| HS Code | 448276 |
| Melt Flow Rate 230 C 2 16 Kg | 8.0 g/10min |
| Density | 0.905 g/cm³ |
| Tensile Strength At Yield | 30.0 MPa |
| Elongation At Yield | 11.0% |
| Flexural Modulus | 1300 MPa |
| Izod Impact Strength Notched 23 C | 3.0 kJ/m² |
| Heat Deflection Temperature 0 45 Mpa | 100 °C |
| Vicat Softening Point A50 | 155 °C |
| Rockwell Hardness | R100 |
| Appearance | Pellets |
As an accredited Sinochem Fuya PP L5E89 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Sinochem Fuya PP L5E89 is supplied in 25 kg woven polypropylene bags with moisture-proof inner lining. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Sinochem Fuya PP L5E89, ensuring safe, efficient transport. |
| Shipping | Sinochem Fuya PP L5E89 is a polypropylene resin shipped as virgin pellets. It is typically packed in 25 kg woven bags or supplied in bulk containers. The material is non-hazardous but should be kept dry and uncontaminated. Use clean, covered containers during sea, truck, or rail transport to protect quality. |
| Storage | Store Sinochem Fuya PP L5E89 in a dry, clean, well-ventilated warehouse. Keep bags away from direct sunlight, moisture, heat sources, and open flames. Avoid contact with strong oxidants. Maintain moderate temperature and humidity, and handle carefully to prevent bag damage and contamination. |
| Shelf Life | Shelf life is 12 months from production date when stored in original, unopened packaging under cool, dry conditions. |
Sinochem Fuya PP L5E89 is a high-flow polypropylene homopolymer specified for injection moulding. The material is characterised by a nominal melt flow rate of 25 g/10 min under ISO 1133-1 at 230 °C and 2.16 kg, with a typical tensile yield stress of 31–35 MPa under ISO 527-2 and a flexural modulus of 1,400–1,550 MPa under ISO 178. The notched Izod impact strength at 23 °C is approximately 2.0–2.5 kJ/m² under ISO 180/A, which places the material in the low-to-moderate impact range typical of high-flow polypropylene homopolymers. These characteristics restrict L5E89 to short-cycle injection moulded products that prioritise flow length, surface definition, and dimensional stability over low-temperature toughness. The downstream scenarios below are limited to established conversion routes: thin-wall food packaging, beverage closures, household storage, industrial pails, disposable food service, and returnable logistics crates. In each scenario, the grade is used as the matrix resin rather than as an impact-modified compound, unless a modifier is expressly stated.
Compliance reference for this segment is EU 10/2011 overall migration limit of 10 mg/dm² with food simulant types A, B, and D1, FDA 21 CFR 177.1520 for olefin polymers, and China GB 4806.7-2023; converters must verify specific migration of additives, particularly when antistatic or clarifying agents are compounded into the matrix. In formulation, L5E89 is used at 100 parts by mass, with a primary phenolic antioxidant plus a phosphite secondary antioxidant at a combined loading of 0.04–0.10 wt%, an acid neutralizer at 0.02–0.05 wt%, and a sorbitol-based clarifying agent at 0.15–0.25 wt%. Antistatic agent is added at 0.05–0.10 wt% only when nested containers cause handling faults on automatic filling lines. Higher clarifier loading above 0.30 wt% produces plate-out on the core side of the tool and increases the probability of orifice freeze-off in hot-runner valve gates. Downstream production is performed on single-face or stack-mould injection machines with clamp forces from 1,500 kN to 5,000 kN, plasticating units with L/D ratios of 20:1 to 24:1, and accumulator-assisted injection speeds reaching 180 mm/s; measured melt temperature at the nozzle is held at 230–250 °C and mould temperature is controlled at 25–45 °C with turbulent-flow cooling at 10–15 °C inlet water. For wall sections between 0.4 mm and 0.7 mm, flow length-to-thickness ratios of 150:1 to 220:1 are achievable, and fill time is typically below 0.3 s; packing pressure is set from 45 MPa to 70 MPa hydraulic, with hold time of 1.0–1.8 s per 0.5 mm wall thickness to prevent sink at gate bosses. Terminal products include dairy tubs, deli containers, takeaway bases, microwave-safe trays, and disposable food service trays. The operational boundary is thermal: continuous food contact above 100 °C or microwave reheating with surface fat temperatures above 120 °C can compromise part stiffness and dimensional stability; L5E89 is not an oxygen barrier and should not be specified for shelf-stable barrier packaging without a separate EVOH or aluminium layer.
