| HS Code | 628157 |
| Density | 0.905 g/cm³ |
| Melt Flow Rate | 12 g/10 min (230°C/2.16 kg) |
| Tensile Strength At Yield | 35 MPa |
| Elongation At Yield | 12% |
| Flexural Modulus | 1500 MPa |
| Notched Izod Impact Strength | 3.5 kJ/m² |
| Heat Deflection Temperature 0 45 Mpa | 100°C |
| Vicat Softening Point | 155°C |
| Melting Point | 165°C |
| Rockwell Hardness | R100 |
As an accredited Polypropylene PP 1080 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Polypropylene PP 1080 is supplied in 25 kg heat-sealed woven polypropylene bags with moisture-barrier lining, palletized and shrink-wrapped. |
| Container Loading (20′ FCL) | 20′ FCL: 25 metric tons of Polypropylene PP 1080 in 25 kg bags, palletized, shrink-wrapped, and securely loaded. |
| Shipping | Polypropylene PP 1080 is shipped as non-hazardous plastic granules/pellets, typically in woven polypropylene bags or FIBC bulk bags. It is not regulated as dangerous goods under IMDG/ADR, but keep dry, avoid high heat, open flames, and dust accumulation. Ensure proper labeling and consult the SDS before transport. |
| Storage | Store Polypropylene PP 1080 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. Maintain ambient temperatures, avoid stacking excessively, and ensure no contact with strong oxidizing agents. Follow local regulations and keep away from drains. |
| Shelf Life | Polypropylene PP 1080 has an indefinite shelf life when stored in a cool, dry, shaded area, protected from moisture and UV radiation. |
On high-cavitation closure lines, PP 1080 is processed as a general-purpose isotactic homopolymer with a nominal melt flow rate of 8.0 g/10 min per ISO 1133-1:2022 at 230°C/2.16 kg. Hot runner tools of 32 or 64 cavities are run on toggle machines of 1,200 kN to 2,200 kN clamp force, with the barrel rear zone held at 200°C, the centre zone at 220°C, the front zone at 230°C, and the nozzle at 225°C. The screw selected is a general-purpose PP profile with L/D 20:1, a compression ratio of 2.5:1, and a check ring with 3 mm axial stroke. Excessive wear on the check ring creates shot-weight drift and cap thread short-shot. Valve gates are preferred over open hot tips to avoid stringing and to deliver a round sub-gate land of 0.8 mm to 1.2 mm. The mould coolant temperature is held at 18°C to 28°C, because cycle time in closures is gate-freeze limited rather than part-cooling limited. Injection speed is set as a fill-time target of 0.2 s to 0.5 s for a 2.8 g to 3.5 g cap, producing apparent wall shear rates above 5,000 s⁻¹ at the gate. Hold pressure of 50 MPa to 70 MPa is applied for 0.8 s to 1.4 s. Pressure decay from the gate to the thread root must be small enough to eliminate sink, but excessive packing increases ejection force and thread root cracking. Mould-open and ejection are sequenced so that the part cools below 75°C before the stripper plate separates the thread from the core. Cap deck thickness is 1.0 mm to 1.3 mm, the tamper band hinge zone is 0.30 mm to 0.40 mm, and the thread root radius is not allowed below 0.15 mm. For threaded closure applications, production-scale torque audits are run on a Mettler Toledo or equivalent torque meter. Variation in application torque beyond ±0.3 N·m in a 24 h cap-on-bottle test is typically traceable to post-mould shrinkage, neck finish ovality, or insufficient cooling of the tamper band. PP 1080 exhibits homopolymer creep; at elevated warehouse storage above 40°C, closure back-off torque declines faster than for impact copolymer grades. Sealing tests on carbonated necks are therefore not specified as a simple cap-only property but must be validated with the actual bottle finish under carbonation pressure of 0.4 MPa to 0.6 MPa for the target shelf life. The material is not recommended for hot-filled closures above 85°C or for closure systems requiring continuous rubber-seal compression above 60°C, because creep and stress relaxation create measurable loss of sealing residual stress. Pre-drying is unnecessary for resin stored below 60% RH. After exposure to condensation or high humidity, drying at 80°C for 2 h in a desiccant dryer is used to avoid splay on the deck surface. Purge with a general-purpose PP of similar MFR after colour changes. Do not purge with polycarbonate or nylon at high temperature because residue can delaminate or create contamination in the hot runner.
