| HS Code | 149560 |
| Grade Designation | Oriental Energy PPH M12 |
| Polymer Type | Polypropylene homopolymer |
| Processing Method | Injection molding |
| Melt Flow Rate | 12 g/10 min |
| Density | 0.90–0.91 g/cm³ |
| Tensile Yield Strength | 30–35 MPa |
| Elongation At Break | ≥50% |
| Flexural Modulus | 1300–1500 MPa |
| Notched Izod Impact Strength | ≥3 kJ/m² |
| Heat Deflection Temperature | ≥95 °C |
| Vicat Softening Temperature | ≥150 °C |
| Molding Shrinkage | 1.5–2.0% |
| Melt Processing Temperature | 200–240 °C |
| Mold Temperature | 30–60 °C |
As an accredited Oriental Energy PPH M12,Injection Molding factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Oriental Energy PPH M12 injection molding grade is supplied in 25 kg moisture-resistant woven bags, palletized for bulk handling. |
| Container Loading (20′ FCL) | Oriental Energy PPH M12 injection molding grade loaded in 20′ FCL, 25 kg bags on pallets, shrink-wrapped, secured for sea transport. |
| Shipping | Oriental Energy PPH M12 is a non-hazardous polypropylene homopolymer injection-molding grade supplied as plastic pellets, usually in 25 kg bags or bulk containers. Ship in a dry, clean, ventilated container; protect from moisture, sunlight, contamination, punctures, and excessive stacking. |
| Storage | Oriental Energy PPH M12 injection molding grade: Store in a cool, dry, well-ventilated area away from direct sunlight, heat, flames, and oxidizing agents. Keep packaging sealed and pallets off the floor to prevent moisture pickup and contamination. Ensure containers remain closed when not in use. Avoid UV exposure and extreme temperatures. Maintain housekeeping, follow local regulations, and use oldest stock first. |
| Shelf Life | Shelf life is typically 24 months when stored dry and ventilated, away from direct sunlight and moisture in unopened original packaging. |
At a nominal melt mass-flow rate of 12 g/10 min under ISO 1133-1:2022 (230 °C, 2.16 kg), Oriental Energy PPH M12 occupies the intermediate-flow band that high-speed thin-wall food-contact moulding lines specify for wall stocks between 0.8 mm and 1.6 mm; lower-flow grades create pressure-limited short shots at the end of fill, while higher-flow grades reduce melt strength and increase gate blush on multi-cavity tools with fan gates or sub-gates. On a 350–500 t hybrid injection moulding machine with a 22:1 L/D screw and check-ring non-return valve, a typical barrel profile runs 210 °C feed, 230 °C compression, 245 °C metering and 240 °C nozzle; mould temperature is held between 15 °C and 40 °C with turbulent-flow water circuits. Injection velocity is set from 180 mm/s to 350 mm/s, transfer at 95–98% fill by screw position, packing pressure 45–65 MPa for 0.5–1.5 s, and holding time 6–15 s depending on wall stock and gate freezing. The formulation for food-contact thin-wall articles typically adds 0.05–0.20 wt% sorbitol-derived clarifying agent to suppress haze below 15% at 1.0 mm wall thickness, 0.03–0.08 wt% phosphite/hindered phenolic antioxidant, 0.02–0.06 wt% calcium stearate acid scavenger, and 0.5–2.0 wt% pigment masterbatch in a food-contact-approved carrier resin; the total low-molecular-weight additive package remains below 0.3 wt% to limit interaction with aggressive food simulants. Compliance for this sector is verified under EU Regulation (EU) No 10/2011 Annex IV overall migration limits of 10 mg/dm² for finished articles, FDA 21 CFR 177.1520 olefin polymer provisions, and GB 4806.6-2016 for domestic Chinese applications; the processor is expected to document each masterbatch as compliant rather than relying on the base resin alone. Terminal product types include dairy tubs, portion cups, non-fat dry food containers, chilled food packaging bases, and reusable lunch boxes; microwave reheating of homopolymer parts is limited by the slow oxidative degradation at elevated surface temperature, so fatty food contact above 70 °C requires migration testing under EU 10/2011 simulant D2.
