| HS Code | 817168 |
| Density | 0.90 g/cm³ |
| Melt Flow Index 230 C 2 16 Kg | 3.5 g/10min |
| Tensile Strength At Yield | 35 MPa |
| Elongation At Yield | 11% |
| Flexural Modulus | 1450 MPa |
| Izod Impact Strength Notched 23 C | 45 J/m |
| Rockwell Hardness | 100 R-scale |
| Heat Deflection Temperature 0 46 Mpa | 100 °C |
| Heat Deflection Temperature 1 82 Mpa | 60 °C |
| Vicat Softening Point | 155 °C |
| Melting Point | 165 °C |
| Crystallinity | 50% |
As an accredited Propilven PP Homopolymer J-302 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in 25 kg woven polypropylene bags with moisture-proof inner liner, sealed and clearly labeled for safe handling. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): 20-foot container loaded with Propilven PP Homopolymer J-302 in 25kg bags on pallets, approximately 20 metric tons. |
| Shipping | Propilven PP Homopolymer J-302 is shipped as polypropylene homopolymer pellets in sealed packaging to prevent moisture contamination. The material is non-hazardous for transport under standard regulations. Keep away from direct heat, ignition sources, and prolonged UV exposure. Handle carefully to avoid bag damage and store in a dry, well-ventilated area. |
| Storage | Store Propilven PP Homopolymer J-302 in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep containers tightly sealed to prevent moisture contamination and dust accumulation. Avoid contact with strong oxidizing agents. Maintain stable ambient temperatures; prolonged exposure to high heat may cause degradation. No special storage restrictions required under normal conditions. |
| Shelf Life | Shelf life is 12 months from production if stored unopened in a cool, dry place away from direct sunlight and heat. |
Returnable logistic crates moulded from Propilven J-302 are typically run on reciprocating-screw injection machines configured with a plasticating unit at 20:1–22:1 L/D, screw compression ratio of 2.5:1–3.0:1, and non-return valve clearance held below 0.15 mm to limit shot-weight drift to ±0.3%. For multi-cavity crate tools, clamp force is calculated from a cavity pressure of 35–55 MPa at gate freeze, corresponding to approximately 3.5–5.5 kN per square centimetre of projected area and reaching 1000–1800 tonnes on pallet-sized moulds. Compliance with REACH Article 33 for SVHCs, RoHS Directive 2011/65/EU Annex II, and EU Regulation 10/2011 Annex I for food-contact packaging applies only where the natural resin and added masterbatch are controlled under an overall migration limit of ≤10 mg/dm² (OML). For industrial non-food crates, UN dangerous goods packaging certification may apply; a polypropylene homopolymer without fluorinated barrier treatment generally fails permeation requirements for many UN Class 3 liquids at wall thicknesses below 4 mm. Formulation-wise, natural J-302 is processed without let-down or with 2.0–3.0 wt% carbon black or grey masterbatch for outdoor identification. If annual UV exposure exceeds approximately 800 h, 0.2–0.5 wt% hindered amine light stabilizer masterbatch is added, and 0.1–0.25 wt% nucleating agent may be incorporated to offset the modest crystallinity increase produced by carbon black loadings above 2.5 wt%. Processing parameters include melt temperature 230–250°C, mould temperature 15–40°C, injection pressure 80–110 MPa, holding pressure 60–80% of peak injection pressure for 6–12 s, back pressure 0.5–1.0 MPa, and screw surface speed 0.2–0.4 m/s. Warpage in wide-span crate bases is controlled by maintaining gate-freeze within the holding phase and by sizing cooling channels to achieve a maximum mould-surface temperature deviation of 3°C between cavity halves. Terminal products include stackable fruit and vegetable crates, dairy case tote bins, industrial parts bins, collapsible pallet boxes, and 20–30 L non-UN utility pails.