The thin-wall food container regime is defined by a nominal wall of 0.6 mm to 0.9 mm and a flow length from sprue to last fill point of 100 mm to 200 mm. For PP 1080, the practical flow-length-to-wall-thickness ratio on a cold runner is approximately 180:1, and on a hot runner with sequential valve gates it may reach 220:1. Published data for this specific configuration is limited, so tool trials are required before locking cavity count. The limiting factor is not melt temperature alone but the rapid formation of a frozen skin against the mould wall. With a mould temperature of 20°C to 35°C, the frozen layer occupies a meaningful fraction of the cross-section before the flow front reaches the end of cavity. Where the gate is a film-edge gate 0.4 mm to 0.6 mm thick, gate freeze time is between 0.4 s and 0.8 s. Hold pressure applied after gate freeze cannot compensate for volumetric shrinkage in the panel area. Two-stage injection velocity is used: a fast fill at 250 mm/s to 400 mm/s screw speed to the short-shot point, then a controlled transition to packing at 40 MPa to 60 MPa cavity pressure. Cavity pressure sensors are installed behind the last-fill corner. Transfer from velocity to pressure is triggered at 80% to 90% of final part weight, not by screw position alone. In-flow and cross-flow shrinkage differ because the oriented skin layer is highly anisotropic. A rectangular container lid or tray therefore warps if the gate is placed at one end. The narrow centre of a rectangular lid is often gated by a fan gate or edge gate along the long side to shrink uniformly. Post-mould warpage is inspected on a granite surface plate after 24 h. The flatness limit for a 180 mm tray is typically 1.5 mm, depending on film sealing equipment. Food compliance must be established by the moulder and converter. PP 1080 in food-contact uses is evaluated under FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011, with an overall migration limit of 10 mg/dm² in aqueous food simulants. The resin as supplied should be free of heavy metals per RoHS Directive 2011/65/EU and REACH SVHC lists. The processor must still verify no contaminant from masterbatch, regrind, or hot-runner lubricant. Because PP 1080 is a homopolymer, the finished container has greater stiffness and lower drop impact than a random copolymer. Thin-wall containers shipped to frozen-food chains may crack at -18°C, so cold-chain use requires pre-qualification. Barrier properties are poor: oxygen transmission through 0.7 mm PP exceeds typical EVOH barrier layers by orders of magnitude. PP 1080 trays are therefore suitable for short shelf-life fresh produce, bakery, or dry snacks, not for oxygen-sensitive products. Direct printing on the deck is possible after corona treatment at 42 dyn/cm. Without surface treatment, ink adhesion is inadequate. Regrind addition up to 20% by weight is common when tray weight and dimensions are stable, but repeated heat history increases MFR and reduces impact.
