| HS Code | 972808 |
| Density | 1.04 g/cm³ |
| Melt Flow Rate | 20 g/10min (230°C, 2.16kg) |
| Filler Content | 20% Talc |
| Tensile Strength At Yield | 28 MPa |
| Elongation At Break | 20% |
| Flexural Modulus | 2600 MPa |
| Flexural Strength | 35 MPa |
| Izod Impact Strength Notched 23 C | 35 J/m |
| Izod Impact Strength Notched 30 C | 15 J/m |
| Heat Deflection Temperature 0 45 Mpa | 130 °C |
| Heat Deflection Temperature 1 82 Mpa | 80 °C |
| Rockwell Hardness | R95 |
| Melting Point | 160 °C |
| Moisture Absorption | 0.02% |
| Flammability | UL94 HB |
As an accredited HiPrene PP Compound HT42 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | HiPrene PP Compound HT42 is supplied in sturdy, moisture-resistant packaging, typically 25 kg sealed bags, ensuring safe handling and product integrity. |
| Container Loading (20′ FCL) | 20′ FCL container loading of HiPrene PP Compound HT42, palletized and secured, ensuring safe transport. |
| Shipping | HiPrene PP Compound HT42 is shipped as a non-hazardous polypropylene compound in sealed, moisture-resistant bags or bulk containers. Keep dry, avoid direct sunlight, and store below 40°C. Transport in covered, clean trucks to prevent contamination. Handle with standard industrial equipment and protect packaging from damage during transit. |
| Storage | Store HiPrene PP Compound HT42 in a cool, dry, well-ventilated area protected from direct sunlight, heat sources, and open flames. Keep containers tightly sealed to prevent moisture pickup and contamination. Maintain moderate temperatures, avoiding extreme heat or freezing. Under recommended conditions, shelf life is typically one year from date of manufacture. |
| Shelf Life | Shelf life is typically 12 months from manufacture if stored in original, unopened packaging in a cool, dry place. |
HiPrene PP Compound HT42 is assessed in this application set as a polypropylene copolymer compound with a heat-stabilization package suited to injection molding under sustained thermal load. The certificate of analysis for a given lot should be checked before setting line parameters for melt flow rate, filler content, and UV package. Published data for this specific grade configuration are limited; numerical windows quoted below are therefore class-typical for high-impact PP copolymer compounds unless a supplier certificate contains narrower guaranteed values. No value below replaces lot-specific quality documentation.
| Segment | Standard or test method | Condition | Inspection point |
|---|---|---|---|
| Automotive HVAC housing | ISO 179-1:2020 | 1eA, 23°C | Knit line at motor boss |
| Washing machine tub | IEC 60335-1:2020 | End product | Detergent stress crack |
| Electrical enclosure | IEC 60695-2-11:2021 | 850°C/30 s | Glow-wire ignition mass |
| Battery container | ISO 179-1:2020 | −30°C | Bottom rim weld line |
| Export pallet | ISO 8611-1:2021 | Rated load | Corner foot crack |
| Garden power cover | ISO 4892-2:2021 | UV cycle | Surface after 500 h |
Hot-runner valve gate sequencing, rather than barrel temperature alone, controls knit line integrity in automotive HVAC housing production using HiPrene PP Compound HT42. On a 1,000–1,600 t injection molding machine with a screw L/D ratio of 20:1–24:1, the melt temperature is maintained at 220–245°C, while the mold wall temperature is held at 30–55°C to limit post-demold shrinkage and gate vestige depth. Processors targeting HVAC blower motor covers under IATF 16949:2016 production part approval must submit measured data for notched Charpy impact according to ISO 179-1:2020, flexural modulus per ISO 178:2022, and heat deflection temperature under ISO 75-1:2020 method B at 0.45 MPa. The compound is charged at 100 wt% as supplied; when post-industrial regrind is reintegrated, the addition ratio is restricted to 15–25 wt% of the same-grade regrind after validation that the melt flow rate shift remains below 10% as measured by ISO 1133-1:2022 at 230°C/2.16 kg. The downstream process uses sequential valve gating to move the weld line away from the motor mount boss; gas release via core pins or vacuum venting below -0.07 MPa is required because decomposition of heat-stabilizer packages above 250°C produces die-face deposit at the gate. Terminal parts for this segment include HVAC housings, blower motor covers, and engine cooling fan shrouds where continuous service temperature does not exceed 100–110°C for unfilled copolymer grades.
