| HS Code | 847185 |
| Product | MARLEX PP HD631CF |
| Manufacturer | Chevron Phillips Chemical Company |
| Polymer Type | Polypropylene (PP) homopolymer |
| Physical Form | Pellets |
| Density | 0.905 g/cm³ |
| Melt Flow Rate | 70 g/10 min at 230°C/2.16 kg |
| Tensile Strength At Yield | 35 MPa |
| Elongation At Yield | 10% |
| Flexural Modulus | 1.5 GPa |
| Notched Izod Impact | 21 J/m at 23°C |
| Heat Deflection Temperature | 104°C at 0.46 MPa |
| Vicat Softening Temperature | 149°C |
| Applications | Meltblown and spunbond nonwovens, thin-wall injection molding |
As an accredited MARLEX PP HD631CF factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | MARLEX PP HD631CF polypropylene resin is packaged in 25 kg moisture-resistant bags, ensuring safe handling and storage. |
| Container Loading (20′ FCL) | 20′ FCL loading of MARLEX PP HD631CF polypropylene resin, packed in 25kg bags, approximately 20 metric tons per container. |
| Shipping | MARLEX PP HD631CF polypropylene resin ships in sealed bags, Gaylord boxes, or bulk railcars depending on quantity. Protect from moisture, direct sunlight, and excessive heat. Keep containers dry and ventilated. Transport in covered, clean conveyance. No special hazard classification for general freight, but avoid dust accumulation and follow standard material handling precautions. |
| Storage | Store MARLEX PP HD631CF in a cool, dry, well-ventilated area, tightly sealed in its original container. Protect from direct sunlight, heat, moisture, and ignition sources. Avoid contact with strong oxidizing agents. Maintain stable room temperature and low humidity to prevent degradation or contamination. Proper storage preserves product quality and ensures safe handling. |
| Shelf Life | MARLEX PP HD631CF has an indefinite shelf life when stored in a cool, dry area away from sunlight in original sealed packaging. |
Marlex PP HD631CF enters thin-wall food packaging production in a 48-cavity stack mould with a hot-to-cold runner ratio of 1:4.1 and a 220-tonne all-electric injection moulding machine. The barrel is profiled from 200°C in the feed to 235°C at the nozzle; nozzle body temperature is held at 230°C with a band tolerance of ±3°C. Melt temperature measured at the nozzle by an infrared probe is 228°C to 236°C when screw back pressure is set to 7 MPa and screw speed to 180 rpm. The part wall is specified at 0.75 mm ±0.04 mm, and the fill rate is set at 150 mm/s. Hold pressure of 48 MPa is maintained until cavity pressure decays to 18 MPa; hold time is 1.6 seconds. Cycle time for a 175 mL dairy cup is 5.1 seconds excluding robot removal. Check-ring wear above 0.12 mm produces a cushion position step change of 1.8 mm and unstable hot-runner pressure, which increases shot-to-shot mass variation above 0.15 percent. The maximum regrind level for food-contact production is set at 25 percent unless a three-cycle migration validation is run; above this level melt viscosity drops and cavity filling imbalance becomes measurable on the two outside rows of the stack mould.
Food-contact compliance is assessed under FDA 21 CFR 177.1520(c) for olefin polymers and EU Regulation 10/2011 Annex I, with overall migration not exceeding 10 mg/dm² when tested according to EN 1186-1:2002 using 3 percent acetic acid and 10 percent ethanol simulants. The terminal product is not hot-filled above 75°C because the filled top-load limit of 50 N at 3.0 mm sidewall deflection is not specified for higher fill temperatures. The additive package contains a nucleating agent and an acid neutralizer at 400 ppm to 600 ppm. Haze at 0.75 mm wall stock is 16 to 22 percent under ASTM D1003-13; notched Charpy impact energy at 23°C is 2.8 to 3.5 kJ/m² under ISO 179-1/1eA. Increasing the clarifier/nucleant loading above 0.25 percent is not applied without a new capability study because haze falls by 3 to 5 percentage points while notched impact energy can drop below 2.5 kJ/m², below the 1.2 m drop requirement tested according to ASTM D5276-98. Where HD631CF-specific multi-point haze-impact curves are not published, limits are derived from equivalent clarified polypropylene grade families with the same nominal melt flow rate.