During stackable houseware production, PP 1080 is ejected from the mould only after the corner temperature has fallen below 75°C. Parts such as storage boxes, drawer trays, and refuse-bin lids have nominal walls from 1.8 mm to 2.5 mm, with bases that are flat within 0.8 mm over 300 mm if the mould temperature is uniform within ±5°C. The cooling time is set in proportion to the square of wall thickness. For a 2.0 mm wall, the required cooling time before demoulding is usually 10 s to 14 s. Ejection too early creates corner distortion that cannot be corrected by post-mould cooling jigs. The rib root thickness is held at 0.45 to 0.50 times the adjacent wall to avoid visible sink marks on the outside of the stackable wall. Rib spacing is not a substitute for adequate draft. Side walls are drafted at 1.0° to 1.5°, and textured surfaces require an additional 0.5° per 0.025 mm of texture depth. Tensile modulus of a typical PP 1080 lot is near 1,500 MPa when measured by ISO 527-2:2012. Flexural modulus is near 1,450 MPa under ISO 178:2019. Notched Izod impact of an unfilled homopolymer is low, commonly in the range of 2.5 kJ/m² to 4.0 kJ/m² at 23°C per ISO 180:2023. The grade is therefore not selected for thin-wall luggage or toy wheels. For a stackable storage box, the top-load test is performed on a universal testing machine with a flat platen at 10 mm/min. Failure is usually buckling of the side wall or corner splitting at the gate. Quality improvement comes from reducing gate stresses: a tab gate of 1.2 mm to 1.8 mm depth is used instead of a pin gate because the larger gate area reduces frozen-in stress near the injection point. Housewares requiring a living hinge are not made from PP 1080. The homopolymer chain structure has insufficient repeated flexural fatigue resistance, and hinge failure occurs after a few hundred flex cycles. If a hinge is unavoidable, a random copolymer or impact copolymer grade with high hinge performance is used.
Appliance control panel carriers and small enclosure bodies moulded from PP 1080 usually have nominal wall sections of 2.0 mm to 2.5 mm. The limiting cosmetic defect is sink opposite a fixing boss. Boss outer diameter is sized at 2.0 to 2.5 times the screw boss inner diameter, and the boss wall thickness is kept near 0.6 mm to 0.9 mm. Connecting ribs to the boss must be 0.45 to 0.55 of the adjacent wall. Thicker ribs cause sink on the show surface after cooling, not because the material is weak but because the local volumetric shrinkage is twice that of the thinner rib root. Packing pressure is profiled in two stages: the first stage at 55 MPa for 2.5 s fills the boss and rib junction, and the second stage at 35 MPa for 1.5 s prevents overpacking near the gate. Overpacking creates residual stress that shows as white marks at the gate or as delayed warpage after annealing in the customer’s paint oven. Flame-retardant versions are not assumed. PP 1080 as supplied is a non-flame-retardant homopolymer and typically achieves UL 94 HB at 3.0 mm thickness. For electrical insulating properties, the comparative tracking index of polypropylene is commonly reported above 600 V under IEC 60112:2020, but the exact value for a given lot must be confirmed by the supplier because contaminants and colour concentrates influence leakage current. Continuous service temperature is constrained by heat distortion temperature. A typical value for a homopolymer of this MFR is 90°C to 100°C at 0.45 MPa under ISO 75-2:2022. Internal ribs in airflow shrouds are gusseted at 45° to reduce turbulence-induced vibration. The grade is not used for high-temperature fan impellers above 100°C because creep modulus declines. Published data for laminated or painted PP 1080 appliance panels is limited. Adhesion of UV-cured coatings requires surface activation and validation of cross-hatch adhesion per ISO 2409:2020 after thermal cycling from -20°C to 60°C.
The replacement of impact copolymer with PP 1080 in rigid pails is only valid for low-margin, light-duty dry goods packaging. At 23°C, a 1.5 kg to 3.0 kg pail with wall thickness 1.8 mm to 2.2 mm may survive a drop height of 0.8 m, but the test outcome is strongly influenced by gate placement, regrind content, and part temperature. At 0°C, homopolymer PP 1080 loses impact toughness rapidly. Filled drop tests at -10°C commonly fail through corner cracking or handle root fracture. The standard selected for shipment validation is ISTA 1A or the customer-specific drop protocol, with failure defined as pail body crack, bottom weld-line split, or lid release. Weld lines are a critical variable because the two flow fronts meeting near the handle boss form a low-angle knit line. The mould must be gated from the pail centre bottom with a diaphragm gate to produce a radial flow front. The handle attachment is not a living hinge. Separate injection-moulded handles or metal wire handles are preferred because PP 1080 cannot sustain repeated flexural loading. Stacking load is tested with a static top load of 250 N to 400 N on the lid-rim contact area for 24 h at 40°C. Permanent deformation greater than 1.5 mm is rejected. The lid gasket seat must be flat. A support rib under the rim is 0.8 mm thick and spaced at 25 mm to 35 mm intervals to balance stiffness without sink. For outdoor or UV-exposed storage, PP 1080 must be stabilized with hindered amine light stabilizers and carbon black masterbatch. The unstabilized grade will degrade in direct sunlight and lose surface gloss and molecular weight. The material is not suitable for pails carrying strong oxidizing agents, chlorinated solvents, or hot liquids above 70°C. Drying before processing is generally not required below 60% RH, but regrind containing moisture from wash lines must be dried at 80°C for 2 h to prevent splay and bubbles at the gate area. Drop-test data for PP 1080 in pails with 50% regrind is not always available. Production trials with the specific part shape are required before commercial substitution.
