Dow Hdpe Dmda 8920 Health

Dow HDPE DMDA-8920 HEALTH+

    • Product Name: Dow HDPE DMDA-8920 HEALTH+
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 480048
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.954 g/cm³
    Melt Index 190 C 2 16 Kg 20 g/10 min
    Tensile Strength At Yield 29 MPa
    Tensile Elongation At Break 1000%
    Flexural Modulus 1300 MPa
    Vicat Softening Temperature 127 °C
    Heat Deflection Temperature 0 45 Mpa 73 °C
    Brittleness Temperature < -70 °C
    Shore D Hardness 66
    Environmental Stress Crack Resistance 30 h
    Water Absorption <0.01%
    Melting Temperature 133 °C
    Crystallization Temperature 118 °C
    Mold Shrinkage 0.015–0.025 in/in

    As an accredited Dow HDPE DMDA-8920 HEALTH+ factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Dow HDPE DMDA-8920 HEALTH+ is supplied in 25 kg polyethylene bags, palletized and stretch-wrapped for secure storage and transport.
    Container Loading (20′ FCL) 20′ FCL loaded with Dow HDPE DMDA-8920 HEALTH+ in 25 kg bags, palletized, shrink-wrapped, and secured for ocean shipment.
    Shipping Dow HDPE DMDA-8920 HEALTH+ is typically shipped as a non-hazardous polyethylene resin. Use sealed 25 kg bags or 1000 kg bulk bags, palletized and stretch-wrapped. Store cool, dry, away from sunlight, heat, and contaminants. No dangerous goods labeling generally required; follow SDS and local rules.
    Storage Store Dow HDPE DMDA-8920 HEALTH+ in a cool, dry, well-ventilated area, away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep in original, tightly closed packaging on pallets, off the floor, protected from moisture, dust, odors, and contamination. Maintain moderate ambient temperatures below 50°C, practice first-in-first-out rotation, avoid prolonged UV exposure, and use clean handling equipment.
    Shelf Life Recommended shelf life: 24 months in original unopened packaging, stored cool, dry, well-ventilated, away from direct sunlight.
    Application of Dow HDPE DMDA-8920 HEALTH+

    In solid oral dose packaging lines running continuous shuttle extrusion blow molding, DMDA-8920 HEALTH+ is processed as a neat, pre-stabilized high-density polyethylene blown container resin. The grade is characterized by a density of 0.954 g/cm³ per ASTM D792-20 and a melt index of 0.9 g/10 min per ISO 1133-1:2022; these values place the material in the high-molecular-weight, high-melt-strength segment for narrow-finish 30–250 mL tablet and capsule bottles. Compliance for primary drug packaging requires conformity to USP <661.1> for plastic packaging systems, Ph. Eur. 3.1.3 for polyolefins, and FDA 21 CFR 177.1520(c) 3.1 for olefin polymers used under aqueous, acidic, and low-alcohol contact conditions. On accumulator-head and reciprocating-screw shuttle lines producing 60–100 mL two-parison bottle sets, the resin is delivered from a 24:1 L/D single-screw extruder with a barrier screw and a feed zone maintained at 170–180°C, a compression zone at 185–200°C, and a die head at 195–210°C. Batch-to-batch melt-index variation of ±0.1 g/10 min produces a 2–3% shift in parison length on shuttle lines; incoming lots are therefore pre-qualified by capillary melt flow and die-swell measurement before line start-up. Wall-thickness programming on a 30-point parison controller maintains sidewall variation within ±0.15 mm at the label panel and ±0.25 mm at the pinch-off, which is critical because the pinched flash region concentrates residual stress and is the primary failure origin in closure torque testing per ISO 8317 for child-resistant packages attached to the bottle finish. Formulation addition is limited to a high-purity polyethylene carrier color masterbatch at 0.5–1.5 wt%; no additional antioxidant or slip additive is recommended because the grade contains a pre-dosed stabilizer system, and external slip additives above 0.2 wt% can create label adhesive delamination and increase surface extractables. The terminal finished types are amber and white 30 cc, 60 cc, 100 cc, and 250 cc oral solid dose bottles with tamper-evident induction seal liners and child-resistant closures, intended for direct distribution of compressed tablets, capsules, and oral lyophilisates.