For a 38 mm two-start linerless closure used on high-density polyethylene beverage bottles, HD631CF is moulded in a 72-cavity hot-runner tool on a 180-tonne all-electric press with a 35 mm screw and a 22:1 L/D ratio. The barrel profile runs from 215°C in the rear zone to 240°C at the nozzle. The mould coolant is maintained at 15°C ±1°C with a turbulent-flow circuit of 2.4 m/s linear velocity. Injection time is 0.28 seconds; hold time is 1.1 seconds; cooling time is 3.2 seconds. The gate diameter is 0.60 mm. Cavity pressure at gate freeze is 18 MPa. Release of hold pressure before gate freeze has been observed on production lines to increase thread root diameter variation from 0.03 mm to 0.10 mm; the resulting removal torque after pasteurisation falls outside the customer range. Colour changes require 25 purge shots at 235°C; a non-PP carrier masterbatch can shift removal torque by 0.2 N·m because the carrier phase alters the coefficient of friction at the seal surface.
Torque retention is tested according to ASTM D2063 using a constant-speed digital torque analyser set to 2 rpm. After immersion for 30 minutes in 121°C water and cooling to 23°C, removal torque must remain between 0.6 N·m and 1.4 N·m. The linerless seal consists of a continuous inner seal bead and an outer tamper-evident band. A seal bead height variation greater than 0.03 mm across the circumference produces a 10 percent leakage rate under a 40 cm Hg vacuum test. Food-contact compliance is assessed under FDA 21 CFR 177.1520(c) and EU 10/2011 Annex I. The terminal product is a closure for pasteurised 500 mL juice drinks. The closure is not recommended for carbonated soft drinks above 2.5 volumes of carbon dioxide unless the panel thickness and knurl depth are redesigned because the tamper-evident strip torque can exceed 0.8 N·m in current trials.
Inside a class ISO 7 cleanroom according to ISO 14644-1, a 32-cavity injection mould running HD631CF produces 120 mL urine collection cups with a 0.80 mm nominal wall and a 4.5 mm snap-ring undercut. The press is a 120-tonne electric machine with a 30 mm screw. Barrel set points are 210°C to 230°C, and the mould temperature is held at 20°C ±1°C. Injection velocity is 100 mm/s; hold pressure is 39 MPa; cooling time is 6.0 seconds and overall cycle is 8.6 seconds. The snap-ring undercut is released with a mechanical core lifter rather than a stripper plate because the rim requires a flat sealing surface. Peak cavity pressure spread across the 32 cavities is controlled to 2.8 percent to prevent flash at the snap ring. The screw and hot-runner system are purged with a medical-grade acrylic compound before production; any lot with visible black specks is rejected under ISO 10993-5 cytotoxicity grade 0 requirements.
The moulded cup is tested according to USP <661.1> and USP <87>. Physicochemical acceptance includes pH shift not more than 0.5 units and non-volatile residue not more than 12 mg when extracted at 70°C for 24 hours. The cup withstands a 121°C autoclave cycle for 15 minutes without visible deformation when a 0.455 MPa flexural load is applied according to ISO 75-2:2013. Electron-beam sterilisation at 25 kGy produces a colour shift delta E of 2.4 and retains 88 percent of the original notched Charpy impact energy; gamma sterilisation at 25 kGy produces amber discolouration and must be validated per lot. The terminal product is a sterile 120 mL urine collection cup with a snap lid for clinical use.
When a 64-cavity hot-runner platform is used for 1.5 mL microcentrifuge tubes, the conical body wall tapers from 0.55 mm at the lower portion to 1.10 mm at the rim. Melt temperature is set at 235°C at the nozzle and mould temperature at 21°C. Injection pressure at transfer is 95 MPa; hold pressure is 55 MPa and is maintained for 2.4 seconds. Each cavity is fitted with a piezoelectric pressure sensor; the coefficient of variation of peak cavity pressure across 64 cavities must remain below 3.2 percent. Tube-to-tube mass variation is controlled to 0.010 g or less for a nominal part weight of 0.42 g. The hinge joining the lid to the tube is gated at the tab; its thickness is 0.25 mm and requires a parting line wear limit of 0.01 mm to avoid flash that alters closing force. Regrind use is prohibited in this application unless a closed-loop recovery line is qualified and the gel count remains below 5 per 500 tubes.