| Sector | Regulation or Standard | Key Requirement | Testing Condition |
|---|---|---|---|
| Food-contact closures and thin-wall packaging | FDA 21 CFR 177.1520 | Olefin polymer indirect and direct food additive requirements | Extractives and migration depending on food type |
| EU food-contact articles | Regulation (EU) No 10/2011 | Overall migration limit | 10 mg/dm² |
| Children’s products or stationery with toy classification | EN 71-3:2019+A1:2021 | Migration of certain elements | Limit values by element, aqueous extraction |
| Electrical enclosure insulation | IEC 60112:2020 | Comparative tracking index | Reported value, lot-specific |
| Flame resistance | UL 94 | HB classification | 3.0 mm |
| Global substance compliance | REACH 1907/2006, RoHS 2011/65/EU | SVHC and restricted substances | Supplier declaration |
In office-article moulding, PP 1080 is selected only where flexural fatigue is intermittent and low-temperature drop impact is not the primary specification. File trays, pencil holders, document sorters, and non-return magazine files use the grade for stiffness and dimensional stability under light loads. Nominal wall thickness is 2.0 mm to 2.5 mm, and the flatness requirement for a free-standing document tray is 1.0 mm over a 350 mm length after 24 h conditioning at 23°C/50% RH. The tool surface is textured to VDI 24 to VDI 27. Polished surfaces show flow lines more readily when the melt temperature is below 230°C. Soft-touch or elastomeric overmoulding is not recommended for PP 1080 because the low surface energy requires adhesive or plasma treatment to achieve peel strength above 2 N/mm in a two-shot process. Welding of inserts by ultrasonic or hot-plate methods uses horn amplitudes and weld times that must be tuned for homopolymer PP. Hot-plate temperature of 220°C to 240°C and weld time of 4 s to 8 s produce acceptable bond strength for non-structural joints. The material is suitable for laser marking at low speed, but contrast is lower than on ABS or polyamide unless a marking additive is added. In products likely to be handled by children, compliance is validated against EN 71-3:2019+A1:2021 for elemental migration and against REACH 1907/2006 for SVHC content. The limiting property is not tensile strength but brittle failure at the gate under dropping onto hard floors. A desktop accessory dropped from 1.0 m at 5°C may crack at the injection gate or at a sharp corner. Increasing wall thickness beyond 2.5 mm improves impact only marginally and creates sink marks and long cycle times. PP 1080 is used for low-fall-risk, lightly loaded interior products, not for school boxes or portable tool cases that require copolymer impact resistance. Moulds with direct edge gates and hot tips are preferred over tunnel gates in dark-coloured parts to minimize gate loss and cold-slug marks. The use of regrind from sprues and runners is limited to 15% to 20% because higher amounts shift the MFR and lead to short-shot variations on large flat trays.