Torque retention in injection-moulded PPH M12 closures is governed mainly by residual stress at the hinge and bridge area, by surface slip-agent bloom, and by shrinkage after the tamper-evident band is folded and slit; published data for this specific configuration is limited, but production lines using 32–64-cavity hot-runner tools report that bridge fracture and ovality below 0.3 mm diameter are the main failure modes when barrel temperatures exceed 250 °C or when the hot-runner gate temperature varies by more than 5 °C across the manifold. The formulation for still-water and non-carbonated beverage caps typically uses 0.05–0.15 wt% erucamide or 0.10–0.20 wt% oleamide as a controlled slip agent, 0.05–0.20 wt% nucleating agent to raise crystallization onset and shorten cycle time by 8–12%, 0.04–0.10 wt% antioxidant, and 1–3 wt% white masterbatch; the slip agent is intentionally allowed to migrate to the surface, but exceeding 0.20 wt% erucamide creates mould vent plate-out and can reduce induction seal adhesion. Processing in this sector uses melt temperatures between 230 °C and 250 °C, mould temperatures of 15–30 °C, injection pressure of 80–110 MPa, and cycle times of 7–12 s in high-cavitation tools; holding time is fixed by gate freeze at the valve-gate tip, and premature gate closure produces sink marks at the cap central hub. Compliance for food-contact closures is assessed under EU Regulation (EU) No 10/2011, FDA 21 CFR 177.1520, and GB 4806.6-2016 for food-contact surfaces, with child-resistant designs tested to ISO 8317:2015 for opening and closing cycles; if the closure is used for pharmaceutical or nutritional products, the finished packaging may require additional extractables testing under USP 661.1 or Ph. Eur. 3.1.3. Terminal products include screw caps for still water, edible oil closures, snap-over overcaps for cosmetics, push-pull dispensing caps for sports drinks, and tamper-evident caps with induction seal liners; carbonated soft-drink closure service is not recommended for unfilled PPH M12 because environmental stress cracking under carbonation pressure can cause cap skirt cracking at low radius areas.
When rigid household storage articles are specified for stack-load resistance at ambient temperatures, the main processing variable is not melt flow but the relationship between melt temperature, packing pressure, and wall thickness in the base fillet; sink-mark formation at wall junctions above 2.5 mm is the dominant visual defect, and tools are gated at thick sections to maintain packing during shrinkage. Typical compound formulation for household articles uses 5–15 wt% talc to lift flexural modulus from approximately 1,500 MPa to 2,300–3,000 MPa under ISO 178:2019, 0.05–0.15 wt% hindered phenolic antioxidant, 0.1–0.3 wt% antistatic additive to reduce dust attraction, 0.1–0.5 wt% hindered amine light stabiliser for outdoor use, and 0.5–3.0 wt% colour masterbatch; for articles that will be stacked or loaded intermittently, nucleating agent at 0.05–0.20 wt% reduces differential shrinkage and warpage in flat bases. Processing uses standard single-face or two-platen injection moulding machines with tonnage between 150 t and 600 t, barrel profile 210–240 °C, mould temperature 20–40 °C, injection pressure 80–120 MPa, back pressure 0.8–1.5 MPa, and cooling time 15–30 s for wall stocks from 1.5 mm to 3.0 mm; the screw L/D is maintained at 20:1–24:1, and regrind of clean production scrap up to 30 wt% is common but will reduce notched impact strength by 5–10% per pass depending on thermal history. Compliance for this sector is anchored by REACH Annex XVII restricted substances, RoHS Directive 2011/65/EU for electrical accessories only, and EN 71-3:2019 migration of certain elements where the article may be marketed as a toy or child-use item; food-contact versions follow EU 10/2011 and FDA 21 CFR 177.1520 if the storage article is intended for dry food contact. Terminal products include storage boxes, drawer organisers, laundry baskets, hangers, planters, waste-bin bodies, and garment storage containers; the unfilled or talc-filled PPH M12 matrix is not intended for drop impact below 0 °C, where impact copolymer grades or an addition of 5–10 wt% ethylene-octene impact modifier will be required at the expense of stiffness.