For closures with an integral living hinge and wall thickness above 1.1 mm, J-302 is employed at full natural let-down or with 2.0 wt% white masterbatch; slip additives must be limited to 0.05–0.10 wt% erucamide or oleamide to reduce cap-on-torque without causing stress crazing at the hinge root. Higher slip levels above 0.15 wt% lower coefficient of friction to below 0.25 but accelerate hinge-whitening after repeated flexing beyond 2,000 cycles. Compliance follows EU Regulation 10/2011 for contact with still beverages and food products, 21 CFR 177.1520 for olefin polymers, and 21 CFR 175.300 where the closure liner is a separate resin system. If used for pharmaceutical vial closure bodies, pharmacopoeia monographs EP 3.1.3 and USP <661.1> for polyolefins require extractables control and verification of no visible particle release. Processing on injection machines with 80–200 tonnes clamp force uses a melt temperature of 220–240°C, a mould temperature of 10–20°C at the hinge cavity, injection speed 30–60 mm/s, and holding pressure 50–70 MPa for 1.5–3.0 s to minimize sink at the hinge gate. Hot-runner valve-gated systems with 0.6–1.0 mm gate diameters prevent gate blush on the tamper-evident band; if cold runners are used, runner scrap is limited to 20–25% of shot weight or recycled at 10–20% to avoid MFR drift in the final part. The 3.0 g/10 min melt flow rate narrows the thin-wall process window; when wall thickness drops below 1.0 mm, injection speed must be increased beyond 80 mm/s, which can generate shear heating above 250°C at the gate and cause local degradation, gate streaks, and loss of hinge impact. Terminal closures include flip-top dispensing caps for personal care, tamper-evident beverage closures for non-carbonated dairy and juice products, child-resistant container caps for nutraceuticals, and hinged closures for industrial chemical bottles.
In household injection moulding, colour masterbatch loadings above 4.0 wt% alter the crystallisation kinetics of J-302 enough to shift the peak crystallisation temperature by 2–4°C, which changes gate-freeze timing and forces re-validation of the holding-pressure profile on multi-cavity kitchen tool moulds. Food-contact compliance for opaque and translucent kitchen storage is based on EU Regulation 10/2011 Annex I overall migration limits of 10 mg/dm², 21 CFR 177.1520, and German BfR Recommendation VII for polypropylene; where coloured masterbatches are used, the masterbatch carrier and pigments must themselves meet the same migration and residual content restrictions. Formulation: J-302 natural is let down at 100 parts by weight with 2.0–4.0 wt% pigment masterbatch; 0.15–0.25 wt% sorbitol-based clarifying agent may be included only where the final article must transmit visible light and wall thickness is below 1.5 mm, because clarifier at this dosage lowers haze to 12–18% but reduces elongation at yield by up to 2 percentage points. A 0.1–0.3 wt% glycerol monostearate antistatic masterbatch is added where dry food powder is stored and surface static build-up would cause dust adhesion. Processing on 60–120 tonne machines with a 20:1–22:1 L/D screw uses melt temperature 210–230°C, mould temperature 15–30°C, injection pressure 60–90 MPa, and a holding-pressure-time product of 30–45 MPa·s for 1.5–2.5 mm wall sections. For food containers, screw and barrel chrome plating with a surface roughness below 0.4 µm Ra is specified to avoid dead-spots that degrade polymer into black speck contamination. Terminal articles include stackable kitchen storage containers, lunch boxes, refrigerator vegetable drawers, food scoops, measuring cups, and reusable pantry bins.
Rigid toy components such as interlocking building blocks are produced from J-302 with 2.0–4.0 wt% colour masterbatch, and where outdoor play equipment is moulded, 0.3–0.5 wt% hindered amine light stabilizer plus 0.1–0.2 wt% UV absorber masterbatch is added; the base resin itself contributes negligible UV stabilisation. Compliance with toy safety migration standards is mandatory: EN 71-3:2019+A1:2021 sets category-specific limits for accessible toy materials, and rigid moulded blocks classified as Category III scraped-off materials require lead migration no greater than 23 mg/kg and cadmium no greater than 5.5 mg/kg. ASTM F963-23 contains parallel heavy metal controls for substrates and surface coatings. Phthalate plasticisers are absent from J-302, but any purchased colour masterbatch must be verified against the 0.1% limit for DEHP, DBP, BBP, and DIBP under EU REACH Annex XVII Entry 51 and U.S. CPSIA Sec. 108. Dimensional stability in multi-cavity block tools with 120 cavities depends on controlling linear mould shrinkage to 1.0–1.4% and on achieving a cavity-to-cavity melt temperature variation below 3°C; this is met by valve-gated cold runners with sequential filling rather than open hot runners, which can produce cavity-to-cavity shear differences that shift block post-mould dimensions by up to 0.15 mm. Process settings: melt 220–250°C, mould 20–40°C, injection velocity 80–120 mm/s for flow lengths below 120 mm, holding pressure 65–85 MPa for 2–4 s, back pressure 1.0–1.5 MPa, and a calibrated shrink fixture checked after 24 h at 23°C ± 2°C per ISO 291 to confirm final part dimensions. Terminal products include interlocking blocks, board game pawns and dice, building panels, toy tool parts, and sandpit moulds.