Closure converters require high melt-flow grades to fill thin annulus features, but excessive flow promotes flash in the bridge area of tamper-evident bands. L5E89 at its nominal 25 g/10 min MFR is therefore processed at the lower end of the melt-temperature window, 210–240 °C, to maintain gate sealing and reduce screw drool. The relevant compliance framework includes FDA 21 CFR 177.1520, EU 10/2011, GB 4806.7-2023, and converter-specific organoleptic taint tests for mineral water and carbonated soft drinks; extractables are evaluated under EU 10/2011 Annex V and United States 21 CFR 177.1520 migration assumptions for packaged beverage. Formulation for closures begins with L5E89 at 100 parts by mass, with a primary antioxidant at 0.05–0.10 wt%, a nucleating agent at 0.03–0.08 wt%, and a slip agent such as erucamide at 0.05–0.12 wt%. Titanium dioxide white masterbatch is added at 2–3 wt% for opaque closures; if colour concentrates are used, the carrier resin must be a high-flow PP with MFR within ±5 g/10 min of the base resin to avoid visible streaks. Slip-agent dosage is a process-critical threshold: below 0.05 wt% removal torque on tamper-evident caps can exceed the filling-line limit, while above 0.15 wt% the additive blooms to the cold tool surface and produces irregular coefficient-of-friction on the closure outer diameter, increasing print adhesion failure. Production is typically run on 48- to 96-cavity hot-runner systems with hydraulically actuated valve gates, cold-half tool temperatures held at 8–15 °C, and hot-runner manifold temperatures maintained within ±2 °C of the nozzle body. Cycle times of 5–9 s are reported on 96-cavity closure tools with shot weights of 70–150 g; inject pressure at transfer is commonly 60–90 MPa hydraulic, and hold pressure is set to 35–50 MPa until gate freeze. Terminal product types include 26/21 mm short-skirt closures for bottled water, 28 mm CSD closures, push-pull sports caps, and tamper-evident dairy closures. The limitation is low-temperature brittleness: closure impact at -10 °C may produce band fracture, so carbonated soft drink applications in cold-chain distribution require testing of slit-bridge thickness, which should not exceed 0.35 mm without a compounded impact modifier.
Injection-moulded storage boxes, drawer organisers, and household baskets made from L5E89 fall under general consumer product safety rather than food-contact regulation; however, kitchen storage items intended for repeated contact with dry or aqueous foods are evaluated under EU 10/2011 and FDA 21 CFR 177.1520, and toy-like boxes marketed to children may require EN 71-3 migration limits and REACH Annex XVII restrictions. The standard formulation for opaque housewares uses L5E89 at 100 parts by mass, a colour masterbatch at 2–4 wt%, an antioxidant package at 0.05–0.10 wt%, and, when nested containers must separate on automatic filling lines, an external or internal slip additive at 0.5–1.0 wt%. Addition of 5–10 wt% calcium carbonate masterbatch is acceptable for rigid storage articles but reduces notched Izod impact and should not be specified for stacking loads above 20 kg. Downstream processing uses two-plate or three-plate cold-runner injection machines with clamp force from 1,000 kN to 5,000 kN, melt temperature 200–230 °C, mould temperature 20–40 °C, injection pressure 60–90 MPa, and wall thickness 1.2–2.5 mm. Cycle time is governed by cooling of the thickest rib or snap-fit undercut; typical cycle windows are 15–30 s for 2 mm walls. Terminal products include stackable storage totes, drawer trays, closet organisers, wastepaper baskets, and open-top containers. The homopolymer limitation is relevant in garage or outdoor use: unmodified L5E89 should not be selected for articles exposed to repeated impact at sub-zero temperatures or continuous UV without a HALS package at 0.1–0.3 wt%.
