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MARLEX PP HOE222NP

    • Product Name: MARLEX PP HOE222NP
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 735988
    Density 0.905 g/cm³
    Melt Flow Rate 2.2 g/10 min (230°C, 2.16 kg)
    Tensile Strength At Yield 36 MPa
    Elongation At Break >100%
    Flexural Modulus 1450 MPa
    Notched Izod Impact Strength 3.0 kJ/m² (23°C)
    Heat Deflection Temperature 0 45 Mpa 110°C
    Vicat Softening Temperature 155°C
    Melting Point 165°C
    Rockwell Hardness R95

    As an accredited MARLEX PP HOE222NP factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing MARLEX PP HOE222NP polypropylene resin is packaged in 25 kg sealed multi-wall bags with moisture-proof lining for safe handling.
    Container Loading (20′ FCL) MARLEX PP HOE222NP is loaded in a 20′ FCL, palletized in bags, secured properly for safe transportation.
    Shipping MARLEX PP HOE222NP is a polypropylene resin supplied as free-flowing pellets. It should be shipped in clean, dry containers, bulk trucks, or lined bags to prevent moisture and contamination. Material is not typically regulated as hazardous; however, avoid extreme heat, open flames, and prolonged sunlight exposure during transport.
    Storage Store MARLEX PP HOE222NP in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep containers tightly sealed to prevent moisture absorption and contamination. Maintain moderate temperatures, avoid excessive stacking, and protect from mechanical damage. Ensure good housekeeping to minimize dust accumulation and fire risk.
    Shelf Life MARLEX PP HOE222NP has no defined shelf life if stored properly; keep dry, cool, and away from UV to maintain properties.
    Application of MARLEX PP HOE222NP

    On three-layer coextruded biaxially oriented polypropylene film lines running the nucleated homopolymer as the 80:10:10 to 90:5:5 core-to-skin mass split, Marlex PP HOE222NP is fed to the core extruder at a nominal melt-flow rate of 2.2 g/10 min under ISO 1133-1:2022 at 230 °C/2.16 kg. Melt temperatures are held between 240 °C and 260 °C on single-screw extruders with barrel L/D ratios of 30:1 to 38:1. The cast sheet is quenched on a chill roll at 20–40 °C, stretched in the machine-direction orienter at 130–150 °C to a draw ratio of 4.5:1–5.5:1, then oriented transversely in the tenter at 160–170 °C to 7:1–10:1 and annealed at 150–160 °C. In this application the skin layers typically contain 0.10–0.30 wt% silica antiblock masterbatch and 0.05–0.20 wt% erucamide slip masterbatch, while the core layer is maintained as neat resin with closed-loop edge trim regrind not exceeding 10 wt% of total core feed. Finished film is tested for tensile properties under ASTM D882-18, haze under ASTM D1003-21, coefficient of friction under ASTM D1894-14, and water vapour transmission under ASTM F1249-20 at 38 °C/90% RH. Food-contact compliance for the converted film is evaluated under FDA 21 CFR 177.1520(c) and EU Regulation (EU) No 10/2011, with overall migration controlled below 10 mg/dm² in the prescribed food simulants. Production experience on tenter lines indicates that the fast-crystallizing nucleated grade requires the first MDO preheat roll to remain below 145 °C to avoid roll-sticking defects; operators reduce preheat by 3–5 °C when blocking is detected on the second preheat roll. The grade is not predried under normal closed-package storage, but bags stored at relative humidity above 60% should be dried at 80 °C for 2 h to eliminate surface condensation before extrusion. Terminal products in this segment include 12–30 µm metallized snack wrappers, pressure-sensitive adhesive tape base films, print-lamination pouches, and label facestock for beverage and personal-care packaging.

    Regulatory testing for the food-contact film and sheet segments follows the matrix below.