When ice-cube trays and freezer drawers are moulded without impact modification, the homopolymer’s notched Charpy impact strength of 2–4 kJ/m² at -20°C under ISO 179-1:2010 becomes the limiting property that dictates gate location and wall-thickness distribution, because abrupt thickness transitions below 2.0 mm combined with low-radius corners create brittle fracture during demoulding. Compliance for refrigerator interior components follows EU Regulation 10/2011 for indirect food contact only where the part is behind a barrier or not intended for direct food contact; REACH SVHC and RoHS Annex II apply to all electrical/electronic equipment categories, and IEC 60335-1 household appliance requirements may impose the IEC 60695-2-11 glow-wire test. Unmodified J-302 is classified UL 94 HB and is not substituted into components requiring V-2 classification unless a halogen-free intumescent flame-retardant masterbatch is evaluated, which will reduce melt flow and notched impact. Formulation: base J-302 may be used unmodified, but for freezer trays 0.5–1.0 wt% ethylene-based impact modifier is added to raise low-temperature impact, and 0.2–0.4 wt% nucleating agent is added to reduce warpage in thin flat bases; the nucleator increases flexural modulus from approximately 1,200 MPa to 1,350–1,450 MPa under ISO 178:2019 but lowers impact slightly. Processing on 80–150 tonne machines with a reversed temperature profile is recommended: feed 200°C, compression 220°C, metering 230°C, nozzle 220°C; mould temperature 15–25°C; screw speed 40–80 rpm; shot weight held to 60–80% of barrel capacity to avoid residence times above 5 min, which cause yellowing and a drop in elongation at yield below 6%. Terminal parts include ice-cube trays, refrigerator vegetable crispers, freezer drawer fronts, washing machine detergent drawer bodies, and dishwasher cutlery baskets without metal inserts.
Outdoor garden furniture and plant pots made from J-302 are processed with UV stabiliser masterbatches and anti-fungal additives only where long-term outdoor exposure is specified. Compliance is governed by REACH Annex VII and Annex VIII for outdoor articles not intended for food contact, and by the Packaging and Packaging Waste Directive 94/62/EC only for reusable plant transport trays; there is no mandatory EU UV degradation standard for consumer garden furniture, but many technical specifications reference ISO 4892-2 Xenon arc exposure with colour change ΔE ≤3 after 2,000 h for commercial contracts. Formulation: for natural-coloured garden chairs and tables, 0.4–0.6 wt% HALS and 0.1–0.2 wt% benzotriazole UV absorber are added to delay chalking and surface crazing beyond 2,000 h Xenon exposure; for dark colours, 2.0–3.0 wt% carbon black masterbatch substitutes for UV absorbers when particle size is below 25 nm and dispersion is verified by no visible agglomerates above 10 µm in a pressed film. Regrind content is limited to 20–30 wt% because recycled J-302 loses thermal stabiliser effectiveness under repeated extrusion; addition of 0.05–0.10 wt% additional phenolic antioxidant is required when regrind exceeds 30%, but this may cause yellowing in white parts after 1,000 h Xenon. Process: injection moulding of large garden furniture parts uses low-speed filling at 10–20 mm/s screw advance, melt temperature 230–250°C, mould temperature 20–40°C, holding pressure 50–70 MPa, and cooling times from 25–60 s depending on wall thickness 3–6 mm; gas-assisted injection of hollow backs reduces sink marks but requires pack pressure and gas delay times tuned to avoid gas blow-through at thin ribs. Terminal articles include garden chairs, tables, plant pots, compost bins, window boxes, and stackable plant trays.
