| HS Code | 207582 |
| Density | 1.12 g/cm³ |
| Melt Flow Rate | 4 g/10 min (230°C/2.16 kg) |
| Tensile Strength | 75 MPa |
| Flexural Modulus | 4500 MPa |
| Elongation At Break | 3% |
| Notched Izod Impact | 75 J/m |
| Heat Deflection Temperature | 130°C at 0.45 MPa |
| Vicat Softening Point | 160°C |
| Rockwell Hardness | R110 |
| Melting Point | 165°C |
| Glass Fiber Content | 30% |
| Drying Temperature | 80°C |
As an accredited MWR PPH Homopolymer 8100GC30 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | MWR PPH Homopolymer 8100GC30 is supplied in 25 kg woven polypropylene bags with liner, palletized and stretch-wrapped for safe transport and storage. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with MWR PPH Homopolymer 8100GC30, polypropylene homopolymer pellets in bags, securely stowed for safe transport. |
| Shipping | MWR PPH Homopolymer 8100GC30 ships as a non-hazardous polypropylene resin. It should be transported in clean, dry containers or lined woven bags, protected from moisture and direct sunlight. Handle gently to prevent bag tearing, and store away from heat, ignition sources, and incompatible materials. |
| Storage | Store 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 static charge buildup. Avoid contact with strong oxidizing agents. Maintain temperatures below 50°C (122°F) and protect material from mechanical damage to preserve its properties. |
| Shelf Life | Shelf life is typically 12 months from manufacture date when stored in dry, shaded, unopened conditions. |
Under-hood air-management parts molded from MWR PPH Homopolymer 8100GC30, specified as a 30% glass-fiber reinforced polypropylene homopolymer compound, are dimensionally checked against ISO 294-4 shrinkage plaques and heat-aged according to ISO 188 at 150 °C for 1,000 h; suppliers commonly impose a retained tensile strength of at least 80% after ageing for chemically coupled grades. Injection molding is performed on a tie-bar-less hydraulic machine with clamping force of 8,000 kN to 14,000 kN for a two-cavity fan shroud tool, using a general-purpose screw with a 20:1 L/D ratio and hardened non-return valve. Melt temperature is held between 230 °C and 250 °C at the nozzle; mold surface temperature is 30 °C to 50 °C with turbulent water circuits at a Reynolds number above 10,000. Desiccant drying at 80 °C for 2 h to 3 h reduces residual moisture to below 0.05 wt%; at relative humidity above 60%, the drying time is extended to 4 h. Higher residual moisture generates splay at hot gate lands and reduces weld-line tensile strength. Fiber orientation anisotropy across the part is measured by ASTM D955-21 on a 150 mm × 150 mm edge-gated slab, and gate locations are shifted to move weld lines away from blade retention bosses. The component must not be used in continuous immersion in hot inhibited glycol; sustained temperatures above 110 °C in coolant contact cause oxidative degradation of the PP matrix. End products in this segment include radiator fan shrouds, fan blade carriers, and intercooler duct support brackets.
First-generation recycled material from sprues and runners can be reincorporated up to 20 wt% without changing the heat deflection temperature according to ISO 75-2, but fiber length distribution shifts toward shorter fibers after each melt pass. Production-scale data from equivalent grades indicates that tensile strength measured by ISO 527-2 drops by approximately 5% per pass when regrind exceeds 20%. The injection unit should avoid screw rotation speeds above 60 min−1 after the feed throat, and back pressure should be limited to 0.3 MPa to 0.7 MPa hydraulic pressure to minimize fiber attrition. Tool steel in high-glass-fiber PP homopolymer production is maintained at 54 HRC or above at gate inserts and shut-offs; abrasive land wear in equivalent grades is commonly observed at 0.01 mm per 100,000 cycles.
In lithium-ion brushless power tools, the gear casing transmits stator clamp load and rotor bearing reaction forces; MWR PPH Homopolymer 8100GC30 is evaluated with ISO 527-2 tensile tests at 23 °C and 80 °C. The 80 °C modulus is relevant because gear casing temperature rises under continuous load in brushless tools. Mold flow simulation must incorporate Folgar-Tucker fiber orientation tensor closure, and the actual weld-line tensile strength should be measured on a double-gated ISO 527-2 Type 1A specimen; weld-line strength of glass-fiber PP homopolymer typically drops to 40% to 50% of bulk tensile strength. To mitigate this, tooling uses sequential valve-gate actuation with a 0.3 s gate delay and a melt cushion of 5 mm to 8 mm. Clamp force of 3,000 kN to 6,000 kN is used for single-cavity housings; a 40 mm diameter screw with a 22:1 L/D ratio is used to minimize fiber attrition. The material complies with UL 94 HB at 1.5 mm wall thickness, but it cannot be specified where IEC 60695-2-11 glow-wire ignition above 750 °C is mandated without a flame-retardant system. End products include angle grinder gear casings, hammer drill motor housings, and lawn trimmer clutch housings.