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Polypropylene PP 1080 is an isotactic polypropylene homopolymer grade supplied as cylindrical pellets for injection moulding and compounding. The grade is part of the 1000-series polypropylene grades, where the numerical designation denotes a medium-flow injection-moulding window rather than an absolute melt-viscosity value. At 230 °C under a 2.16 kg piston load, the melt flow rate measured to ISO 1133-1:2022 is typically 8–10 g/10 min. Solid-state density determined by ISO 1183-1:2019 is 0.90–0.91 g/cm³. Differential scanning calorimetry at a cooling rate of 10 K/min gives a crystallisation peak of 112–118 °C and a melting peak of 160–165 °C when tested to ISO 11357-3:2018. The xylene-soluble fraction measured by ISO 16152:2005 is typically 4–6 %, which separates PP 1080 from heterophasic impact copolymers that often exceed 10 % xylene-soluble content.
For the end-user, the resin is specified where a balance of fast filling, adequate rigidity, and reproducible shrinkage is required in caps, closures, thin-walled containers, housewares, and small appliance components. Published data for this specific designation is limited; lot-specific certificates should supersede representative values in any production specification.
Compared with a 2–4 g/10 min homopolymer, PP 1080 exhibits a lower apparent shear viscosity at 1000 s⁻¹ and 230 °C, generally in the range 60–90 Pa·s when measured by capillary rheometry according to ISO 11443:2021. In a 24-cavity hot-runner cap mould with 0.7 mm nominal wall thickness, the practical effect is a hydraulic injection-pressure reduction of approximately 15–25 % relative to a 3 g/10 min grade at the same melt temperature. The lower viscosity reduces clamp-force demand for a given projected area; however, post-mould shrinkage is greater than low-flow grades. Shrinkage measured after 24 h at 23 °C and 50 % RH according to ISO 294-4:2018 typically falls between 1.2 % and 1.6 % in the flow direction. Lower-flow homopolymers may show 0.2–0.4 % lower shrinkage, and elastomer-modified copolymers may display more anisotropic shrinkage because dispersed rubber-phase orientation alters local volume relaxation.
Injection moulding of PP 1080 on reciprocating-screw machines with screw diameters from 25 mm to 40 mm and L/D ratios of 20:1 to 24:1 commonly uses a barrel temperature profile of 200 °C in the feed zone, 210 °C in the compression zone, 220 °C in the metering zone, and a nozzle temperature of 220–230 °C. Screw speed is maintained between 80 rpm and 120 rpm; back pressure is held between 0.5 MPa and 1.5 MPa. Melt temperature should remain above 210 °C for thin-wall fill and below 250 °C to avoid chain scission and yellowing. Mould temperatures between 20 °C and 35 °C are sufficient for functional parts; for high-gloss closures and grained surfaces, a mould temperature of 40–50 °C reduces flow marks. Holding pressure is commonly 50–70 % of peak injection pressure, with holding time of 4–8 s per 1 mm of nominal wall thickness. If lot-to-lot melt flow rate shifts by 2 g/10 min, filling pressure can change by approximately 10–15 %; processors should verify the certificate value before converting a new batch.
For high-speed thin-wall conversion, a general-purpose polyolefin screw with a compression ratio of 2.0:1 to 2.5:1 and a check ring with a radial clearance below 0.05 mm maintains shot-to-shot consistency. If the non-return valve leaks, cushion control becomes unstable, and short shots can occur even when the barrel temperature profile is correct. Cushion length is normally held at 2–5 mm. Shot volume should not exceed 70 % of maximum barrel capacity to limit residence time; residence time at melt temperature above 230 °C should be kept below 10 min to avoid upward MFR drift.
The property envelope below represents medium-flow polypropylene homopolymers with a melt flow rate of 8–10 g/10 min. These values are not a substitute for lot-specific certificates, but they provide a basis for comparison with lower-flow homopolymers and higher-impact copolymers.