| Application segment | Melt temperature (°C) | Mould temperature (°C) | Injection/holding pressure (MPa) | Primary standard anchor |
|---|---|---|---|---|
| Rigid crates and pallet boxes | 230–250 | 15–40 | 80–110 / 60–80% of peak | ISO 1133-1:2022; ISO 294-1 |
| Hinged closures | 220–240 | 10–20 at hinge | 50–70 holding | 21 CFR 177.1520; EU 10/2011 |
| Household storage | 210–230 | 15–30 | 60–90 injection | EU 10/2011; 21 CFR 177.1520 |
| Toy blocks | 220–250 | 20–40 | 65–85 holding | EN 71-3:2019+A1:2021 |
| Freezer drawer fronts | 200–230 | 15–25 | 70–100 injection | ISO 179-1:2010; IEC 60335-1 |
| Garden furniture | 230–250 | 20–40 | 50–70 holding | ISO 4892-2 |
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Propilven PP Homopolymer J-302 is a general-purpose injection-molding polypropylene homopolymer. Its selection is governed by the interplay of melt mass-flow rate, crystallization shrinkage, short-term temperature resistance, and economic moldability. Product-specific public data for this exact grade remain limited; therefore, the numerical values presented in this document are class-representative values for polypropylene homopolymers in the same nominal melt-flow classification. They must be superseded by the manufacturer’s current certificate of analysis, technical data sheet, and regulatory documentation. The J-302 identifier is treated as a manufacturer-specific injection-molding designation within the Propilven PP family, not as a universal resin code. The product is supplied as pelleted resin and is intended for rigid injection-molded parts in which high stiffness, moderate flow, and low cost per unit volume dominate the material specification.
The nominal melt mass-flow rate for this class is 3.0 g/10 min when determined in accordance with ISO 1133-1:2022 at 230 °C and 2.16 kg. This value places J-302 in the low-to-medium flow segment for polypropylene injection-molding grades. In practice, the 3.0 g/10 min flow class is selected because it balances injection pressure against solid-state stiffness. Grades with melt mass-flow rates below 2.0 g/10 min often show higher tensile yield stress but require longer fill times and higher hydraulic pressure in multi-cavity tools. Grades above 10 g/10 min fill thin sections more readily but sacrifice flexural modulus and may create excessive flash at parting lines unless clamp force is increased.
The flow-length-to-wall-thickness ratio for the 3.0 g/10 min class is typically sufficient for wall sections from 1.5 mm to 4.0 mm. In a spiral-flow test at 230 °C, comparable homopolymer grades in this class generally produce flow lengths in the region of 400 mm to 500 mm at 2 mm wall thickness, although cavity geometry and gate dimensions alter this result substantially. For rigid housewares, small appliance bodies, pails, furniture components, and non-demanding packaging items, this flow class reduces the occurrence of sink marks and allows consistent screw recovery.
| Property | Nominal class value | Test method |
|---|---|---|
| Melt mass-flow rate | 3.0 g/10 min at 230 °C/2.16 kg | ISO 1133-1:2022 |
| Density | 0.905 g/cm³ | ISO 1183-1:2019 |
| Tensile stress at yield | 35 MPa | ISO 527-2:2012, specimen type 1A, speed 50 mm/min |
| Tensile elongation at yield | 10% | ISO 527-2:2012, specimen type 1A |
| Flexural modulus | 1,450 MPa | ISO 178:2019 |
| Notched Charpy impact strength at 23 °C | 2.0 kJ/m² | ISO 179-1:2010/1eA |
| Heat deflection temperature | 90 °C at 0.45 MPa | ISO 75-2:2013/B |
| Vicat softening temperature | 155 °C | ISO 306:2022/A50 |
In an 8-cavity cold-runner mold producing straight-sided storage boxes with 2.5 mm nominal wall thickness, the practical injection window for this material class is commonly established on a clamping force of 1,200 kN to 1,500 kN. The material is fed through a general-purpose polyolefin screw with an L/D ratio between 20:1 and 24:1 and compression ratio between 3.0:1 and 3.5:1. Barrel zone settings are often profiled from 210 °C at the feed throat to 230 °C at the nozzle. A screw back pressure of 0.5 MPa to 1.0 MPa and injection speed of 80 mm/s to 120 mm/s are typical starting values for wall sections in the 2.0 mm to 3.0 mm range. Short shots at the end of fill in such tools have been corrected more reliably by raising nozzle temperature to 235 °C than by increasing hold pressure beyond 60 MPa. Excessive hold pressure in this semicrystalline grade can increase gate-area stress, molded-in orientation, and post-mold distortion.
