosity at the flow front controls the pressure required to pack out ribs, bosses, and thin-wall sections before gate freeze. Sink-mark formation is governed by local volumetric shrinkage, hold pressure, and gate seal time; therefore machine pressure settings alone are insufficient. Cavity pressure sensors located near the gate and before the end of fill are used to determine whether the gate remains open during the packing phase. If gate freeze occurs before cavity pressure decays to a stable level, sink marks deepen and part mass variability increases. On production-scale toggle-clamp machines with clamp forces between 500 kN and 2000 kN, the typical response is to extend the hold-pressure time or enlarge the gate diameter. Weld-line strength in impact-modified PLA is especially sensitive to flow-front temperature. When two melt fronts meet after flowing around a core pin, the impact-modifier phase can become oriented parallel to the weld plane, producing a local notch-sensitive plane. Venting near the weld line, elevated mould temperature, and gate repositioning are used to raise the flow-front temperature without exceeding the degradation limit of the compound.

    For snap-fit closures and threaded caps, the practical processing target is to maintain melt temperature at the weld line above the crystalline onset temperature of the PLA phase. Infrared thermography at the parting line is one available method; cavity pressure sensors in the knit area are another. The hold-pressure profile should be derived from pressure-time data rather than generic machine settings. A switch-over from injection to hold that occurs too late can produce flash and mould damage, while switch-over that occurs too early can produce short shots or excessive shrinkage. The processing window is therefore established on the specific machine and mould, not transferred from a generic data sheet.

    Thermal Degradation Pathways in Impact-Modified PLA Compounds

    Thermal degradation of PLA proceeds through random chain scission, unzipping to lactide, and hydrolytic chain cleavage if moisture is present. At melt temperatures above 220 °C, the rate of molecular weight loss increases sharply. The resident melt in the barrel should be kept below the manufacturer’s maximum melt temperature, and screw recovery should be matched to the cycle so that the melt cushion is not re-plasticised for long periods. The presence of an impact-modifier phase may alter the degradation profile depending on the modifier’s thermal stability and residual acid content. Alkaline processing aids should be avoided because they catalyse PLA ester hydrolysis. Hot-runner systems with dead spots or overly long residence times can produce yellowing and plate-out; free-flow hot-runner geometries with direct-gated nozzles are preferred.

    Experimental lot evaluations on reciprocating-screw machines show that melt residence times above 5 min at melt temperature can reduce molecular weight and shift notched Charpy impact strength even when visual degradation is absent. The recommended control is to record melt temperature, cycle time, cushion size, and screw recovery speed for each lot. A falling melt viscosity or rising melt mass-flow rate after repeated drying cycles may indicate progressive hydrolytic or thermal damage rather than normal lot-to-lot variation. The use of regrind from impact-modified PLA parts should be controlled by blending ratios and verified by ISO 1133-1:2022 melt flow testing and ISO 179-1/1eA impact testing, because multiple heat histories accelerate molecular weight reduction.

    Comparative Failure Mode Analysis: Unmodified PLA, Impact-Modified PLA, and ABS

    Unmodified PLA tested according to ISO 527-2 typically fails in a brittle mode with low elongation at break. Impact-modified PLA reduces notch sensitivity and increases ductility, but the trade-off is a reduction in tensile modulus and tensile strength. The exact balance for TEREZ NatureGran PV 6930 is specific to the certificate of analysis, but the expected difference from unmodified PLA is a measurable increase in notched Charpy impact energy and a lower modulus. Heat deflection temperature may also be lower than that of a neat PLA grade because the impact-modifier phase contributes compliance without increasing the load-bearing network.

    Compared with ABS, the impact-modified PLA retains a higher biobased carbon content but has a density near 1.24–1.28 g/cm³, while amorphous ABS is typically 1.04–1.07 g/cm³. This creates a weight penalty for PLA mouldings. ABS also generally provides higher notched impact strength and better retention of stiffness at elevated service temperatures. PLA-based impact-modified compounds should therefore be limited to non-load-bearing, non-safety-critical mouldings where service temperatures remain below the Vicat softening point. Compared with other impact-modified PLA formulations, the PV 6930 grade should be differentiated by its melt mass-flow rate, notched Charpy impact strength at 23 °C, shrinkage anisotropy, and the specific modifier chemistry. High-viscosity impact modifiers may raise injection pressure requirements, while low-viscosity grades may sacrifice impact strength or create flash on worn platens. Tool design should not be finalised without lot-specific shrinkage data acquired according to ISO 294-4.

    When Moisture Uptake Exceeds 0.25 wt%, Pre-Drying Becomes the Critical Unit Operation

    PLA hydrolyses at melt temperatures, so residual moisture must be kept below 250 ppm before processing. If pellets are exposed to ambient air at relative humidity above 60 %, moisture uptake can exceed the threshold within hours. Pre-drying in a desiccant dryer with a dew point below -40 °C and an inlet air temperature of 80 °C for at least 4 h is the standard procedure. Residual moisture is measured by ISO 15512:2019 Karl Fischer titration or an equivalent calibrated loss-on-drying instrument. If moisture exceeds 250 ppm, the melt mass-flow rate increases, impact strength falls, and splay marks appear on the part surface. Production-scale experience with recirculating dryers shows that a dew-point sensor failure can raise moisture and produce viscosity drift even when barrel temperatures remain unchanged; therefore melt viscosity or MFR should be monitored after each drying cycle.

    Typical injection moulding operating envelope for impact-modified PLA compounds
    ParameterTypical rangeReference or note
    Desiccant drying temperature80 °C for 4 hDew point below -40 °C, residual moisture ≤ 250 ppm
    Melt temperature180–210 °CUpper limit constrained by PLA thermal degradation
    Mould temperature25–40 °CHigher mould temperature improves dimensional stability but increases cycle time
    Screw back pressure5–10 barModerate back pressure avoids excessive shear heating
    Hold pressure400–800 barDependent on gate geometry and melt flow length
    Maximum melt residence time≤ 5 minShorter residence time reduces molecular weight loss

    For non-load-bearing injection-moulded articles such as cosmetic packaging, office equipment housings, and consumer electronic enclosures, TEREZ NatureGran PV 6930 is evaluated on drop-weight impact, moulded-in stress, and dimensional stability after conditioning. Food-contact applications require verification of impact-modifier compliance under EU Regulation 10/2011 or FDA 21 CFR 177.1520; the presence of an impact-modifier phase may exclude use under those clearances unless the specific grade is explicitly listed. REACH and RoHS documentation should be requested from the manufacturer. Continuous service above 50–55 °C may produce creep and loss of interference fit in press-fit assemblies, so elevated-temperature performance must be verified with the final moulded part rather than inferred from the polymer family. The material is not intended for safety-critical or load-bearing structural components.

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