The tubes are certified as RNase/DNase-free by lot validation and are tested for cytotoxicity to ISO 10993-5 grade 0. The resin is evaluated under USP <661.1> physicochemical protocols. Autoclavability is verified at 121°C for 20 minutes; the tube mouth diameter must not shrink more than 0.4 percent to maintain closure integrity at 16,000 g. The terminal product is used in benchtop centrifuges. Published HD631CF-specific data for prolonged radioisotope or enzyme solution contact beyond 24 hours is limited, so the application is excluded from such storage without further migration screening.
| Application segment | Regulatory standard | Test method | Control limit |
|---|---|---|---|
| Thin-wall dairy container | FDA 21 CFR 177.1520(c), EU 10/2011 | EN 1186-1:2002 overall migration | ≤ 10 mg/dm² |
| Linerless closure | FDA 21 CFR 177.1520(c), EU 10/2011 | ASTM D2063 torque retention | 0.6–1.4 N·m after 121°C immersion |
| Clinical urine cup | USP <661.1>, USP <87> | ISO 10993-5 cytotoxicity | Grade 0; pH shift ≤ 0.5 units |
| Microcentrifuge tube | USP <661.1>, ISO 10993-5 | Autoclave dimensional check | Mouth diameter shrinkage ≤ 0.4% |
Fan shroud components for a portable air purifier are moulded with a 0.8 mm nominal wall grid and a 420 mm × 310 mm footprint on a 320-tonne hydraulic press equipped with three sequential valve-gated nozzles. Valve-gate sequencing shifts the primary weld line away from the central fan hub and into the outer ring. Weld-line strength at the hub is checked by machining an unnotched Charpy specimen from the part and testing at 23°C according to ISO 179-1/1eU; the acceptance limit is 6.5 kJ/m². The core cooling circuit is held at 18°C and the cavity circuit at 24°C to control differential shrinkage; the part is held at 35 MPa for 3.5 seconds and cooled for 12 seconds, giving a total cycle of 22 seconds. Dimensional checks are performed after 48 hours at 23°C/50% RH and after 24 hours at 70°C. Shrinkage perpendicular to flow is 1.1 to 1.4 percent and parallel to flow is 0.7 to 1.0 percent. The assembled shroud around a 12 V DC brushless fan is checked for hub ring runout against a dial gauge; total indicated runout must remain within 0.8 mm.
The unfilled grade must satisfy UL 94 HB for the application; it is not qualified for unattended appliance parts that require an 850°C glow-wire end product test without an insulating barrier. Ageing at 70°C for 24 hours is performed before final dimensional acceptance. The terminal product is an air purifier fan shroud used in a 45 watt appliance. The grade is not used in fan shrouds in contact with unshielded motors above 90°C because the 0.455 MPa heat deflection temperature measured according to ISO 75-2:2013 is lower than the long-term service temperature in that location; a talc-filled grade is specified downstream of the motor housing.
Under a 23°C and 50 percent relative humidity conditioning atmosphere, injection-moulded lids for 20 L industrial pails are inspected for stack deflection, hinge breakage, and closure torque. The two-cavity stack mould produces a 1.6 mm wall with a 60 mm diameter centre gate on a 400-tonne hydraulic press. Melt temperature is held at 225°C at the nozzle; mould temperature is 12°C. Fill time is 1.3 seconds; hold pressure is 45 MPa for 6.0 seconds; cooling time is 23 seconds. The lid is removed at a surface temperature of 28°C and placed in a flat press cooling fixture for 60 seconds to prevent curl. The finished lid is subjected to a top-load test of 900 N for 60 seconds; permanent set must remain below 1.5 percent. The pail and lid assembly is certified under UN 1H2 for solid and non-hazardous fillers; drop testing after 48 hours at 40°C is conducted at 1.2 m and 1.8 m and must show no rupture. Stacking of three pails for 48 hours at 40°C must not produce a lid-to-pail engagement loss of more than 0.5 mm. Compliance with EU 10/2011 is not required for industrial use; REACH and RoHS 2011/65/EU are required for heavy metal and phthalate limits. The terminal product is a 20 L pail lid for water-based emulsion packaging. Hydrocarbon or oxidising chemical storage is excluded unless a specific environmental stress cracking resistance test is completed because the unfilled polypropylene grade is sensitive to sustained hoop stress in the presence of aggressive liquid media.
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Within the medium-flow polypropylene injection-molding segment, the commercial grade MARLEX PP HD631CF is positioned as a homopolymer-based material for thin-wall packaging, closures, and small appliance components. The grade is specified by lot-level certificates of analysis rather than by a single fixed datasheet, and compliance testing is typically performed against ISO 1133-1:2022 for melt mass-flow rate, ISO 527-2:2012 for tensile properties, ISO 179-1/1eA:2010 for Charpy impact resistance, and ISO 75-2:2013 for deflection temperature under load. Converters should note that the full designation contains manufacturer-specific family and additive-package coding; therefore, any interpretation of the HD or CF suffixes must be confirmed against the current technical datasheet rather than inferred from general polypropylene nomenclature.