Drying of J-302 class resin is generally unnecessary because polypropylene is not hydrolytically degraded by moisture. However, when cold pellets are transferred from an unheated warehouse to a warm production floor at relative humidity above 60%, surface condensation can produce splay and surface defects. Under those conditions, a desiccant hopper dryer set to 80 °C for 2 h with a dew point of −20 °C or lower is a sufficient corrective action. This drying step removes surface moisture only; it does not condition the bulk polymer.
The recommended melt temperature range for this class is 210 °C to 250 °C. Operation below 210 °C increases melt viscosity and may lead to short shots, freeze-off at the gate, and excessive screw torque. Operation above 250 °C, particularly with residence times above 5 min, can cause thermal-oxidative chain scission, yellowing, loss of molecular weight, and surface splay. The crystallization temperature of polypropylene homopolymer is typically observed near 120 °C to 125 °C, which means that mold temperature has a direct influence on cooling time and shrinkage uniformity. Mold temperatures between 20 °C and 50 °C produce acceptable cycle times. A mold temperature of 30 °C to 40 °C is frequently selected for general-purpose parts. Higher mold temperatures up to 60 °C reduce frozen-in orientation and improve dimensional stability but increase cycle time and may reduce productivity in multi-cavity tools.
Injection pressure for J-302 class resin normally falls between 70 MPa and 140 MPa. Hold pressure should be optimized to the minimum level that prevents sink marks and controls part mass. Hold-pressure levels above 60 MPa in thin sections are rarely required and may produce residual stress. Screw rotation speed should be adjusted to ensure that screw recovery is completed before the cooling timer expires. For a 40 mm diameter general-purpose screw, screw speeds from 60 rpm to 120 rpm are typical. Back pressure below 0.5 MPa can result in poor color dispersion when masterbatch is added, while back pressure above 1.5 MPa can increase residence time and thermal history without a commensurate melt-quality benefit.
For pigmented production, the addition of carbon black masterbatch above 2 wt% should be evaluated because it can increase apparent melt viscosity and may reduce notched impact strength. Titanium dioxide additions in this same range can increase stiffness and density. Additive packages that release acidic decomposition products at processing temperature, including certain halogenated flame-retardant systems, should be avoided unless an acid-scavenging masterbatch is validated. The base homopolymer does not inherently contain clarifiers, antistatic agents, or UV stabilizers; these packages must be specified as separate additive masterbatches and documented by the compounder or molder.
Feed system sizing and venting are often more important than barrel profile in controlling part quality. For J-302 class resin, cold-runner diameters from 4.0 mm to 6.0 mm are common for parts with projected areas up to 0.05 m². Gate land length should generally be 0.75 mm to 1.0 mm. The gate thickness should not exceed 60% of the part wall thickness to permit clean gate freeze-off. Vent depths at the end of fill should be between 0.025 mm and 0.040 mm. Insufficient venting in this semicrystalline resin can produce diesel burns, short shots, and higher fill pressure. Mold shrinkage determined on 60 mm × 60 mm × 2 mm plaques in accordance with ISO 294-4 is class-typically 1.2% to 1.6% in the flow direction and 1.4% to 1.8% transverse after 48 h at 23 °C. Post-mold shrinkage can continue for up to 24 h to 48 h as secondary crystallization proceeds. Critical dimensions should therefore be measured after conditioning, not immediately after demolding.