Non-structural appliance components injection-moulded from PPH M12 are selected when the part must pass a combination of electrical safety, dimensional rigidity, and long-term thermal ageing at moderate service temperatures; the defining compliance boundary is not resin formulation but the evidence chain required by IEC 60335-1:2020 Clause 30.2 for glow-wire resistance of unattended appliances, UL 94 HB or UL 94 V-2 flammability classification for housings, RoHS Directive 2011/65/EU Annex II restricted substances, and REACH candidate-list SVHC disclosure. A typical compound for appliance brackets, drain trays, and fan shrouds contains 10–20 wt% talc for flexural modulus in the range 2,200–3,200 MPa under ISO 178:2019, 0.1–0.5 wt% long-term heat stabiliser, 0.05–0.15 wt% processing antioxidant, and 0.5–2.0 wt% colour or carbon black masterbatch; if the part is exposed to washing-machine detergent solution or condensate, the formulation must avoid acid-sensitive pigments and excessive calcium carbonate filler above 10 wt% because calcium salt dissolution can produce surface pitting. Processing uses medium-to-large injection moulding machines with 300–600 t clamp force, melt temperatures of 220–250 °C, mould temperatures of 30–60 °C, injection pressure 100–140 MPa, and cycle times 25–45 s; thick ribs and bosses require screw decompression after plasticising to prevent drool, and gas counterpressure is used on some drainage components to reduce sink over 3.0 mm wall transitions. Terminal parts include air-conditioner drain pans, refrigerator kick plates and control-panel brackets, vacuum-cleaner housings, lint-filter frames, and fan shrouds; continuous service above 90 °C requires long-term heat-ageing data under UL 746B and is not recommended for unfilled PPH M12 unless the specific stabiliser package has been validated at the target temperature.
| Downstream sector | Primary standard or regulation | Critical test method / clause | Operational boundary |
|---|---|---|---|
| Thin-wall food-contact containers | EU Regulation (EU) No 10/2011, FDA 21 CFR 177.1520, GB 4806.6-2016 | Annex IV overall migration; simulants B and D2 | Total low-molecular-weight additives ≤ 0.3 wt%; melt temperature ≤ 250 °C |
| Non-carbonated beverage closures | EU Regulation (EU) No 10/2011, FDA 21 CFR 177.1520, ISO 8317:2015 | Torque retention, bridge fracture, ovality | Erucamide ≤ 0.20 wt%; hot-runner gate ΔT ≤ 5 °C |
| Rigid household storage articles | REACH, RoHS Directive 2011/65/EU, EN 71-3:2019 | Migration of elements; stack-load dimensional checks | Service temperature ≥ 0 °C unless impact modifier added |
| Appliance components | IEC 60335-1:2020, UL 94 HB, RoHS Directive 2011/65/EU | Clause 30.2 glow-wire; UL 746B long-term ageing | Continuous service ≤ 90 °C unless stabiliser package is validated |
| Diagnostic and laboratory consumables | ISO 10993-1:2018, ISO 13485:2016, EU MDR 2017/745 | Biological evaluation plan; sterilization validation | Steam autoclaving ≤ 5–10 cycles; gamma ≤ 40 kGy |
| Industrial logistic crates | ASTM D642-15, ISO 12048:2021, REACH, EU 10/2011 | Stack compression, UV weathering, migration | Hot-washing ≤ 80 °C; calcium carbonate ≤ 10 wt% |
In diagnostic and laboratory consumable manufacturing, the choice between ethylene oxide, gamma irradiation, or steam autoclaving changes the additive constraints on the injection-moulded PP article, because steam at 121 °C can hydrolyse some nucleator or antistatic packages and generate haze, while gamma irradiation above 40 kGy can initiate oxidation and shift yellowing index by more than 2 units unless a radiation-tolerant antioxidant is selected. PPH M12 is therefore formulated for this sector with a low-extractables package: 0.03–0.10 wt% hindered phenolic antioxidant, 