For large-diameter washer tubs molded with PP copolymer compounds, radial runout after ejection is caused by nonuniform crystallinity across the tub skirt when cooling rate differentials exceed 15°C/min. HiPrene PP Compound HT42 is processed in a two-stage injection-compression sequence on presses with clamp force of 800–1,400 t; the barrel profile is set from rear to nozzle at 200/215/230/235/240°C, and the compression stroke is initiated when the melt front covers 70–80% of the cavity area. For household washing machine applications, the material must align with IEC 60335-1:2020 general safety through end-product testing, while material-level documentation commonly includes stress-crack resistance under detergent pre-soak, tensile yield stress per ISO 527-2:2021, and notched Charpy impact per ISO 179-1/1eA:2020 at 0°C. A production-validated formulation for the tub skirt is 90–94 wt% HT42 compound, 5–8 wt% talc-filled PP regrind to raise modulus, and 0.6–1.2 wt% color masterbatch; higher talc content above 10 wt% is avoided because it reduces weld-line elongation at drain-port ribs below 3%, a known failure initiation site in spin cycles. The downstream process requires vacuum venting at -0.08 MPa and screw back pressure of 3–5 MPa to prevent viscosity stratification across the shot. Terminal product types include washing machine outer tubs, dishwasher base frames, and condensate collector trays in heat-pump dryers.
Compounds used for electrical enclosures require more than a UL 94 rating; glow-wire flammability and post-test insulation integrity are the controlling criteria on production lines. For HiPrene PP Compound HT42 processed into DIN-rail junction boxes, the compliance chain includes IEC 60695-2-11:2021 at 850°C/30 s for finished enclosures, UL 94 at 0.8 mm or 1.6 mm thickness for material pre-classification, ISO 527-2:2021 tensile modulus for load-bearing snap-fit geometry, and RoHS 2011/65/EU Annex II substance restrictions for PV installations. The formulation is let down at 82–88 wt% compound with 12–18 wt% halogen-free intumescent flame-retardant masterbatch when a V-0 end use is specified; for V-2 applications, the compound is run neat at 100 wt% with only 0.3–0.8 wt% of a non-blooming processing stabilizer. Molders use screw torque monitoring and zone temperatures limited to 210–235°C because intumescent packages exhibit exothermic decomposition and scorch at melt temperatures above 240°C, causing black speck contamination at the nozzle seat. The injection profile is slowed to fill speeds of 25–40 mm/s at the gate to prevent shear heating beyond 3–5°C adiabatic rise. Final products include consumer distribution board housings, DIN rail terminal enclosures, and photovoltaic DC junction boxes.
At wall thicknesses of 2.8–4.5 mm, battery container side-wall injection with HiPrene PP Compound HT42 presents a specific low-temperature drop test challenge: the weld line near the bottom rim must survive −20°C impact exposure without separation. In this segment, the compound is molded on accumulator-equipped machines with shot volumes of 800–1,500 cm³ and a clamp force of 1,200–2,000 t; melt temperature is 215–230°C for thick side walls. The regulatory framework for lead-acid battery containers includes IEC 61056-1:2012 for general purpose lead-acid battery cells and ISO 4892-2:2021 UV exposure for trays used in solar power backup installations; material property documentation typically reports notched Charpy impact per ISO 179-1:2020 at −30°C and elongation at yield per ISO 527-2:2021. The formulation addition ratio is 100 wt% as-supplied compound, with 0.5–1.0 wt% nucleating agent to reduce post-molding secondary crystallization; addition of post-consumer battery box regrind above 20 wt% is excluded because the melt flow rate rises beyond the upper control limit of 11 g/10 min, causing flash at the side/bottom insert plane. The production process uses sequential coining and low pack pressure of 20–30 MPa to reduce side-wall sink over the lead bushing inserts. Terminal products are starter battery containers for heavy duty vehicles, e-rickshaw battery shells, and solar energy storage box trays.
Export pallet production is a low-complexity, well-established segment in which 88–92 wt% HiPrene PP Compound HT42 is let down with 8–12 wt% high-density polyethylene regrind and 0.5–1.0 wt% color masterbatch, processed by low-pressure structural foam injection molding at melt 215–230°C with 0.4–0.8 wt% blowing agent, and validated against ISO 8611-1:2021 pallet loading plus ISO 179-1:2020 notched Charpy impact at −20°C; terminal items are export pallets, folding container side panels, and agricultural crates.
In gas-assisted molding of garden power tool covers, controlled gas bubble penetration through the thick rim section without breakout at the parting line governs the processing window. HiPrene PP Compound HT42 runs on gas-assisted equipment with nitrogen gas pressure of 8–15 MPa and gas delay time of 0.8–2.0 s after prefill of 85–92% cavity volume. In this segment, outdoor power equipment manufacturers require UV and heat aging documentation per ISO 4892-2:2021, notched Izod impact per ISO 180:2019, and dimensional stability after 1,000 h at 90°C following ISO 175:2010 fluid immersion testing. The formulation addition ratio is set at 100 wt% compound for thin-wall areas, while thick rib sections are produced with a local let-down of 5–10 wt% short-glass masterbatch only where the gas channel requires increased modulus; adding glass above 10 wt% in the cover skin creates surface roughness after painting. The production process clamps the tool at 15,000–22,000 kN and uses sequential gas injection to hollow the handle bar, reducing post-mold shrinkage at the grip boss. Terminal product types are grass trimmer engine covers, chainsaw sprocket housings, and backpack blower fan scrolls.