    Regulatory instrumentScopeTest method or limitApplication coverage
    FDA 21 CFR 177.1520Olefin polymers intended for food-contact articlesEnd-test extraction and food-type classificationBOPP film, cast PP film, thermoformed sheet
    EU Regulation (EU) No 10/2011Plastic materials and articles intended to come into contact with foodOverall migration 10 mg/dm²; specific migration limits in Annex I Table 1All food-contact film and sheet scenarios
    EU Packaging Directive 94/62/ECPackaging and packaging waste placed on the EU marketSum of Pb, Cd, Hg, Cr(VI) 100 mg/kgAll converted articles produced from this resin
    REACH Regulation (EC) No 1907/2006Chemical substances in articlesAnnex XVII restrictions; Candidate List SVHC communication at article levelAll downstream segments

    What Process Adjustments Control Haze and Seal Initiation in Cast Polypropylene Retort Layers?

    Cast-film lines running the nucleated homopolymer use a single-screw extruder with 25:1–30:1 L/D and vacuum degassing, feeding a flat die at 220–250 °C with the air gap held between 15 mm and 25 mm to limit neck-in. Chill-roll temperature is set at 18–32 °C on the gloss surface and 35–50 °C on the matte surface where duplex cooling is needed; draw-down ratio is restrained to 1.2:1–2.0:1 because excessive air-gap draw increases machine-direction orientation and reduces seal strength. Heat-seal layers are typically coextruded with a random copolymer PP skin, adding 0.05–0.20 wt% erucamide slip and 0.10–0.25 wt% synthetic silica antiblock to the skin layer, while the core layer retains the homopolymer at 60–80 wt% of the total film mass. Seal initiation temperature is measured on a laboratory heat-seal tester under ASTM F2029-16, and hot-tack is recorded under ASTM F1921-12; the target heat-seal strength for retortable CPP is normally above 12 N/25 mm at 160 °C dwell. Cast-film compliance is anchored to FDA 21 CFR 177.1520 for direct food contact and EU Regulation (EU) No 10/2011; migration testing follows EN 1186-1:2002 with overall migration below 10 mg/dm². Production-scale observations show that silica antiblock levels above 0.25 wt% in a 15 µm cast layer can raise haze above 6% and scuff chill-roll surfaces, while levels below 0.10 wt% may produce blocking on wound rolls after 3–6 months at warehouse temperatures above 30 °C. The material should be dried at 80 °C for 2–4 h only if exposed to condensation; prolonged drying above 90 °C can oxidise the pellet surface and raise yellowness index. Finished products include retortable lidding films, frozen-food pouches, textile overwrap, and sterile medical device pouches after radiation or ethylene oxide compatibility validation.

    When Plug-Assist Thermoforming Develops Corner Splitting Below 150°C

    Because the nucleated PP crystallises more rapidly than conventional PP homopolymer on cooling, extruded sheet enters the forming station with a narrower thermoforming window. Sheet extrusion is run through a 30:1–36:1 L/D single-screw or twin-screw line with a gear pump and flexible-lip die at 220–250 °C, followed by a three-roll stack with roll temperatures of 70–90 °C for the middle roll and 60–80 °C for the top and bottom rolls. The sheet is either directly fed to a plug-assist thermoformer or reheated to a surface temperature of 155–170 °C; oven zoning is adjusted so that the sheet core reaches 158–168 °C without the surface exceeding 172 °C, above which sag and local thinning appear. The forming mold is held at 40–60 °C, and plug material is selected for low thermal conductivity to avoid chilling the sheet below 150 °C during pre-stretch. If forming occurs below 150 °C, stress whitening at plug-assisted corners and cracking along the flange radius are observed on production tools, particularly at draw ratios deeper than 1.5:1. Formulation adjustments for this segment include edge trim regrind at 15–30 wt% blended with virgin material, antistatic masterbatch at 0.10–0.20 wt% to reduce dust attraction on nested containers, and an optional clarifying masterbatch at 0.05–0.15 wt% where low-haze deli lids are required. Food-contact sheet is tested under FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011; sensory and migration testing under EN 1186-1:2002 and EN 13130-1:2004 is required for fatty food simulants because PP homopolymer has higher permeability to non-polar migrants than barrier resins. Terminal products include dairy cups, produce trays, bakery clamshells, deli containers, and clear lids for refrigerated retail packs. Operational limits include restricting regrind incorporation to 30 wt% unless melt-flow and tensile impact retention under ISO 179-1:2020 are verified on a batch basis; higher regrind ratios reduce sag resistance and lower the upper forming temperature below 165 °C.