| Property | Typical value | Test method |
|---|---|---|
| Tensile stress at yield, 50 mm/min | 32–35 MPa | ISO 527-2:2012, type 1A |
| Tensile elongation at yield | 8–12 % | ISO 527-2:2012, type 1A |
| Flexural modulus, 2 mm/min | 1250–1500 MPa | ISO 178:2019 |
| Notched Charpy impact, 23 °C | 2.5–4.0 kJ/m² | ISO 179-1:2020/1eA |
| Notched Charpy impact, -20 °C | 1.0–1.8 kJ/m² | ISO 179-1:2020/1eA |
| Heat deflection temperature, 0.45 MPa | 85–95 °C | ISO 75-2:2013, method B |
| Vicat softening temperature, A50 | 150–155 °C | ISO 306:2022 |
| Mould shrinkage, flow direction | 1.2–1.6 % | ISO 294-4:2018 |
Impact-modified heterophasic copolymers at the same flexural modulus can show notched Charpy values at 23 °C in the range 10–25 kJ/m²; PP 1080 is therefore not specified for cold-temperature impact service or automotive exterior parts without additional compounding. The grade's modulus supports rigid articles that require dimensional stability under load at ambient temperatures, but elongation at yield is relatively low, and the ductile-to-brittle transition is near 0 °C.
If a tool has flow-path-to-wall-thickness ratios exceeding 250:1, short shots and warpage become process-critical. For a 0.6 mm wall container, PP 1080 typically requires a melt temperature of 230–240 °C at the nozzle and a filling velocity at or above 120–150 mm/s. Hydraulic injection pressure on a 32 mm screw machine can reach 90–110 MPa. If the hot-runner manifold is not independently zoned, tip-to-tip temperature variation above 5 °C can produce fill imbalance across 32 cavities; this is a known production bottleneck on valve-gated systems. The polymer's thermal conductivity is approximately 0.20 W/(m·K), so cooling time is controlled by wall-thickness squared rather than by melt temperature alone. A cooling-time estimate for a 0.8 mm wall part at a mould temperature of 30 °C is 4–6 s based on transient heat-transfer calculations for semicrystalline polypropylene. If cycle time is pushed below the ejection temperature limit, parts may exhibit sink marks, warpage, or buckling at the gate. Dimensional acceptance should be checked after 48 h because post-mould crystallisation can shift shrinkage by 0.1–0.3 %.
For food-contact applications, compliance is established under EU Regulation (EU) No 10/2011 and FDA 21 CFR 177.1520 for olefin polymers. The resin is not intrinsically approved for all food types; the finished article must be migration-tested under the intended simulant and time-temperature conditions specified in Annex III and Chapter IV of EU 10/2011. The overall migration limit for plastic food-contact materials is 10 mg/dm², or 60 mg/kg for infant foods. Under FDA 21 CFR 177.1520(c), polypropylene homopolymer may be used in contact with food in accordance with the extractables limitations in 177.1520(c)(1) and (2). If PP 1080 is used in microwave reheat containers, users should verify heat-distortion limits and conduct sensory screening because volatile degradation products can form above 200 °C under extended heating. Supplier compliance certificates are required for REACH SVHC screening and for RoHS Directive 2011/65/EU.
| Regulatory framework | Relevant reference | Scope relevant to PP 1080 |
|---|---|---|
| EU food-contact plastics | EU 10/2011 | Overall migration limit 10 mg/dm²; specific migration limits apply |
| US food-contact olefin polymers | 21 CFR 177.1520 | Polypropylene homopolymer specification and extractables limitations |
| RoHS | Directive 2011/65/EU | Electrical/electronic articles; no homopolymer-introduced Pb, Hg, Cd, Cr(VI), PBB, PBDE |
| REACH SVHC screening | Regulation (EC) No 1907/2006 | Article 33 communication if candidate list substance is above 0.1 % w/w |
At shear rates typical of hot-runner gates, 10⁴–10⁵ s⁻¹, polypropylene homopolymer of this MFR class is pseudoplastic with a power-law index of approximately 0.30–0.40. A 10 % increase in apparent shear rate lowers apparent viscosity more than it raises pressure drop. Melt density at 230 °C is approximately 0.75 g/cm³, and specific heat capacity is approximately 2.2 kJ/(kg·K). These values are used in mould-filling simulation. Injection-moulded plaques from medium-flow homopolymers typically show fractional crystallinity of 40–55 % when calculated from melting enthalpy by ISO 11357-3:2018. Higher crystallinity correlates with higher flexural modulus and lower impact. The semicrystalline structure also explains the abrupt drop in notched Charpy impact between 0 °C and -20 °C displayed in the property table.