    Does Environmental Stress Crack Resistance Govern Liquid Oral Dose Container Design?

    High-viscosity pediatric syrup and oral suspension containers in the 100–500 mL size range are produced on accumulator-head extrusion blow molding lines with a 25:1–30:1 L/D extruder and a grooved feed throat that conveys the 0.954 g/cm³ resin without flooding at screw speeds above 90 rpm. The critical application-specific parameter is environmental stress crack resistance measured per ASTM D1693 Condition B, 100% Igepal CO-630, where a molded bottle sidewall is exposed to surfactant and elevated temperature to determine the onset of cracking. Because liquid oral formulations often contain 0.1–0.5 wt% polysorbate or sorbitol-based non-ionic surfactants, the container wall must be designed to maintain a minimum wall thickness of 0.6 mm in the bottom-chine region and 0.8 mm in the handle-bearing shoulder, where parison hang-time variation on large tools creates thin spots. Compliance for oral liquid primary packaging under European Union jurisdiction falls under EU Regulation 10/2011 for plastic food contact materials unless the product is registered as a drug; in pharmaceutical applications, compliance is demonstrated to Ph. Eur. 3.1.3 and USP <661.1>, with extractables profiling per USP <1663> when the bottle is exposed to a 40°C aqueous simulant for 10 days. The compounding step for colored oral liquid bottles incorporates 0.5–1.0 wt% of a high-purity liquid-dispersible masterbatch and optionally 0.1–0.3 wt% of a polydimethylsiloxane-based external lubricant only when parison stacking lines are observed at the neck flash; however, slip addition above 0.3 wt% reduces heat-transfer coefficient and produces cold spots at the mold parting line. Production machines are typically dual-station shuttle or rotary wheels with mold clamping force of 8–15 tons per cavity, mold cooling inlet temperature 12–18°C, and cycle times of 14–22 s for a 250 mL bottle with a 28 mm neck finish. Terminal finished types are amber and opaque white liquid oral dose bottles for syrups, oral suspensions, pediatric electrolyte solutions, and iron/nutritional supplements; all containers are leak-tested in-line at 0.02–0.04 MPa differential pressure before discharging.

    Narrow-neck topical irrigation and antiseptic bottle bodies impose parison programming windows below ±10°C

    Compared with solid oral dose bottles, topical irrigation containers blow molded from DMDA-8920 HEALTH+ require narrower parison programming windows because the high-density backbone of the resin raises melt viscosity; at melt temperatures below 190°C the parison exhibits melt fracture at the die lip, while above 215°C the stabilizer package begins to produce visible specks and elevated volatile residues. The acceptable melt-temperature envelope is therefore ±10°C around a 205°C center, and the die-head temperature must be held 5–8°C cooler than the metering zone to maintain parison diameter uniformity. These containers are produced on continuous shuttle machines equipped with 20–25:1 L/D single-screw extruders and converging die mandrels; the blow pin is designed as a 9:1 length-to-diameter rotary unit to minimize bore-surface scratches in the neck finish. Compliance for these products includes FDA 21 CFR 177.1520(c) 3.1 for the resin, USP <661.1> for the packaging system, and ISO 10993-1:2018 for biocompatibility evaluation when the bottle is classified as a medical device accessory for wound irrigation. Formulation addition is typically a high-opacity white masterbatch at 1.0–2.0 wt% to reduce light transmission into the stored solution, and no external processing aid is used because the masterbatch already includes a low-viscosity HDPE carrier that reduces head pressure; adding a secondary amide slip agent must be avoided because amides migrate to the inner surface and alter surface tension of the fluid path. Production processes include in-line controlled flow-head extrusion with 100-point radial parison programming for the neck and body geometry, followed by automated trimming and leak testing at 0.04 MPa for 4 s. The resulting terminal products are rigid HDPE topical irrigation bottles, antiseptic wash bottles, and wound-cleansing containers in 100 mL, 250 mL, and 500 mL configurations, usually paired with a screw-top cap or twist-open tip.