    In high-volume pallet unitizing, flat polypropylene strapping produced from the nucleated homopolymer is extruded through a 24:1–30:1 L/D single-screw extruder at 220–250 °C, quenched in a water bath with a cascade temperature control maintained between 30 °C and 45 °C, then passed through hot-air or water-heated orientation ovens at 120–140 °C and stretched 8:1–12:1. The strapping line adds a UV stabilizer masterbatch at 0.20–0.50 wt%, titanium dioxide white masterbatch at 1.0–3.0 wt% where high opacity is specified, and calcium carbonate masterbatch at 3–8 wt% only for low-tenacity economic strap where reduced elongation is acceptable. Embossing rolls are kept at 80–100 °C to imprint cross-hatch patterns without generating microcracks, and winder tension is set below 10% of the strap break strength to prevent cold creep and coil set. Break strength and elongation are measured under ASTM D638-14 or ISO 527-2:2012, and weathering retention is evaluated under ASTM G154-23 using UVA-340 lamps at 0.35 W/m² for outdoor construction logistics. Compliance for industrial strapping is anchored to the EU Packaging Directive 94/62/EC heavy metal limit of 100 mg/kg for the sum of Pb, Cd, Hg, and Cr(VI), and to REACH Regulation (EC) No 1907/2006 Annex XVII restrictions; food-contact status is not claimed for this segment. Production experience shows that water bath temperature fluctuations greater than ±5 °C produce asymmetric quench stresses that appear as strap curl during winder start-up, and that orientation oven temperatures above 145 °C lower elongation at break below 8% and increase snap-back breakage during palletising. Terminal products are 9–19 mm polypropylene strapping for bundle closure, pallet unitizing, and export packaging logistics.

    Monoaxial Tape Yarn Orientation and the Narrow Preheat Window in Water-Quenched PP

    Water-quenched tape-yarn lines manufacturing woven sack, FIBC, and agro-textile fabrics start by extruding the nucleated PP into a flat film die at 220–250 °C, quenching in a water bath at 25–35 °C, slitting into tapes of 2.5–5.0 mm, and orienting in hot-air ovens with first-zone temperatures of 130–145 °C and subsequent zones at 140–150 °C to a total stretch ratio of 6:1–10:1. The nucleated grade provides higher tenacity after orientation but narrows the first-zone preheat tolerance to approximately ±5 °C; first-zone temperatures above 155 °C cause edge fibrillation and frequent tape breaks at the draw stand, while temperatures below 125 °C increase splitting during high-speed weaving. Additive loadings for this sector include calcium carbonate masterbatch at 2–6 wt% for opaque woven sacks, hindered amine light stabilizer masterbatch at 0.30–0.60 wt% for agricultural shade nets, and a processing lubricant masterbatch at 0.05–0.10 wt% where line speeds exceed 180 m/min. Fabrics woven from these tapes are tested for tensile properties under ISO 13934-1:2013, tear resistance under ISO 13937-3:2000, and UV ageing under ASTM G154-23; for flexible intermediate bulk containers, design and testing follow ISO 21898:2004 and applicable UN transport regulation requirements. The compliance baseline for EU sales is REACH Regulation (EC) No 1907/2006 and the EU Packaging Directive 94/62/EC heavy metal threshold of 100 mg/kg. Production-scale data show that resin drying at 80 °C for 2 h is necessary when bags have been stored in humid environments, because surface moisture can generate splay marks in the quenched film and interfere with downstream fibrillation resistance. End products include woven polypropylene sacks for agriculture and building materials, FIBC bulk bags, crop shade netting, and carpet backing woven tapes. Published data for the specific interaction of HOE222NP with metal-pigmented UV masterbatches in long-term desert exposure is limited; outdoor warranties require batch-specific tensile retention testing rather than reliance on nominal additive ratios.