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HiPrene PP Compound HT42 is supplied as a cylindrical pellet based on a heat-stabilized polypropylene matrix compounded with a mineral filler system. The grade is intended for injection molding where sustained heat, low post-mold warpage, and reduced mold shrinkage are required. The “42” in the product designation is read in this technical note as a nominal mineral filler loading of 42 wt%; however, because published data for this specific configuration is limited, the exact filler type, particle size distribution, stabilizer package, and lot-specific properties must be confirmed against the manufacturer’s certificate of analysis. Indicative class values for 40–45 wt% mineral-filled heat-stabilized PP compounds, determined under standardized methods, include density of 1.23–1.28 g/cm³ per ISO 1183-1:2019, melt mass-flow rate of 8–20 g/10 min per ISO 1133-1:2022 at 230 °C/2.16 kg, and flexural modulus of 3,500–4,800 MPa per ISO 178:2019. Water absorption under ISO 62:2008 at 23 °C/50% RH is generally below 0.1%, but drying remains advisable when pellet sacks have been exposed to plant humidity above 60% RH.
Mineral fillers at high loadings change the crystallization and thermal-mechanical response of the polypropylene matrix. Under ISO 75-2:2013 method A at 1.80 MPa, unfilled PP homopolymer commonly exhibits a heat deflection temperature of 55–60 °C, whereas 40 wt% talc-filled heat-stabilized compounds typically fall between 125 °C and 132 °C. The HT42 class is expected to occupy the upper end of this range if the filler loading is consistent with the grade suffix. Coefficient of linear thermal expansion measured under ISO 11359-2:1999 in the machine direction between 23 °C and 80 °C is commonly reduced to 30–50 µm/(m·°C) in highly filled PP, compared with 100–150 µm/(m·°C) for unfilled homopolymer. Post-mold shrinkage under ISO 294-4:2018 is typically 0.4–0.7% in the flow direction and 0.6–0.9% transverse to flow, provided that packing pressure is maintained above 50 MPa and gate freeze-off is not premature. These changes are accompanied by reduced impact toughness. Notched Charpy impact strength under ISO 179-1:2010 at 23 °C is commonly 2.0–4.5 kJ/m² for 40% mineral-filled PP versus 6.0–12.0 kJ/m² for a medium-impact copolymer. The trade-off is managed by part design with corner radii not less than 1 mm and rib-to-wall ratios below 0.6.
| Property | Test method | Indicative range for 40–45 wt% mineral-filled heat-stabilized PP | Condition |
|---|---|---|---|
| Density | ISO 1183-1:2019 | 1.23–1.28 g/cm³ | 23 °C |
| Melt mass-flow rate | ISO 1133-1:2022 | 8–20 g/10 min | 230 °C/2.16 kg |
| Tensile strength at yield/break | ISO 527-2:2012 | 24–30 MPa | Test speed 50 mm/min |
| Tensile modulus | ISO 527-2:2012 | 3,500–4,800 MPa | Test speed 1 mm/min |
| Flexural modulus | ISO 178:2019 | 3,800–5,000 MPa | Test speed 2 mm/min |
| Heat deflection temperature | ISO 75-2:2013 method A | 125–132 °C | 1.80 MPa |
| CLTE machine direction | ISO 11359-2:1999 | 30–50 µm/(m·°C) | 23–80 °C |
| Notched Charpy impact | ISO 179-1:2010 | 2.0–4.5 kJ/m² | 23 °C, notch A |
| Mold shrinkage flow direction | ISO 294-4:2018 | 0.4–0.7% | 60 MPa packing |
High filler loadings increase melt viscosity and shear heating. On a 350-ton hydraulic injection molding machine with a 40 mm general-purpose screw and 20:1 L/D ratio, barrel zone settings are often 190 °C at the feed zone, 210 °C in the transition zone, 220 °C in the metering zone, and 200–210 °C at the nozzle. Melt temperature measured by an insertion thermocouple should not exceed 230 °C; thermal degradation of the stabilizer package accelerates above 245 °C and produces surface splay, brown streaking, and reduced weld-line strength. Screw recovery speed should be limited to 80–120 rpm on medium-sized machines to prevent excessive shear heating. Back pressure should be set to 0.5–1.5 MPa to maintain shot consistency without extending recovery time. Mold temperatures of 30–60 °C are usually sufficient; textured surfaces may require a higher mold temperature to avoid gloss bands and flow hesitation. Predrying at 80 °C for 2–4 h is recommended when storage relative humidity exceeds 60% or when vacuum vents are unavailable. External moisture above 0.05% by mass can generate silver streaks in thin-wall sections. Desiccant drying is not mandatory for a virgin polypropylene compound but provides process stability in high-humidity plants.