    For in-vitro diagnostic reagent bottles, DMDA-8920 HEALTH+ is selected where the resin’s pre-dosed stabilizer package yields a lower total organic carbon background than general-purpose blow molding HDPE when extracted in high-purity water under USP <1663> conditions. The downstream production process is four-cavity shuttle extrusion blow molding on 24:1 L/D extruders, with the melt pressure entering the die limited to 220–260 bar to prevent shear-induced degradation and the mold temperature maintained at 10–20°C to reduce crystallinity-driven shrinkage below 1.2%. Compliance for in-vitro diagnostic reagent bottles in the European market requires conformity to IVDR (EU) 2017/746 for the assembled medical device, a quality management system audited to ISO 13485:2016, and chemical compliance with REACH Annex XVII restrictions for phthalates and heavy metals; the resin is also qualified under FDA 21 CFR 177.1520 when the buffer or reagent is incidental to a food/clinical sample. Formulation constraints are stricter than for oral solid dose packaging: the addition ratio of colorant masterbatch is held to 0.1–0.3 wt% and only high-purity titanium dioxide or carbon black carriers are allowed because higher levels reduce the signal-to-noise ratio in optical detection systems that read through the bottle wall. No external slip, antistat, or processing aid is added to diagnostic reagent bottles because these additives create low-molecular-weight extractables that can interfere with enzymatic and chemiluminescent assays. Terminal finished types are 50 mL, 125 mL, 250 mL, and 1000 mL narrow-mouth reagent bottle bodies with tamper-evident screw necks, often fitted with drip-free polypropylene closures or dispenser tips; the bottle bodies are used for wash buffers, diluents, staining reagents, and transport media.

    Application segmentPrimary standardSpecific clause/monographTest methodOperational limit
    Solid oral dose containersFDA 21 CFR177.1520(c) 3.1USP <661.1>Parison wall variation ±0.15 mm at label panel
    Liquid oral dose bottlesPh. Eur.3.1.3ASTM D1693 Condition B, 100% Igepal CO-630Minimum wall 0.6 mm bottom chine
    Topical irrigation bottlesFDA 21 CFR177.1520(c) 3.1ISO 10993-1:2018Melt window ±10°C around 205°C
    Diagnostic reagent bottlesIVDREU 2017/746ISO 13485:2016Colorant 0.1–0.3 wt%
    Medical device secondary packagingISO11607:2019ISO 11137-1:2006Gamma dose 15–25 kGy
    Oral nutritional supplement bottlesFDA 21 CFR177.1520EN 1186 or USP <1663>Neck inner diameter ±0.05 mm

    When Medical Device Secondary Packaging Requires Gamma-Sterilization Compatibility

    Medical device and combination-product manufacturers that select HDPE for secondary containment vessels must address the resin’s oxidative response to ionizing radiation. DMDA-8920 HEALTH+ can be blow molded on accumulator-head machines into rigid containers for pre-filled swab systems, specimen collection tubes, and device accessory trays, but gamma irradiation above 25 kGy induces chain scission and carbonyl formation that raises melt-flow index and causes yellowing; for this reason the grade is generally qualified for a radiation exposure window of 15–25 kGy. Processing for these medical device packaging components uses a 28:1 L/D barrier screw with a vented feed throat under a −0.3 to −0.5 bar vacuum to remove trace volatiles that could later deposit on device surfaces; melt temperature is set at 195–210°C, and the accumulator head is programmed to deliver a 12–18 mm parison into a 2-cavity tool with a 20-ton clamp force per cavity. Compliance for medical device secondary packaging includes ISO 11607:2019 for packaging of terminally sterilized medical devices, ISO 10993-1:2018 for biological evaluation of the plastic component, and AAMI ST98 for cleaning validation if the container is reusable. Formulation addition differs from primary drug packaging in that a high-purity masterbatch is restricted to 0.0–0.5 wt% and only non-leaching inorganic colorants are permitted; at levels above 0.5 wt%, inorganic pigments become points of stress concentration that reduce notched Izod impact strength by approximately 10–15% after irradiation. Published data for this specific blow molded configuration is limited, so post-irradiation qualification is performed on finished containers per ISO 11137-1:2006 and ISO 11607:2019 rather than relying on resin datasheet values alone. Terminal finished types are rigid disposable device accessory containers, specimen transport tubes, and sterile kit trays that are sealed with coated paper or flash-spun polyolefin lids; the HDPE body is not intended as the sterile barrier itself but as the protective secondary container.