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    Certification & Compliance
    More Introduction

    MARLEX PP HOE222NP is a nucleated polypropylene homopolymer supplied in pellet form for injection molding. The grade is positioned for thin-wall rigid packaging, closures, and technical articles where elevated crystallization velocity is required relative to conventional non-nucleated homopolymer resins. Melt flow rate determined under ISO 1133-1:2022 at 230 °C and 2.16 kg is reported as 2.2 g/10 min; density determined under ISO 1183-1:2019 is reported as 0.905 g/cm³. These values place the product in a medium-flow injection molding band, balancing cavity-fill pressure against melt strength during pack and hold.

    The designation suffix NP indicates a nucleated formulation. Nucleation raises the crystallization temperature and produces a finer spherulitic structure at a given cooling rate. In thin-wall cup and container molds this structural change permits earlier demolding because the solidification plateau is reached nearer to the mold-contact temperature. Typical application sites include dairy cups, dry-food containers, appliance housings, media covers, and non-transparent closures where cycle-time reduction and stiffness-controlled wall-thickness design are primary cost drivers. Operational boundaries include reduced notched impact toughness relative to impact copolymer grades and a practical melt temperature ceiling near 250 °C; sustained operation above that threshold accelerates molecular weight reduction and surface splay.

    Does Nucleation Alter the Shrinkage Anisotropy Window?

    Nucleation alters the shrinkage anisotropy window by shifting the onset of crystallization to a higher temperature during cooling. Differential scanning calorimetry of nucleated grades commonly shows a crystallization peak between 118 °C and 125 °C at a cooling rate of 10 °C/min, compared with 105 °C to 112 °C for an equivalent non-nucleated homopolymer. As a result, the differential shrinkage between flow direction and transverse direction can exceed 0.2 percentage points in flat rectangular parts. Gate location should therefore be placed near the thickest section, and holding pressure should be maintained until gate freeze. Published data for part-specific shrinkage covariance is limited; mold trials should validate the anisotropic ratio for parts with length-to-thickness ratios above 100:1.

    Barrel Thermal Profiling, Screw Recovery, and Back-Pressure Limits

    Processing on 25–40 mm reciprocating screw machines with 20:1 to 24:1 L/D ratio uses a rising barrel profile from feed to nozzle. Feed zone settings of 180–200 °C, compression zone settings of 210–230 °C, metering zone settings of 220–240 °C, and nozzle settings of 220–240 °C are typical. Mold temperature is generally held at 20–50 °C. Back pressure of 0.5–1.0 MPa stabilizes shot weight without excessive recuperation time. Screw rotation should be limited to keep melt residence time below 5 min; longer hold times at high temperature cause yellowing and loss of molecular weight.

    On multi-cavity hot-runner systems with 8–16 drops, the primary production-scale failure mode observed is gate blush at melt temperatures above 245 °C and stringing when nozzle tips run hotter than 240 °C. Shot-to-shot variation of melt cushion should be kept within 1.5 mm to avoid inconsistent packing in cavities near the sprue versus end-of-manifold positions. Valve-gated systems require a delay of 0.2–0.5 s after screw retract before decompression to prevent drool. At relative humidity above 60 %, pellet pre-drying at 80 °C for 2 h is recommended to reduce splay and surface defects.