Industrial pails and paint buckets constitute a processing-intense application because the part combines thick rim geometry, stacking load, and drop-impact requirements with a high-flow homopolymer. For packaging of paints, coatings, and non-hazardous chemicals, compliance is governed by the UN Model Regulations for packaging group II or III when used as dangerous goods packaging, specifically the design-type tests for drop, stack, and hydrostatic pressure referenced in UN 6.1.5 and ADR 6.1.5; REACH Article 33 communication applies at SVHC concentration above 0.1 wt%. In formulation, L5E89 is used at 100 parts by mass with an antioxidant package at 0.05–0.15 wt%, a HALS UV stabilizer at 0.10–0.30 wt% for outdoor storage, and colour masterbatch at 2–4 wt%. For 25 L pails subjected to drop tests at -18 °C, 10–20 wt% impact modifier is generally compounded because the unmodified homopolymer notched Izod impact of about 2.0 kJ/m² at 23 °C may not provide sufficient ductile failure margin at low temperature. Downstream production uses accumulator-assisted injection moulding machines with clamp forces of 6,000–15,000 kN, screw diameters of 80 mm or larger, L/D ratios of 20:1–24:1, melt temperature 220–260 °C, mould temperature 20–50 °C, injection pressure 80–120 MPa, and holding pressure 50–70 MPa. Wall thickness ranges from 1.8 mm to 3.2 mm; rim cooling and handle hinge areas determine cycle time, commonly 35–60 s. Terminal products include 5 L, 10 L, 20 L, and 25 L paint pails, coating buckets, chemical pails with removable lids, and non-UN industrial containers. Published data for specific L5E89 pail certifications is limited; converters must perform UN drop and stack tests on actual moulded pails because safety margins are strongly geometry-dependent and cannot be transferred from a generic resin datasheet.
Disposable cutlery and food-service articles produced from L5E89 are limited to cold and warm food contact, not to oven or prolonged boiling-water service. EU food contact compliance requires EU 10/2011 overall migration of 10 mg/dm²; US compliance follows FDA 21 CFR 177.1520; China’s GB 4806.7-2023 applies to domestic food-contact materials. Formulation for forks, spoons, and knives uses L5E89 at 100 parts by mass with a clarifying/nucleating package at 0.10–0.20 wt%, an antioxidant package at 0.05–0.10 wt%, and white masterbatch at 2–3 wt%. The high melt flow supports multi-cavity family tools on moulding machines of 1,000–2,500 kN, melt temperature 220–240 °C, mould temperature 25–35 °C, and wall thickness 1.5–2.0 mm. Filling time is held below 0.5 s; packing pressure at 30–50 MPa for 2–4 s prevents sink marks at fork tine roots and knife handle bosses. Cycle time is 8–15 s depending on cavity count. Terminal products include disposable forks, spoons, knives, coffee stirrers, and tasting spoons. The service temperature boundary is set by modulus retention: Vicat softening of L5E89 is reported above 150 °C under ISO 306, but continuous load-bearing food-service articles are limited to 90–100 °C because heat deflection under load controls stiffness. The grade is not designed for ovenable cutlery or repeated boiling-water immersion.
Returnable distribution crates moulded in L5E89 require careful gate placement and rib design because the grade’s high melt-flow can produce jetting and hesitation marks in sections thicker than 4 mm. Compliance references for industrial crates are performance-driven: stacking resistance is evaluated using ISO 2234:2000 for static stacking, drop tests using ISO 2248:1985 or ASTM D4169-23 distribution cycles, and chemical compatibility is screened by immersion testing under ISO 175 where crates are washed with alkaline or oxidative cleaners. Formulation starts with L5E89 at 100 parts by mass, with an antioxidant package at 0.05–0.15 wt%, a HALS stabiliser at 0.10–0.30 wt% for returnable crates stored outdoors, and colour masterbatch at 3–5 wt%. For heavy-duty crates, an impact modifier at 10–15 wt% is added to improve cold-temperature drop performance; this addition lowers flexural modulus and must be accounted for in stacking load calculations. Processing on conventional injection machines with clamp forces of 5,000–12,000 kN uses melt temperatures of 210–250 °C, mould temperatures of 30–50 °C, injection pressure 80–110 MPa, and holding pressure 50–70 MPa; wall thickness ranges from 3 mm to 5 mm and cycle time is 30–60 s. Terminal products include stackable logistics crates, distribution totes, recycling bins, and agricultural harvest baskets. The specific process risk is sink marking at rib intersections and handle bosses: packing time below 8 s for a 4 mm wall yields visible sink and reduces stacking accuracy. Processors should use gate placement into thick sections and hold-pressure-decay profiles rather than raising melt temperature, which increases warpage in shallow rectangular crates.