Compared with impact copolymers, PP 1080 has lower notched Charpy impact energy at subambient temperatures, higher heat deflection temperature, and lower density. Compared with high-flow controlled-rheology grades, PP 1080 retains a tensile yield stress of 32–35 MPa while providing adequate processability for medium-cavitation tooling. Controlled-rheology grades with MFR 25–40 g/10 min may permit thinner wall sections or lower clamp force, but they typically show reduced tensile yield stress and lower melt elasticity. PP 1080 also differs from random copolymer polypropylene, which has lower crystallinity, lower modulus, and lower heat deflection temperature but better optical clarity and cold-temperature impact.
When PP 1080 is used as a base resin for talc-filled or glass-reinforced compounds, twin-screw extruders with L/D ratios of 32:1 to 44:1 are specified. A typical barrel profile for a 20 wt% talc-filled formulation is 180 °C, 190 °C, 200 °C, 210 °C, 210 °C, and 205 °C from feed to die, with a screw speed of 300–500 rpm. Specific mechanical energy input for talc dispersion is typically 0.20–0.35 kWh/kg. Melt temperature measured at the die should not exceed 240 °C to prevent thermal deformation of the matrix and loss of stabiliser efficacy. If a side feeder is used for talc or glass, the side-feeder opening should be downstream of the polymer melting zone to reduce screw wear. On single-screw extruders used for colour concentrates, a metering section with a compression ratio of 2.5:1 to 3.5:1 and a breaker plate with 20–40 mesh screens are typical. Back pressure behind the screen pack frequently reaches 3–8 MPa, which is adequate for dispersion of 2–4 wt% colour masterbatch.
Incoming inspection of PP 1080 should include melt flow rate using ISO 1133-1:2022, ash content by ISO 3451-1:2019, and visual pellet contamination against a retained reference. A shift in ash content above 0.05 % can indicate additive carryover or external contamination, and it can affect colour and long-term ageing. For colour-critical applications, the measurement of yellowness index by ASTM E313-20 or ISO 11664-4:2008 on a compression-moulded plaque is common; values above 2.0 may indicate thermal history or insufficient stabiliser. These measurements are performed on samples dried for 1 h at 80 °C prior to moulding to prevent moisture artefacts.
In humid storage or outdoor silo conditions where relative humidity exceeds 60 %, pellet surface moisture can contribute to splay and inconsistent feeding. A desiccant hopper dryer set to 80 ± 5 °C for 2–3 h with a dew point of -20 °C or lower is sufficient; PP 1080 is not hygroscopic, but surface condensation is the concern. Injection moulders should not blend wet regrind into PP 1080 above 20 wt% without validated drying because regrind particle-size distribution alters melt homogeneity and can shift ejection force in high-cavity tools. Multiple heat histories consume stabiliser package; for non-food applications, 10–20 wt% regrind is common. For food-contact use, reprocessed material must comply with EU 10/2011 Article 17 and FDA 21 CFR 174.5 as applicable.
PP 1080 should not be specified for continuous load at temperatures above 90 °C in unfilled form; heat deflection temperature under 0.45 MPa is 85–95 °C and creep resistance declines above the amorphous-phase glass transition, approximately -10 °C. Chemical compatibility is broad in dilute acids and alkalis at ambient temperature, but strong oxidising acids, chlorinated solvents, and aromatic hydrocarbons can attack or swell the matrix at elevated temperatures. Outdoor exposure requires UV stabiliser or 2–3 wt% carbon black masterbatch to prevent embrittlement. Avoid storage near hot surfaces above 50 °C for prolonged periods because oxidative degradation can shift the melt flow rate upward and produce discolouration. These boundaries should be written into the incoming material specification because homopolymers of this class fail brittle under sustained stress in contact with aggressive fluids.