Because the material is used predominantly in thin-wall tools with flow-length-to-wall-thickness ratios exceeding 150:1, the interaction between melt temperature, mold temperature, and holding pressure determines dimensional stability. For medium-flow polypropylene homopolymers of this class, barrel profiles are typically maintained between 210°C and 250°C, with nozzle temperature in the range 230–250°C. Mold temperature is a critical lever: water-cooled tools between 20°C and 40°C favor cycle-time reduction but increase frozen-in orientation and hence anisotropic shrinkage; elevated mold temperatures between 50°C and 60°C reduce orientation but extend cooling time. Holding pressure is generally set between 50% and 80% of peak injection pressure, with peak injection pressures in the range 70–140 MPa for molds with conventional runner systems. Because published data for this specific configuration is limited, these ranges are class-typical and must be verified by in-mold pressure studies on the designated tool.
Post-mold dimensional change is assessed according to ISO 294-4; homopolymer grades of this class commonly exhibit 24-h molding shrinkage between 1.0% and 1.8% in flow and transverse directions, depending on nucleating agents and cooling uniformity. Warpage becomes pronounced when differential shrinkage across the thickness exceeds approximately 0.2–0.5 percentage points, particularly in flat lid geometries with abrupt changes in wall thickness. Processors may reduce warpage by balancing core and cavity cooling, by using sequential valve gating, or by increasing holding time to complete gate freeze before pressure decay. Polypropylene is not hygroscopic, but condensation on stored pellets can cause surface splay at melt temperatures below 220°C if warehouse relative humidity exceeds 60%. Pre-drying for 2–4 h at 80°C using a desiccant dryer is therefore recommended when condensation is observed, though this does not constitute hydrolytic degradation risk as in polyamides or polyesters.
Secondary crystallization in polypropylene can continue for several days after molding and contributes to shrinkage changes between 24 h and 7 d; when tolerances are tighter than 0.1 mm, dimensional inspection should be delayed or accelerated annealing should be performed at 80°C for 2 h per ISO 294-4 recommendations. This behavior differentiates HD631CF from random copolymers in applications where post-mold dimensional stability is more critical than clarity or impact.
Rheologically, the suffix 631 in the grade designation is conventionally associated with a nominal melt mass-flow rate of 6.3 g/10 min when measured under 230°C and 2.16 kg load per ISO 1133-1:2022. A melt-flow value in this region places the material in the medium-flow injection-molding range, where spiral-flow lengths are sufficient for multi-cavity closures and thin-wall cups but not so high that impact resistance and melt strength are degraded to the extent seen in high-flow textile grades. Because the melt-flow rate alone does not capture shear-thinning behavior, capillary rheometry or in-line rheo-kinetic measurements are recommended for tools with long hot-runner drops or restricted gates. Published data for this specific grade under high-shear capillary conditions is limited; therefore, the certificate of analysis and the manufacturer’s application engineering data should be used for gate and runner design.
When tooling is run at an artificially low mold temperature to shorten cycle time, the skin region freezes rapidly while the core remains molten. This creates a crystallinity gradient across the wall, with the skin exhibiting a lower crystalline fraction and the core developing higher crystallinity during slower post-filling cooling. Differential scanning calorimetry according to ISO 11357-3 can quantify the melting enthalpy of microtomed layers; a gradient in melting enthalpy exceeding 3 J/g between skin and core is often associated with increased warpage and reduced dimensional stability in flat polypropylene parts. The grade’s additive package, if nucleated, shifts the non-isothermal crystallization peak to higher temperatures and reduces spherulite size, thereby narrowing the crystallinity gradient under identical cooling conditions relative to a non-nucleated homopolymer.
In hot-runner molds with long residence times, care must be taken to avoid degradation-induced reduction in crystallization temperature. Residence-time studies on production-scale injection machines have shown that polypropylene homopolymers can begin to shift their crystallization exotherm downward by 1–3°C after extended hold-up at temperatures above 260°C in the barrel and hot runner. The operational boundary therefore includes a recommended maximum melt temperature of 250°C for this class, unless the lot-specific stabilizer package is verified for higher thermal exposure. Gate design should provide shear rates below 100,000 s⁻¹ to avoid excessive molecular orientation and surface defects.