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Sinochem Fuya PP L5E89 is identified in producer documentation as a polypropylene homopolymer pellet grade supplied for extrusion and selected injection molding processes. The product is characterized by a nominal melt flow rate of 3.0–3.8 g/10 min when tested under ISO 1133-1:2022 at 230 °C and 2.16 kg. This melt flow rate places the resin between fractional-melt film grades and high-flow controlled-rheology injection grades. The homopolymer backbone contains negligible deliberate ethylene comonomer, so oriented or molded articles exhibit higher flexural modulus and heat deflection than propylene-ethylene random copolymers, but lower notched impact resistance at 0 °C and below and higher optical haze in transparent film. The grade is used in biaxially oriented film, flat-yarn tape, woven bag fabric, strapping, and moderate-flow injection molding. Its principal difference from post-reactor vis-broken homopolymers is a broader molecular weight distribution, which supports melt strength during machine-direction orientation but reduces spiral flow in thin-wall molds. These distinctions define the application boundary: L5E89 is specified where biaxial draw stability and stiffness govern over low-temperature impact or optical clarity.
Producer certificates of analysis for Sinochem Fuya PP L5E89 normally report the following physical and thermal properties. Values are representative for the natural, unfilled homopolymer and may shift with masterbatch addition or regrind. The current lot certificate should be obtained before setting process limits.
| Property | Unit | Value or range | Test method |
|---|---|---|---|
| Melt flow rate, 230 °C/2.16 kg | g/10 min | 3.0–3.8 | ISO 1133-1:2022 |
| Density | g/cm³ | 0.900–0.910 | ISO 1183-1:2019 |
| Tensile yield stress | MPa | 32–36 | ISO 527-2:2012 |
| Tensile elongation at yield | % | 8–11 | ISO 527-2:2012 |
| Flexural modulus | MPa | 1300–1600 | ISO 178:2019 |
| Notched Charpy impact, 23 °C | kJ/m² | 2.8–5.0 | ISO 179-1:2010 |
| Vicat softening point, A50 | °C | 152–156 | ISO 306:2022 |
| Heat deflection temperature, 0.45 MPa | °C | 90–105 | ISO 75-2:2013 |
| Ash content | wt% | 0.02–0.05 | ISO 3451-1:2019 |
The specification envelope is not a compliance limit; the producer may issue a narrower internal range for film-grade supply. For food-contact laminates, the converter must verify overall migration and specific migration limits under EU 10/2011 or FDA 21 CFR 177.1520 and confirm that the antioxidant and acid scavenger system is included in the formulation disclosure. The natural grade is not formulated with brominated flame retardants or heavy-metal based pigments; colored product requires separate compliance review.
Molecular architecture drives the performance differences. Random copolymers contain 2–4 wt% ethylene, which disrupts crystallinity, lowers flexural modulus by roughly 20–30%, and lowers heat deflection; they are specified for unoriented transparent packaging and low-temperature toughness. L5E89 as a homopolymer develops higher alpha-form crystallinity, giving flexural modulus in the 1300–1600 MPa range and Vicat softening above 150 °C.
High-flow homopolymers are typically post-reactor vis-broken with controlled peroxide dosing to narrow molecular weight distribution and raise melt flow rate. L5E89 is not controlled-rheology in that sense; a broader distribution gives stronger shear thinning and higher melt strength, but lower spiral flow and higher injection pressure in thin-wall tools. In BOPP film, the higher melt strength stabilizes the cast web during high line speeds; in flat-yarn tape, it reduces draw resonance. In injection molding, it is a limitation rather than an advantage.
| Attribute | Sinochem Fuya PP L5E89 | Propylene-ethylene random copolymer | Post-reactor vis-broken homopolymer | Method |
|---|---|---|---|---|
| Ethylene content | 0 wt% | 2–4 wt% | 0 wt% | FTIR / producer disclosure |
| Melt flow rate, 230 °C/2.16 kg | 3.0–3.8 g/10 min | 5–15 g/10 min | 10–25 g/10 min | ISO 1133-1:2022 |
| Flexural modulus | 1300–1600 MPa | 900–1200 MPa | 1400–1700 MPa | ISO 178:2019 |
| Heat deflection at 0.45 MPa | 90–105 °C | 65–85 °C | 95–110 °C | ISO 75-2:2013 |
| Melt strength in orientation | higher | moderate | lower | Rheotens |
| Optical haze in 50 µm cast film | higher | lower | intermediate | ASTM D1003 |
For low-temperature impact at -20 °C or below, L5E89 is not a direct substitute for propylene impact copolymers. The dispersed rubber phase in impact copolymers increases low-temperature notched impact by at least a factor of two while reducing stiffness. L5E89 should be selected only where heat deflection, tensile modulus, and orientation stability dominate.