    Oral Nutritional Supplement Bottle Extrusion and Oxygen-Transmission Constraints

    When a dry powder nutritional supplement bottle is tooled on a wheel-type continuous blow molder, the 200–500 mL format must be specified with a wall thickness that compensates for the resin’s high oxygen-transmission rate compared with PET. The production route is wheel-type continuous extrusion blow molding with 8–12 stations and 160,000–200,000 finished bottles per 24 h on a single line; parison delivery is through a spider-supported die head with 0.8–1.2 mm adjustable gap, and the mold cooling circuit is operated at 8–14°C with a 0.3–0.5 MPa chilled-water pressure drop to achieve a cycle time of 11–16 s for a 300 mL bottle. Because HDPE has water absorption below 0.01% at 23°C, predrying is not required for bulk moisture, but surface condensation at relative humidity above 60% is removed by a desiccant-bed air sweep on the hopper to avoid splay. Regulatory compliance for oral nutritional supplement primary packaging falls under FDA 21 CFR 177.1520, EU Regulation 10/2011 if the product is regulated as a food, and USP <661.1> if the product is formulated as a dietary supplement in the United States; extractables testing per USP <1663> or food-contact migration testing per EN 1186 is used depending on the market. Formulation addition ratios in this segment are 0.5–1.5 wt% color masterbatch, 0.1–0.2 wt% processing aid only during high-humidity periods when surface condensation is observed on incoming resin, and 0.0–0.5 wt% UV stabilizer only for products stored under uncontrolled retail lighting; adding more than 0.2 wt% external slip is contraindicated because label adhesives and shrink-sleeve films exhibit peel failures on the low-friction surface. Downstream production includes a post-molding cooling station with forced air at 10–15°C and an in-line dimension check using a non-contact laser micrometer that records neck inner diameter ±0.05 mm and body ovality ≤0.5 mm. Terminal finished types are opaque HDPE nutritional supplement bottles for protein powders, meal-replacement dry powder, chewable vitamins, and effervescent electrolyte tablets in non-oxygen-sensitive formats; oxygen-sensitive formulations are either placed in sealed foil pouches inside the HDPE container or sealed in a multilayer barrier overpouch.

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    Certification & Compliance
    More Introduction

    Dow HDPE DMDA-8920 HEALTH+ is an injection-molding grade of high-density polyethylene intended for thin-walled rigid parts in healthcare packaging, closures, and medical device components. The base resin is characterized by a melt flow rate of 20 g/10 min at 190 °C under 2.16 kg load when tested according to ASTM D1238 or ISO 1133-1:2022, and a nominal density of 0.954 g/cm³ at 23 °C according to ASTM D792 or ISO 1183-1:2019. These two values position the grade in the high-flow, high-stiffness end of the HDPE injection-molding range. The high melt index shortens fill time in multi-cavity tools, but it also reduces melt strength relative to blow-molding HDPE grades with melt flow rates below 1 g/10 min.

    Unlike conventional HDPE grades used in extrusion blow molding, DMDA-8920 HEALTH+ is not formulated for high parison sag resistance. The lower melt elasticity requires the melt to be injected under flow-front control rather than inflated against a mold wall; consequently, the product is directed to closed-mold processes such as injection molding and thin-wall injection-compression molding. This distinction is operationally important in converting facilities where HDPE silos are shared: the high-flow grade can purge easily, but screw recovery, shot-size settings, and hold-pressure profiles must be re-established because of the different melt viscosity and shear sensitivity.

    What Melt Rheology Boundaries Govern Thin-Wall Injection Molding of DMDA-8920 HEALTH+?