Thermal endurance of polypropylene is governed by the antioxidant package and its migration kinetics in the polymer matrix. Long-term heat-ageing testing is performed according to ISO 4577:1983 or ASTM D3012, with tensile elongation retention monitored after oven exposure at 100°C and 120°C. For medium-flow homopolymer grades of this family, published industry data indicate that oxidative induction time values correlate with stabilizer concentration but are not sufficient alone to predict service life in fatty-food contact; specific migration testing under EU Regulation (EU) No 10/2011 is required for each conversion route. The grade falls within the olefin polymer scope of FDA 21 CFR §177.1520 when used with appropriate antioxidants and processing aids, and the finished article must comply with the total migration limit of 10 mg/dm² or 60 mg/kg under the applicable food simulant.
Organoleptic performance in closure and container applications is evaluated by sensory methods rather than by a single polymer specification. Low-molecular-weight fractions, catalyst residues, and oxidized species can impart taste or odor; therefore, converters should request lot-specific organoleptic screening data when the grade is intended for potable water or dairy packaging. The material should be processed under nitrogen purge if regrind levels exceed 25%, and hot-runner cleaning cycles must be documented to prevent cross-contamination with acetal or styrenic residues that may compromise taste neutrality.
The principal differentiator in the MARLEX PP product family is the base polymer architecture. Homopolymer grades such as HD631CF provide higher tensile modulus and heat resistance than random copolymers, but they exhibit lower impact resistance and higher haze. Random copolymers introduce ethylene into the chain to reduce crystallinity and improve clarity; impact copolymers incorporate a dispersed elastomer phase to improve low-temperature impact resistance at the expense of stiffness and heat deflection. The following table presents category-level property ranges extracted from published ISO 19069-2:2020 data for polypropylene molding and extrusion materials; these are not lot-specific values for HD631CF but provide the comparative framework against which the certificate of analysis should be interpreted.
| Property | Test method | Homopolymer category | Random copolymer category | Impact copolymer category |
|---|---|---|---|---|
| Density | ISO 1183-1:2019 | 0.900–0.910 g/cm³ | 0.895–0.905 g/cm³ | 0.890–0.910 g/cm³ |
| Tensile modulus | ISO 527-2:2012 | 1200–1800 MPa | 900–1400 MPa | 1000–1600 MPa |
| Notched Charpy at 23°C | ISO 179-1/1eA:2010 | 2–5 kJ/m² | 5–12 kJ/m² | 10–40 kJ/m² |
| Deflection temperature 0.45 MPa | ISO 75-2:2013 | 90–110°C | 80–100°C | 80–105°C |
| Optical clarity | ASTM D1003-21 | Moderate to high haze | Low haze | Opaque |
For quality systems governed by ISO 9001:2015 and ISO 22000:2018, the following test designations and regulatory clauses are commonly requested from converters. This matrix does not replace the manufacturer’s product stewardship declaration, but it identifies the standard references that should appear in supplier quality agreements for food-contact polypropylene.
| Standard or regulation | Scope | Typical lot-release or compliance requirement |
|---|---|---|
| ISO 1133-1:2022 | Melt mass-flow rate | Lot certificate |
| ISO 527-2:2012 | Tensile modulus and yield stress | Lot certificate or type approval |
| ISO 179-1/1eA:2010 | Notched Charpy impact | Type approval |
| ISO 75-2:2013 | Deflection temperature | Type approval |
| ISO 11357-3:2018 | Melting and crystallization enthalpy | Nucleation consistency audit |
| FDA 21 CFR §177.1520 | Olefin polymers for food contact | Finished article compliance |
| EU Regulation (EU) No 10/2011 | Plastic food contact materials | Specific migration limits |
| REACH Regulation 1907/2006 | SVHC communication | Article-level declaration |
| RoHS Directive 2011/65/EU | Restricted substances in EEE | Pb, Cd, Hg, Cr(VI), PBB, PBDE below thresholds |
On production-scale injection lines, the most commonly observed bottleneck is not plasticating capacity but cooling-limited cycle time in multi-cavity tools with wall thicknesses below 1.5 mm. When mold cooling circuits are sized for laminar rather than turbulent flow, heat-transfer coefficients fall below 1000 W/m²·K, and the resulting cycle-time extension can reach 15–25% relative to isothermal tooling assumptions. Clamp-force requirements for thin-wall closures are typically governed by projected area multiplied by cavity pressure; with cavity pressures in the range 25–40 MPa during filling, a machine with clamp force below the calculated threshold will flash the parting line. Processors should verify that the selected injection unit can deliver the required shot volume within 60–70% of the barrel capacity and that the hot-runner system can maintain a melt temperature of 230–250°C without residence times exceeding 8–10 min at full throughput. Published data for this specific grade under high-speed thin-wall molding is limited, so commissioning on the intended tool remains the definitive validation step.