J-302 class homopolymer differs from polypropylene random copolymers primarily in stiffness, temperature resistance, optical transparency, and impact behavior. The homopolymer has higher flexural modulus and higher heat deflection temperature because it lacks the ethylene comonomer that disrupts crystallization in random copolymers. It also has lower notched impact strength, especially at low temperature, and higher haze. This makes J-302 class material suitable for rigid, opaque applications where mechanical stiffness and dimensional stability are more important than clarity or impact toughness.
Compared with polypropylene impact copolymers, J-302 class homopolymer shows higher tensile yield stress and higher flexural modulus, but significantly lower notched Charpy impact strength at 23 °C and below 0 °C. Impact copolymer grades are therefore preferred for luggage, automotive interior trim, battery cases, and cold-storage containers. J-302 class material is not appropriate for sub-zero impact service unless the part is designed with thick sections, generous radii, and low external stress.
| Property | J-302 class homopolymer | Random copolymer class | Impact copolymer class |
|---|---|---|---|
| Melt mass-flow rate | 3.0 g/10 min | 6.0 g/10 min | 2.0–4.0 g/10 min |
| Flexural modulus | 1,450 MPa | 950 MPa | 1,100 MPa |
| Tensile stress at yield | 35 MPa | 25 MPa | 27 MPa |
| Notched Charpy impact at 23 °C | 2.0 kJ/m² | 6.0 kJ/m² | 12.0 kJ/m² |
| Notched Charpy impact at −20 °C | 1.5 kJ/m² | 2.0 kJ/m² | 6.0 kJ/m² |
| Heat deflection temperature at 0.45 MPa | 90 °C | 75 °C | 80 °C |
| Optical character | Opaque, high haze | Transparent to translucent, low haze | Opaque, high haze |
Within the broader Propilven injection-molding range, J-302 class occupies a lower-flow tier relative to higher-flow homopolymers used for thin-wall food containers and caps. Higher-flow grades shorten fill time and reduce clamp force, but they generally show lower tensile yield stress and lower flexural modulus because of reduced molecular orientation and lower average molecular weight. J-302 class resin is therefore selected when the part contains medium-thickness walls, requires higher stiffness, and does not require extremely rapid cavity filling.
Low-temperature service is the most common operational boundary that forces replacement of J-302 class resin with an impact copolymer. At 0 °C, notched impact strength of homopolymer is already low, and at −20 °C the material can fail in brittle mode with limited energy absorption. Applications such as freezer containers, cold-climate housings, and structural brackets should be evaluated under ISO 179-1:2010/1eA at the actual minimum service temperature before tool construction. If the failure mode is brittle at the target temperature, material substitution is required.
For applications involving hot-water contact, the homopolymer’s heat deflection temperature should not be interpreted as continuous-use temperature. Polypropylene homopolymer can exhibit creep and stress relaxation at temperatures above 80 °C, particularly under load. The Vicat softening temperature of 155 °C reflects a short-term thermal softening point, not a service limit. Continuous load-bearing service above 80 °C requires creep data generated under the actual stress and temperature conditions. Published data for this specific configuration in continuous hot-water service is limited.
Compliance status for Propilven PP Homopolymer J-302 must be confirmed through the supplier’s current additive declaration and lot-specific certificate of analysis. Polypropylene homopolymers in this class are routinely supplied with statements referencing FDA 21 CFR 177.1520(c) for olefin polymers in food-contact articles, subject to end-use conditions and additive restrictions. Under EU Regulation (EU) No 10/2011, migration testing with appropriate food simulants is required for the finished article; the base resin alone is not automatically food-contact compliant. REACH registration under Regulation (EC) No 1907/2006 is a supplier obligation, and the presence of substances of very high concern must be excluded through the supplier’s safety data sheet. For electrical and electronic equipment, base polypropylene homopolymer does not typically contain cadmium, lead, mercury, hexavalent chromium, polybrominated biphenyls, or polybrominated diphenyl ethers above the maximum concentration values specified in Directive 2011/65/EU, but additive masterbatches and processing aids must be verified separately.
No conclusion or forward-looking statement is provided. The final material decision should be made from the manufacturer’s current technical data sheet, certificate of analysis, and application-specific validation data obtained under production-scale conditions.