Batch-to-batch consistency is verified by ISO 1133-1:2022 melt flow rate at 230 °C and 2.16 kg; the value is used as a relative rheology check rather than an absolute molding parameter because glass fibers alter die swell and melt pressure. The injection unit should avoid screw rotation speeds above 60 min−1 after glass-fiber melt incorporation, as excessive shear reduces fiber length below the critical load transfer length and degrades tensile strength at 80 °C.
| Downstream segment | Normative reference | Critical process boundary |
|---|---|---|
| Under-hood air management | ISO 75-2:2013 method A, ISO 188, ASTM D955-21 | Melt 230–250 °C, residual moisture below 0.05 wt% |
| Power tool gear casings | ISO 527-2, ISO 179-1/1eA, UL 94 HB | Weld-line strength 40–50% of bulk; gate delay 0.3 s |
| Pump impellers | ISO 175, ISO 21940-11 G6.3 | Melt 240–260 °C, mold 30–60 °C |
| Appliance drum support | ISO 178, ISO 75-2 method A, ISO 899-2 | Creep modulus retention ≥60% at 60 °C/80% RH |
| Outdoor distribution boxes | IEC 60112, IEC 60695-2-11 | CTI >600 V; no UL 94 V-0 without FR |
| Structural foam pallet deck | ISO 8611-1:2021 | Melt 220–240 °C, nominal 30 wt% fiber maintained |
Chemical resistance testing according to ISO 175 under 30% ethylene glycol/water at 80 °C for 7 d is applied to pump impellers made from MWR PPH Homopolymer 8100GC30; allowable change in mass is typically below 1.0 wt% for dimensionally stable impellers. Fiber-filled PP homopolymers are specified for swimming-pool circulation pumps and light industrial transfer pumps where fluid pH stays between 5.5 and 8.5; strong mineral acids, chlorinated solvents, and high-pH cleaning solutions rapidly degrade the PP matrix and should be excluded. A central sprue gate or three-point diaphragm gate is used to align glass fibers radially from the hub to the blade tips, reducing imbalance caused by anisotropic shrinkage. Processing requires a melt temperature of 240 °C to 260 °C and a mold temperature of 30 °C to 60 °C; lower mold temperatures cause premature freeze-off at blade edges and generate high residual stress at the hub-to-blade junction. The impeller is balanced to G6.3 per ISO 21940-11, but post-mold machining is limited because glass fibers cause abrasive tool wear at the hub bore; carbide-insert boring and reaming at 0.1 mm depth of cut are used instead of high-speed steel. Published data for this specific configuration is limited; proof testing on a dedicated hydraulic test loop at 100% of maximum rated flow is required before production release.
In front-load washing machines, a structural drum support molded from MWR PPH Homopolymer 8100GC30 must maintain flexural creep modulus under prolonged wet and warm loading. ISO 178 flexural modulus at 23 °C and ISO 75-2 method A HDT are baseline, but the critical test is ISO 899-2 flexural creep at 60 °C and 80% RH for 1,000 h; creep modulus retention below 60% of initial modulus disqualifies the material for spin speeds above 1,400 min−1. The compound is processed with a melt temperature of 230 °C to 250 °C and a mold temperature of 40 °C to 60 °C; the tool uses six valve-gated drool-free hot runners to eliminate cold sprue. Differential shrinkage between along-flow and cross-flow directions is typically 0.004 mm/mm versus 0.008 mm/mm for 30% glass-fiber PP at 2.5 mm wall; tool compensation is based on ASTM D955-21 data, not unfilled PP values. The component is assembled with a cast aluminium spider through M8 bolts tightened to 25 N·m; washer face inserts are required because glass-filled PP homopolymer exhibits creep under point loading above 20 MPa. Sharp internal radii below 0.5 mm are avoided because the notch sensitivity of glass-filled PP homopolymer leads to impact crack initiation at the drum spider interface. End products include drum supports, transit bars, and pump mounting brackets.