    Melt Cushion Control Remains the Dominant Source of Cavity-to-Cavity Variation

    Cavity-to-cavity mass flow variance in thin-wall molds is more strongly influenced by melt cushion stability than by melt temperature variation within the recommended window. A cushion setpoint of 2–4 mm is typical because smaller cushions amplify shot-size error and larger cushions extend recovery time. Screw decompression should follow the shot with a distance not exceeding 2 mm to prevent air entrapment at the next melt accumulation stage. In production runs of 0.5 mm wall cups, cushion drift above 1 mm has been associated with short shots in end-of-manifold cavities and flash near the sprue, confirming that pack pressure decays unevenly across the manifold when the cushion is not held constant.

    When Thin-Wall Rigidity Requirements Exclude Impact Copolymer Grades

    For parts where top-load strength is governed by wall modulus rather than toughness, selection of MARLEX PP HOE222NP over a medium-impact polypropylene copolymer is supported by its higher flexural modulus and higher heat deflection temperature. The trade-off is a lower notched Izod impact value and reduced ductility at sub-zero temperatures. If the application requires hinge flexural endurance or impact resistance below 0 °C, an impact copolymer should be evaluated. In contrast, if the design requirement is minimum wall thickness under a compressive load, the nucleated homopolymer permits either wall-thickness reduction or higher top-load retention after hot filling.

    Reported Mechanical Property Profile and Test Method Alignment

    The following values are typical published data and should be verified against the current supplier certificate of analysis for the specific production lot.

    Property Test Method Typical Published Value
    Melt Flow Rate, 230 °C, 2.16 kg ISO 1133-1:2022 2.2 g/10 min
    Density ISO 1183-1:2019 0.905 g/cm³
    Tensile Stress at Yield ISO 527-2:2012 36 MPa
    Tensile Strain at Yield ISO 527-2:2012 9 %
    Flexural Modulus ISO 178:2019 1600 MPa
    Notched Izod Impact, 23 °C ISO 180/A:2019 3.0 kJ/m²
    Heat Deflection Temperature, 0.45 MPa ISO 75-2:2013 96 °C

    What Regulatory Boundaries Apply to Food-Contact and Electrical-Enclosure Use?

    Compliance assessment for this polypropylene grade derives from the base polymer class and the additive package. A compliance checklist matrix is shown below.

    Framework Designation Assessment Basis
    FDA food contact 21 CFR 177.1520 Olefin polymer; compliance depends on additive package and intended conditions of use
    EU food contact Regulation (EU) 10/2011 Migration testing required for specific food simulants
    RoHS Directive 2011/65/EU Typical PP homopolymer meets Pb, Cd, Hg, and Cr(VI) limits; verify with supplier certification
    REACH EC 1907/2006 Substance registration and SVHC declaration required from supplier

    Compared with a non-nucleated homopolymer of equivalent melt flow rate, the nucleated grade exhibits higher flexural modulus and a narrower mold temperature window for consistent shrinkage control. The faster crystallization reduces warpage in some geometries but can increase sink-mark visibility at rib intersections if packing is curtailed too early. Compared with a random copolymer, the grade yields lower clarity and lower impact resistance but higher heat resistance; this trade-off makes it unsuitable for transparent refrigerator containers where contact clarity is the primary selection criterion. The product is not a clarified grade, and thin-section transparency is limited even with rapid mold cooling.

    When Low-Temperature Impact Resistance Is Non-Negotiable

    For parts exposed to impact at temperatures below 0 °C, the use of MARLEX PP HOE222NP is generally inappropriate unless wall thickness and geometry compensate for the inherent brittleness of the homopolymer matrix. The notched Izod value declines with decreasing temperature, and weld lines in cold-runner molds show lower elongation at break than unfused regions. In such applications, an impact copolymer or a polypropylene compound with elastomer modification should be specified. No amount of nucleating-agent control changes the fundamental low-temperature impact limitation of a homopolymer polypropylene backbone. Published data for this specific configuration under sub-zero instrumented impact is limited; end-use validation at the lowest service temperature is required.

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