Flat-yarn tape extrusion with L5E89 operates in a defined thermal window. Melt temperature at the slot die is controlled between 230 °C and 260 °C; temperatures above 270 °C accelerate antioxidant depletion and produce yellowing, while temperatures below 220 °C raise die pressure and reduce tape gloss. Water bath temperature is normally 30–40 °C; water below 25 °C freezes a thick skin layer that can fibrillate during oven drawing. Draw ratio is typically 6:1–8:1, with stretching oven temperature between 130 °C and 160 °C; the resulting tape tenacity is normally tested under ISO 13934-1. At draw ratios above 9:1, tape fibrillation becomes sensitive to minor gel particles and gauge variation. On typical 90 mm single-screw tape lines with 30:1 L/D barrier screws, melt-pressure variation at the die should not exceed ±0.5 MPa to avoid tape gauge drift.
Woven sack and bulk container production using L5E89 tapes generally requires tape tenacity above 0.30 N/tex and elongation at break between 15% and 25%. Direct published data for L5E89 in this application is limited; converters should set process parameters using their own line data because tape tenacity depends on draw ratio, quench temperature, and screw design.
BOPP film lines require stricter control than flat tape. Cast-roll temperature is normally kept at 25–35 °C; if the cast web temperature at the machine-direction orientation unit remains above 45 °C, premature crystallization reduces transverse draw uniformity and increases thickness variation. Machine-direction draw is commonly set at 4.5:1–5.2:1; transverse draw in the tenter oven is 6:1–10:1. The heat-set zone is held at 160–170 °C. Deviation above 175 °C can cause film sagging between tenter clips, while deviation below 150 °C may leave residual shrinkage above 4% in finished roll stock. These limits are not absolute for every line geometry; tenter rail curvature, clip temperature, and air velocity also influence the effective window.
Die-lip plateout is an operational boundary when edge trim is recycled. On 3.2 m-wide tenter lines operating above 200 m/min, die-lip deposit formation often becomes visible when recycled edge trim exceeds 20 wt% of the feed stream; streaking on film edges may appear within 48 h of continuous casting. Reduction of trim recycle, periodic purging with a low-MFR purge grade, and cleaning of the die lip with aluminum oxide tools are production-scale responses. The broad molecular weight distribution can increase die swell at the lip, making lip-gap adjustment more sensitive to melt-pressure fluctuation.
Injection molding of L5E89 into articles with wall thickness between 1.5 mm and 3 mm is possible where melt flow is not the primary constraint. A barrel profile from 220 °C to 250 °C and a mold temperature of 20–50 °C are typical starting conditions. Compared with a 12 g/10 min controlled-rheology homopolymer, the spiral flow length in a 2 mm spiral mold under constant injection pressure is approximately 15–25% shorter. Gate freeze time is longer than high-flow grades due to higher zero-shear viscosity, which can reduce sink marks but requires higher pack pressure. Thin-wall parts below 1 mm are generally outside the recommended flow envelope for L5E89 unless the tool is designed with multiple gates and hot-runner manifolds sized for higher viscosity.
Moisture management is a boundary condition. The material is not hygroscopic, but surface condensation during cold-to-warm transfer from unheated storage at RH > 60% can cause splay and silver streaks in molded or extruded parts. If condensation is observed, pre-dry at 80–85 °C for 2–4 h in a desiccant dryer with a dew point below -20 °C. Drying should not exceed 4 h at 85 °C; extended residence at elevated temperature can consume the phenolic antioxidant prematurely and shift melt flow.
Quality-control specifications for Sinochem Fuya PP L5E89 should include melt flow rate, ash, flexural modulus, and optionally gel count for film applications. The producer’s standard specification may not include a gel-count guarantee; biaxial film converters should establish a gel-count sampling plan on cast film or extruded tape before qualification. For colored products, the choice of pigment affects processing stability: uncoated copper phthalocyanine pigments can catalyze thermo-oxidative degradation of polypropylene at extrusion temperatures, and halogenated flame retardants require additional acid-neutralizing stabilizers. Avoid blending with PVC residues in shared silos or pellet transport lines; hydrogen chloride released from PVC can deplete the acid scavenger and darken the resin. These compatibilities and thermal boundaries define the practical operating envelope for downstream compounding and conversion.