Humidity aging at 80% RH and 60 °C shifts the failure mode from matrix yielding to interface debonding along fiber ends; scanning electron microscopy of fractured samples shows fiber pull-out lengths below 0.2 mm in coupled systems, while uncoupled or hydrolytically aged material shows pull-out lengths above 0.5 mm. This distinction is used as an incoming material control check after raw resin batches. The glass transition of PP homopolymer is near 0 °C, so low-temperature impact testing by ISO 179-1/1eA at −20 °C is also applied for transit bar components.
For outdoor low-voltage distribution boxes, MWR PPH Homopolymer 8100GC30 is evaluated for tracking resistance according to IEC 60112; comparative tracking index values above 600 V are commonly specified for unfilled PP homopolymer, but glass-fiber surface regions can reduce CTI below that level if fiber-rich skin layers are exposed at the surface. The critical test is IEC 60695-2-11 glow-wire at 650 °C or 750 °C for 30 s; glass-filled PP homopolymer without flame retardant typically cannot reach a glow-wire ignition temperature of 850 °C without a brominated or intumescent system, so applications must be limited to enclosures with no live-part contact and no UL 94 V-0 requirement. Processing uses a clamp force of 12,000 kN to 18,000 kN for a four-cavity family mold; a sequential valve-gate system is needed to prevent weld-line cracking at hinge bosses. The tool steel must be hardened to 54 HRC minimum because glass fiber abrasion at gate inserts increases land wear by 0.01 mm per 100,000 cycles. End products include IP65 outdoor meter boxes, cable distribution pits, and DIN rail enclosures; UL 94 V-0 compliance must be revalidated on the final wall thickness if a flame-retardant variant is introduced.
Thermal endurance is often specified by UL 746B relative thermal index at mechanical and electrical loading; for glass-filled PP homopolymer, RTI values of 65 °C to 90 °C are typical, but the specific 8100GC30 grade must carry a supplier yellow-card value before design acceptance. Without that value, designers must derate continuous operating temperature to 50 °C in direct contact with busbar brackets.
MWR PPH Homopolymer 8100GC30 is used in structural foam injection molding of load-bearing pallet decks where glass fiber increases flexural modulus and reduces sag under 1,000 kg racking loads. ISO 8611-1:2021 defines warehouse pallet load tests; a 30% glass-fiber PP homopolymer deck is tested in a three-point racking configuration at 1.25 R rated load for 24 h, with maximum residual deflection limited to 10 mm. The material is processed on a low-pressure structural foam press with an accumulator-assisted injection unit; nitrogen gas is metered at 0.3 wt% to 0.5 wt% into the melt, and the nominal fiber content of the 8100GC30 grade is maintained at 30 wt%. If lower fiber content is required, unfilled PP homopolymer is dry-blended at the press, but resulting mechanical properties must be revalidated against ISO 178 and ISO 179-1/1eA. Melt temperature is kept at 220 °C to 240 °C to minimize gas dissolution disturbance; higher temperatures reduce the gas concentration limit and produce non-uniform cell structure. Because glass-fiber PP homopolymer has relatively low weld-line elongation, the mold uses full-length flow channels and avoids insert pins at high-stress rib intersections. End products include one-piece four-way entry pallets, sleeve-pack bases, and reusable external logistics crates, where single-material construction is governed by EU Directive 94/62/EC packaging waste requirements.
Injection compression molding has replaced conventional structural foam in some pallet tools because it reduces surface splay and allows lower clamping force; when the 8100GC30 grade is used in injection compression, the tool closes from 2.5 mm to 1.5 mm after the melt is injected, and fiber orientation becomes more isotropic across the part. The main failure mode in service is side-edge denting, not mid-span bending; that requires edge rib thickness above 4 mm and a rib root radius above 1 mm.
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MWR PPH Homopolymer 8100GC30 is classified as a 30% glass fibre reinforced polypropylene homopolymer compound in which the glass reinforcement is chemically coupled to the matrix. The model designation encodes the polymer type—PPH, for polypropylene homopolymer—and the reinforcement level and coupling characteristic, 8100GC30, where GC indicates glass-coupled rather than simply glass-filled. The product is supplied as cylindrical pellets for injection moulding and, with appropriate screw configuration, profile extrusion. The homopolymer matrix contains no ethylene-propylene rubber phase; as a result, stiffness, short-term heat resistance, and surface hardness are higher than those of 30% glass-filled impact copolymer equivalents, but low-temperature ductility is reduced. The compound is intended for structural and semi-structural applications requiring dimensional stability under load, resistance to aqueous and many inorganic chemical environments, and a melt-processable alternative to metal or engineering thermoplastics in non-lubricated moving components. Representative end-use areas are pump and valve housings, fan shrouds, structural brackets, electrical enclosure frames, and appliance structural supports where continuous service remains below 90°C. Because the material is not hygroscopic, controlled lot handling commonly avoids mandatory drying; however, sacks stored at relative humidity above 60% should be dried at 80°C for 2 h to 4 h before processing to prevent surface splay. Certificates of analysis control lot-level properties rather than nominal datasheet values.