Production-scale experience with 40–45% mineral-filled PP compounds indicates that filler particle size distribution is a significant source of batch-to-batch variation. Sieve analysis on a 45 µm mesh often leaves 0.5–2.0% residue, but occasional coarse fractions from partially opened mineral filler bags have caused die-face plugging in twin-screw compounding and gate blocking in multi-cavity molds. Gravimetric dosing with loss-in-weight feeders and online melt pressure monitoring before the screen changer reduce the frequency of these events. When molding HT42, the use of a hardened bimetallic screw and barrel is recommended because mineral filler accelerates screw flight wear; campaigns exceeding 250,000 cycles on standard nitrided steel have shown increased check ring leakage and shot weight drift. Mold steels should be hardened to at least HRC 52 in high-velocity gate areas.
High filler content also changes capillary flow behaviour. Shear viscosity at 100 s⁻¹ and 230 °C for a 40 wt% talc-filled PP may range from 150–250 Pa·s when measured under ISO 11443:2021, compared with 80–140 Pa·s for a 20 wt% talc-filled grade. The higher viscosity reduces die swell and produces a flatter velocity profile, but it also increases pressure drop through long runner sections. Melt volume-flow rate under ISO 1133-1:2022 at 230 °C/2.16 kg is commonly 6–18 cm³/10 min for this class. Back pressure must be high enough to prevent unmelted mineral agglomerates, but excessive back pressure above 2.0 MPa can raise melt temperature by 5–10 °C through shear heating and consume cycle time. Check ring wear is accelerated by mineral filler, so non-return valve clearance should be inspected at intervals no greater than 50,000 cycles. Nozzle tips with tungsten carbide inserts reduce erosion at the gate interface when processing against textured or hardened mold inserts.
Replacing a 20 wt% talc-filled PP compound with an HT42-class 42 wt% mineral-filled grade alters tooling tolerances because the higher filler content reduces mold shrinkage and increases melt viscosity. The higher viscosity commonly requires a widening of gate thickness by 10–15% to prevent jetting; edge gates below 1.0 mm are generally unsuitable. In multi-cavity family tools, the reduced shrinkage of HT42 can produce overpacking of the first-filled cavities unless melt flow is balanced through runner cross-section changes or valve gate sequencing. Compared with a 20 wt% talc-filled PP having a density of 1.04–1.06 g/cm³, the 42 wt% class raises part mass by approximately 15–18% for identical geometry. This mass penalty is offset by a 25–35% increase in tensile modulus and a 20–30 °C improvement in heat deflection temperature. Specific heat and thermal conductivity increase modestly, which can extend cooling time by 10–15% in thick-walled bosses and ribs. Published data for the exact HT42 filler system is limited; therefore mold trials should be run with shrinkage gauges at three gate-to-boss distances before steel changes are finalized.
Under the European Union REACH Regulation (EC) No 1907/2006, the product must be covered by a valid safety data sheet. The polypropylene base should meet the generic designation system requirements of ISO 19069-1:2015; typical PP homopolymer and impact copolymer grades are classified as PP-H or PP-B. Under RoHS Directive 2011/65/EU Annex II, lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE are not expected in certified compounds. Flammability under UL 94 is generally HB for mineral-filled PP at typical part thicknesses, unless brominated flame retardants are included, which are not used in HT42. Chemical resistance to engine coolant, battery acid, and windshield washer fluid is acceptable for short-term exposure at 23–60 °C; however, long-term contact above 80 °C with hot mineral oil or fuel containing high aromatic content can soften the PP matrix and cause stress cracking at weld lines. Use in direct contact with food is governed by FDA 21 CFR 177.1520 for the polypropylene base and by specific mineral filler approvals; converters should confirm individual food-contact status because mineral-filled grades are not universally cleared.
Thin-wall air ducts and fan shrouds molded from HT42 have shown reduced bowing after paint bake cycles at 120 °C for 30 min, provided that the material is packed at pressures above 60 MPa and the mold temperature is not below 40 °C. In underhood acoustic covers, the higher modulus permits rib height reductions of 20–30% without sacrificing stiffness, but low-temperature impact at −30 °C must be validated under ISO 179-1:2010 because mineral-filled PP grades exhibit a ductile-to-brittle transition near 0 °C. Extended heat aging at 150 °C for 1,000 h in a forced-air oven under ISO 188:2011 may reduce tensile strength by 10–25%. Published data for this specific configuration is limited, so lot-specific testing is required for parts exposed to continuous underhood temperatures above 130 °C.