0.02–0.05 wt% acid neutraliser, 0.10–0.30 wt% clarifying agent for transparent or translucent parts, and 0–20 wt% clean regrind that has been qualified for the same sterilization dose; plasticisers, slip agents, and unknown colour masterbatches are excluded because they raise extractable fractions and interfere with validated analyte recovery in diagnostic assays. Processing is carried out in cleanroom injection moulding under ISO 14644-1:2015 Class 8 or better, using 100–300 t machines with screw L/D of 22:1–24:1, melt temperature 220–240 °C, mould temperature 20–40 °C, injection speed 80–200 mm/s, and holding pressure 60–80 MPa; tooling is polished to SPI-A2 or better, and any mould release agent is omitted because silicone contamination invalidates protein binding and optical readout. Compliance is assessed at the finished-device level under ISO 10993-1:2018 biological evaluation planning, ISO 13485:2016 clause 7.5.3 for validation of sterilization and cleanroom processes, EU MDR 2017/745 Annex I general safety and performance requirements, and FDA 21 CFR 177.1520 if the consumable is also used with food; resin certification alone does not provide biocompatibility clearance. Terminal product types include centrifuge tubes, pipette tips, microplate strip tubes, sample cups, specimen containers, and diagnostic cartridge housings; repeated steam autoclaving of translucent unfilled parts is limited to 5–10 cycles before optical haze and dimensional change exceed user specifications, depending on wall thickness.
Logistic crates, pallet boxes, and ventilation containers moulded from PPH M12 operate under intermittent static loads, frequent washing, and sometimes outdoor storage; the dominant long-term failure mode is not instantaneous breakage but creep buckling of the sidewall when stack compression at 40–60 °C exceeds the compounded part's compressive yield, and the design check is usually performed under ASTM D642-15 or ISO 12048:2021 as applicable to complete transport packaging. The formulation for industrial material-handling parts uses 5–15 wt% talc or 5–10 wt% impact modifier to balance top-load stiffness and drop impact at low ambient temperature, 0.05–0.20 wt% antioxidant, 0.10–0.50 wt% hindered amine light stabiliser where the crate will be stored outdoors, and 1–3 wt% carbon black masterbatch for UV resistance; calcium carbonate is generally avoided above 10 wt% because it reduces weld-line strength at the handle and grid intersections. Processing requires large-tonnage injection moulding machines with clamp force from 800 t to 1,600 t, melt temperatures of 220–250 °C, mould temperatures of 20–50 °C, injection pressure 100–140 MPa, and cycle times of 30–60 s for single-face or stacked tools; hot-runner valve gates, conformal cooling in the base plate, and sequential valve gate opening are used to prevent hesitation lines and weak knit lines at the grid ribs. Compliance for logistic crates includes REACH Annex XVII for heavy metals and phthalates, RoHS Directive 2011/65/EU where the crate may be used in electrical or electronic product logistics, EU Regulation (EU) No 10/2011 if direct food contact is claimed, and ISO 18601:2013 for reusable packaging systems; export punnets or trays for fruit and vegetable contact may require additional marker migration testing under EU 10/2011 Annex II. Terminal products include collapsible fruit and vegetable crates, bread trays, pallet boxes, dunnage trays, ventilation containers, and fish tubs; direct contact with aggressive fruit-juice leachates, hot-washing above 80 °C, or chemical sanitisers with oxidising agents should be avoided unless the exact stabiliser and additive package is validated for the exposed surface area.
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