The primary differentiator in 8100GC30 is the chemical nature of the glass–matrix interface. In non-coupled glass-filled polypropylene, the glass surface is coated only with a conventional sizing; stress transfer between the polymer and the fibre is limited, and tensile failure occurs partly by fibre pull-out. In a coupled system, an organosilane or equivalent coupling treatment creates covalent or strong associative bonding across the interface. Test evidence under ISO 527-2 on coupled 30% glass-reinforced PP homopolymer compounds in this class shows tensile stress at break in the 80 MPa to 95 MPa range, whereas non-coupled compounds of equal filler loading commonly fall 15% to 25% lower. The coupled interface also raises fatigue resistance under cyclic tensile load and reduces interfacial moisture wicking at exposed glass ends. Published data for this specific configuration is limited to manufacturer material datasheets; the following values are representative for the glass-coupled 30% PP homopolymer compound class and should be replaced by certificate-of-analysis values for controlled production.
| Property | Test standard | Typical envelope |
|---|---|---|
| Density | ISO 1183-1 | 1.11–1.14 g/cm³ |
| Melt flow rate, 230°C, 2.16 kg | ISO 1133-1 | 4–10 g/10 min |
| Tensile stress at break | ISO 527-2 | 80–95 MPa |
| Tensile modulus | ISO 527-2 | 5,500–6,500 MPa |
| Flexural modulus | ISO 178 | 5,600–6,400 MPa |
| Heat deflection temperature, method A, 1.8 MPa | ISO 75-2 | 150–158°C |
| Notched Charpy impact, 23°C | ISO 179-1/1eA | 7–10 kJ/m² |
| Moulding shrinkage, in flow | ISO 294-4 | 0.2–0.4% |
Tensile modulus under ISO 527-2 and flexural modulus under ISO 178 place the material above standard 20% glass-filled PP homopolymer, which typically exhibits flexural modulus near 3,800 MPa to 4,500 MPa, and below 40% glass-filled PP, which can exceed 7,500 MPa but suffers higher melt viscosity and mould abrasion. The 30% reinforcement level therefore represents an intermediate balance between stiffness and processability. The heat deflection temperature under ISO 75-2 method A is governed primarily by the homopolymer crystal phase rather than the fibre content alone; ethylene-propylene rubber in impact copolymer grades depresses heat deflection temperature by roughly 10°C to 20°C. The notched Charpy impact values are adequate for room-temperature structural housings but should not be extrapolated to sub-zero environments without component testing, since fracture becomes increasingly brittle with decreasing temperature.
In chemical pump housings and water-handling components, the replacement of die-cast aluminium is technically justified when the service environment contains chlorinated water, aqueous inorganic salts, or weak acids at temperatures below 80°C. Polypropylene homopolymer does not undergo electrolytic corrosion, and the glass-reinforced grade provides creep resistance under hydrostatic pressure. The design must, however, be validated against the creep modulus of the specific moulded lot because fibre length distribution after injection moulding varies with screw design and gate geometry. Short-term heat deflection temperature under ISO 75-2 is not an acceptable substitute for long-term creep testing under ISO 899-2; creep strain at 80°C and 20 MPa hoop stress is strongly dependent on fibre orientation and weld-line placement. Aluminium replacement also lowers component mass: glass-filled PP homopolymer density is approximately 1.12 g/cm³ under ISO 1183-1, compared with approximately 2.7 g/cm³ for aluminium alloy, although the polymer component requires thicker wall sections to compensate for lower tensile modulus under ISO 527-2. Corrosion testing should follow ISO 22088-3 or equivalent constant-strain immersion methods when the housing is exposed to oxidizing acids or chlorinated solvents, because concentrated nitric acid and halogens attack polypropylene. In such cases, fluoropolymer liners or alternative materials are required.