    At injection shear rates between 10,000 s-1 and 50,000 s-1, the resin exhibits pronounced shear thinning; apparent viscosity drops sufficiently to permit filling of wall sections down to 0.4 mm in multi-cavity tools when gate geometry and venting are correctly designed. The melt temperature window is nonetheless constrained. Below 190 °C, gate freeze and uneven filling become dominant defects, especially in hot-runner systems with subgated pin tips smaller than 0.8 mm. Above 230 °C, thermally driven viscosity collapse can produce gate stringing, part warpage, and additive degradation products. Published data for this specific configuration are limited beyond the manufacturer’s typical property sheet. On production injection machines of this class, a starting barrel profile of 190 °C rear, 200 °C center, 210 °C front, and 210 °C nozzle is commonly evaluated, with mold coolant temperatures held between 15 °C and 40 °C.

    Because the melt flow rate is 20 g/10 min, the injection pressure required for thin-wall parts is lower than that for medium-flow HDPE grades, but clamp force is not correspondingly reduced when flow length-to-thickness ratio exceeds 150:1. Melt pressure at transfer is typically held between 40 MPa and 80 MPa, and holding pressure is set at 60–80% of the peak injection pressure. Inadequate holding pressure produces sink marks over ribs and bosses; excessive holding pressure increases molded-in stress and can contribute to environmental stress cracking when the molded article is exposed to alcohols, surfactants, or disinfectant solutions.

    Table 1 lists representative physical and mechanical values for the base resin. These are typical injection-molding values from the manufacturer’s product data, not specification minima. Mechanical properties were determined on standard ASTM specimens prepared by injection molding.

    Table 1: Representative properties of Dow HDPE DMDA-8920 HEALTH+
    PropertyTest methodTypical value
    Melt flow rate, 190 °C/2.16 kgASTM D123820 g/10 min
    Density at 23 °CASTM D7920.954 g/cm³
    Tensile stress at yield, 50 mm/minASTM D63826 MPa
    Flexural modulus, 1% secantASTM D7901,100 MPa
    Notched Izod impact at 23 °CASTM D25625 J/m
    Deflection temperature under load, 0.455 MPaASTM D64870 °C

    The flexural modulus near 1,100 MPa provides greater wall rigidity than low-density polyethylene or linear low-density polyethylene, permitting down-gauging of containers by approximately 10–15% relative to lower-modulus polyolefins while maintaining similar panel deflection under top load. However, the notched Izod impact value of 25 J/m is lower than that of high-molecular-weight HDPE blow-molding grades, which can exceed 100 J/m; therefore the grade is not selected where impact toughness in thick sections is the controlling requirement.

    Thermal Degradation and Additive Migration Boundaries in Healthcare Packaging

    DMDA-8920 HEALTH+ undergoes the same thermal degradation mechanisms as general-purpose HDPE. Repeated extrusion cycles in the presence of oxygen generate carbonyl species measurable by FTIR as an increase in absorbance near 1,718 cm-1. The practical melt temperature should therefore be held at or below 230 °C, especially in hot-runner tools where residence time at temperature can exceed 15 minutes during startup or machine stoppage. When regrind is used, the ratio should be limited to 30% by weight unless forced-ventilation and antioxidant stability studies support a higher level. The non-hygroscopic character of HDPE means pre-drying is not required unless sacks have been stored in conditions that permit surface condensation at relative humidity above 60%; in that case, 1–2 h at 80 °C is adequate to remove surface moisture and prevent splay.

    Additive migration must be evaluated on the finished article, not on the raw resin. Under Regulation (EU) No 10/2011, overall migration limits and specific migration limits apply to the final plastic article; the grade’s compliance must be demonstrated on the molded component in its intended contact configuration. For medical devices, biological evaluation according to ISO 10993-1 is performed at the article level, and no raw-resin certificate substitutes for that assessment. The HEALTH+ designation indicates a healthcare product stewardship protocol, but published data for this specific configuration are limited beyond the base resin data sheet.