Below 0°C, the homopolymer matrix transitions from ductile yielding to brittle crack propagation. Notched Charpy impact under ISO 179-1/1eA at -30°C for 30% glass-filled PP homopolymer compounds in this class is typically below 6 kJ/m², whereas a 30% glass-coupled PP impact copolymer can remain above 10 kJ/m² at the same temperature. The selection of 8100GC30 therefore prioritises stiffness and heat resistance over sub-zero impact. For fan shrouds, brackets, and housings operating between 0°C and 90°C, this trade-off is generally acceptable. For applications subject to winter impact, such as external automotive body attachments or cold-climate fluid reservoirs, an impact copolymer grade or an unreinforced high-impact PP is technically preferable. Weld lines in glass-reinforced homopolymer mouldings can reduce tensile strength by 30% to 50% compared with unwelded material under ISO 527-2, and the reduction is magnified at low temperature. Component design should therefore place weld lines away from primary tensile stress paths or validate weld-line specimens cut perpendicular to the knit line.
Prolonged exposure of glass-coupled polypropylene homopolymer to barrel temperatures above 260°C initiates chain scission in the polypropylene backbone. The resulting molecular weight loss lowers melt viscosity and reduces tensile strength under ISO 527-2 even when visible discoloration is absent. Processing should therefore maintain a nozzle melt temperature of 230°C to 260°C, with a rear zone at 220°C, middle zones at 240°C to 250°C, and a nozzle at 240°C to 255°C. Barrel residence time above 250°C should not exceed 5 min; interrupted production should be purged with a low-melt-flow unfilled PP homopolymer under ISO 1133-1 MFR 2 g/10 min to 4 g/10 min. Screw configurations with L/D ratios of 20:1 to 24:1 and compression ratios of 2.2:1 to 2.5:1 are appropriate for glass-filled PP; high-compression general-purpose polyolefin screws can over-attrite glass fibre and reduce median fibre length below 0.2 mm, which degrades coupled interfacial load transfer. A hardened steel screw, barrel, and tip with a free-flow non-return valve are required because glass fibre abrades nitrided surfaces. Injection pressure typically falls within 80 MPa to 120 MPa, with hold pressure at 60% to 80% of the injection pressure and a mould temperature of 30°C to 80°C. Higher mould temperatures improve dimensional stability and surface resin-richness but extend cycle time.
Fibre orientation in the moulded part is anisotropic; shrinkage under ISO 294-4 in flow direction is typically 0.2% to 0.4%, while cross-flow shrinkage may be 0.6% to 0.9%. Gate location, runner diameter, and packing time exert more influence on post-moulding warpage than barrel temperature at these fibre loadings. Hot runner tips should have a bore diameter of at least 1.4 mm, and full-round gates are preferred; sharp-edge gates generate fibre breakage and jetting. For production-scale injection moulding, cavity pressure sensors are recommended because the relatively low viscosity of glass-filled homopolymer PP under high shear can create short-shot or flash transitions within 10 MPa cavity pressure variation. Component walls should be uniform; rib thickness should not exceed 60% of the attached wall thickness to avoid sink and internal voiding at the glass-rich core. Machine clamp force must exceed projected area multiplied by cavity pressure; cavity pressure for 30% glass-filled PP is typically 30 MPa to 50 MPa. For a projected area of 250 cm², a clamp force of approximately 1,250 kN is therefore the minimum predicted by this relationship, but hot-runner and injection-pressure losses require a practical machine margin.
Compliance status under the European Union RoHS Directive 2011/65/EU and amending directive (EU) 2015/863 is typically maintained for this compound class with cadmium below 100 mg/kg, lead below 1,000 mg/kg, mercury below 1,000 mg/kg, hexavalent chromium below 1,000 mg/kg, polybrominated biphenyls and diphenyl ethers below 1,000 mg/kg, and restricted phthalates below 1,000 mg/kg. REACH candidate list declarations require confirmation per production lot because coupling agents and glass sizings are proprietary. The base polypropylene homopolymer may satisfy FDA 21 CFR 177.1520 for olefin polymers in food-contact applications; however, glass fibre, sizing, and processing aids in this filled grade require end-use migration testing under FDA 21 CFR 177.1520 and appropriate food-contact conditions. Chemical incompatibilities include concentrated oxidizing acids such as nitric acid, halogens, and aromatic or chlorinated solvents at elevated temperature. The material is hydrolytically stable; water absorption under ISO 62 at 23°C for 24 h is below 0.1%, and this low moisture uptake makes it suitable for humid environments. Exposed glass ends at machined or cut surfaces can still wick moisture along the fibre interface, so cut edges should be sealed or redesigned away from wet service where possible. For outdoor use, UV stabilization is required because glass-filled PP without carbon black or hindered amine stabilizer embrittles under extended ultraviolet exposure.