    Table 2: Regulatory and compliance evaluation framework
    Jurisdiction / standardRelevant clause or methodAssessment remark
    United States FDA21 CFR 177.1520(c)Olefin polymers for food contact; final article compliance required
    European UnionRegulation (EU) No 10/2011Overall migration limit 10 mg/dm²; specific migration depends on additives
    US PharmacopeiaUSP <661.1>, <661.2>Plastic packaging systems for pharmaceuticals; article-level testing required
    Biological safetyISO 10993-1Biological evaluation of medical devices; no raw-resin certification
    REACHRegulation (EC) No 1907/2006Substance registration and SVHC screening for the supplied grade

    Sterilization exposure requires molded-part qualification. Gamma radiation and ethylene oxide cycles are commonly evaluated for HDPE, but dose tolerance must be established on the finished component because free-radical crosslinking and chain scission occur simultaneously. Steam autoclaving at 121 °C is generally outside the practical continuous-use temperature range for high-density polyethylene; significant warpage and dimensional relaxation can occur because the deflection temperature under load is approximately 70 °C at 0.455 MPa. Chemical contact with strong oxidizing acids, halogenated solvents, or high concentrations of aromatic hydrocarbons should be avoided; polyethylene swells and may crack under stress in such environments.

    When DMDA-8920 HEALTH+ Replaces Random Copolymer PP in Molded Caps and Medical Device Housings

    The high flow index and density create a different property balance than random copolymer polypropylene. DMDA-8920 HEALTH+ typically exhibits lower heat distortion temperature than random copolymer PP; the 0.455 MPa DTUL of approximately 70 °C is below the 90–100 °C values reported for many PP copolymers. Substitution is therefore limited to applications with service temperatures below 50 °C or with short transient excursions that do not approach the low-load heat distortion value. The advantage is in moisture barrier and flow: high-density polyethylene of this density generally provides lower water-vapor transmission than random copolymer PP at equal wall thickness, though oxygen transmission is higher. The melt flow rate of 20 g/10 min permits lower melt temperature and shorter cycle time in thin-wall lids, caps, and small housings.

    In processing comparisons, random copolymer PP may require mold temperatures of 20–40 °C; DMDA-8920 HEALTH+ operates in a similar coolant band but requires lower melt temperature and shorter hold time because of faster crystallization. On a 130-ton, 16-cavity hot-runner tool molding 0.6 mm wall caps, cycle-time reductions of 5–10% may be achievable relative to a medium-flow PP grade when gate geometry is optimized; however, published data for this specific configuration are limited and tool-specific validation is required. The material also demonstrates lower melt strength than PP, so melt transfer and hot-tip sequencing must be adjusted to prevent gate blush and filament formation.

    Injection Molding Equipment, Clamp Force, and Hot-Runner Sequencing

    High-flow HDPE of this class requires a general-purpose polyolefin screw with a compression ratio between 2.5:1 and 3.0:1 and an L/D ratio of at least 20:1. Slippage on the screw can occur if the feed throat is not cooled; the feed throat should be maintained at 40–60 °C by closed-loop chiller control to prevent bridging and screw stalling. Shot size should be between 30% and 70% of maximum barrel capacity to minimize residence time. Hot-runner manifolds should have streamlined melt channels without dead spots, because high-density polyethylene degrades under long residence at elevated temperature. Mold venting should follow high-flow polyolefin practice with conservative vent depth, because thin-wall filling at high flow rate can otherwise trap air and produce burn marks at the flow front.

    Injection velocity should be selected to avoid jetting. Because the resin fills thin walls rapidly, an excessively high injection speed can create a narrow melt stream that folds onto itself and produces visible flow marks. A medium injection speed with controlled velocity-to-pressure transfer is preferred, with transfer set when the flow front reaches approximately 95% of fill. Clamp force requirements should be calculated from projected part area multiplied by a cavity pressure estimate of 30–50 MPa; machines from 80 to 180 tons are commonly evaluated for multi-cavity production, depending on total projected area and number of cavities.

    Blending with barrier resins such as EVOH or polyamide is not a direct drop-in operation. These polar polymers are immiscible with HDPE; without tie-layer resins, melt separation and delamination occur in the molded article. Similarly, the addition of incompatible color concentrates or antibiotic additives can reduce environmental stress crack resistance and should be qualified using ASTM D1693 under the intended chemical environment. Operational boundaries for DMDA-8920 HEALTH+ therefore include melt temperature control below 230 °C, avoidance of high-moisture storage without pre-drying above 60% relative humidity, and exclusion of powerful oxidizing or aromatic solvents that can swell and stress-crack molded parts.

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