Dow Hdpe Dmda 8007 Health

Dow HDPE DMDA-8007 HEALTH+

    • Product Name: Dow HDPE DMDA-8007 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 809050
    Polymertype High Density Polyethylene (HDPE)
    Density 0.965 g/cm³
    Meltindex 8.0 g/10 min at 190°C/2.16 kg
    Tensileyieldstrength 31 MPa
    Tensileelongationatbreak 600%
    Flexuralmodulus 1370 MPa
    Notchedizodimpact 53 J/m
    Vicatsofteningtemperature 128°C
    Heatdeflectiontemperature 73°C at 0.45 MPa
    Shoredhardness 66
    Moldshrinkage 0.015–0.025 in/in
    Processingmethod Injection Molding
    Form Pellets
    Color Natural
    Odor Odorless
    Regulatorycompliance USP Class VI, ISO 10993, FDA 21 CFR 177.1520

    As an accredited Dow HDPE DMDA-8007 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-8007 HEALTH+ is supplied in 25 kg polyethylene bags, palletized and stretch-wrapped for safe transport.
    Container Loading (20′ FCL) Dow HDPE DMDA-8007 HEALTH+ loaded in 20′ FCL: palletized 25 kg bags, dry container, evenly distributed and secured for ocean shipment.
    Shipping Dow HDPE DMDA-8007 HEALTH+ typically ships as a non-hazardous solid polyethylene resin in sealed bags, boxes, or octabins on pallets. It is not regulated for transport under DOT, IMDG, or IATA. Store dry, away from heat, and follow local shipping regulations.
    Storage Store Dow HDPE DMDA-8007 HEALTH+ in its original, unopened bags or containers in a cool, dry, well-ventilated area. Protect from direct sunlight, moisture, excessive heat, and ignition sources. Keep away from strong odors, contaminants, and incompatible chemicals. Palletize securely, avoid puncturing bags, and follow first-in, first-out stock rotation. Consult the SDS for detailed handling and storage requirements.
    Shelf Life Typically 24 months when stored in original, unopened packaging under cool, dry conditions, away from direct sunlight.
    Application of Dow HDPE DMDA-8007 HEALTH+

    Dow HDPE DMDA-8007 HEALTH+ Application Scenarios

    In extrusion blow molding of dry oral solid-dose containers, the grade is processed as a monolayer parison on shuttle or long-stroke machines equipped with 24:1 to 30:1 L/D barrier screws and axial or radial wall-thickness programmers. The melt temperature window is 175–205 °C, with head and die zones held 5–10 °C below the screw-tip melt temperature to stabilize parison hang strength. Nominal density of 0.958 g/cm3 (ASTM D1505) and melt index of 0.76 g/10 min at 190 °C/2.16 kg (ASTM D1238) produce sufficient die swell for pinch-off weld integrity in 30–125 mL tablet and capsule bottles. That swell does not compensate for poor die-gap centering on worn accumulator plungers; off-center parison creates side-wall thinning and cap-land ovality that cannot be corrected later. For round tablet bottles, blow mold temperature is typically controlled at 10–30 °C, and cycle time is dominated by base flash and neck calibration rather than body-wall cooling. A 100 mL bottle with a 0.7–0.9 mm body wall can be cooled in 8–14 s on water-cooled aluminum tooling, but the deflashed pinch-off tail must remain below 0.5 mm to avoid cap torque failure. In this segment the resin is run without color concentrates containing amide slip or antistatic additives unless a downstream USP <661.1> extractables profile has been revalidated. The polymer falls under FDA 21 CFR 177.1520(c) 2.1 for olefin polymers, and the HEALTH+ designation is controlled for low odor and taste transfer using organoleptic panel protocols aligned with ASTM E1870. Tablets and capsules are protected primarily by top-load performance and moisture resistance; design verification commonly requires top-load retention above 250 N for a 60 mL round bottle after conditioning at 40 °C/75% RH for 72 h, although published data for DMDA-8007 at this exact geometry is limited. The most frequent production failure mode is not resin degradation but inconsistent parison length when closed-loop regrind exceeds 20 wt%, because first-generation recycled flake can reduce hang strength; regrind is therefore limited to 15–20 wt% unless online melt-flow monitoring is available.

    What Changes When the Same Grade Moves from Dry Oral Solids to Aqueous Liquid Formulations?

    Aqueous liquid oral formulations shift the dominant failure mode from top-load compression to environmental stress cracking. Syrups, suspensions, and preservative-containing oral liquids require heavier wall sections and improved pinch-off welding because filled bottles are exposed to surfactants, high-osmolarity solutes, and repeated handling stress. The resin is typically molded into 200–500 mL bottles with body-wall thickness from 0.8 mm to 1.5 mm, and the parison programmer must reduce the shoulder transition from neck to body below a 3:1 thickness ratio to avoid stress concentration. Environmental stress cracking resistance is evaluated by ASTM D1693 in 10% Igepal CO-630 at 50 °C; F50 values are used as a release criterion, but the actual formulation must be tested because high sugar content, sodium benzoate, and certain flavoring compounds can accelerate cracking beyond Igepal screening. Mold temperature becomes a process conflict: raising mold temperature from 15 °C to 30 °C improves residual stress relaxation and ESCR, but for a 250 mL syrup bottle with a 1.2 mm body wall, cavity residence time can rise from 14 s to 22 s. Excessively low mold temperatures below 10 °C freeze residual stress near the pinch-off weld and reduce F50 in demanding preservative systems. The finished syrup bottle is paired with PP child-resistant caps and induction seals; leak testing commonly follows USP <671> container–closure integrity protocols. Regulatory anchors include USP <661.1> and European Pharmacopoeia 3.1.3 for polyolefins. Long-term contact with iodine-based sanitizers, strong oxidizers, or concentrated aromatic oils is not recommended because surface crazing and chain scission can occur; compatibility under the actual fill formulation is mandatory before commercial use.

    Compliance anchors for DMDA-8007 HEALTH+ by downstream segment
    SegmentResin-side standardCritical test condition
    Dry oral solid-dose bottlesFDA 21 CFR 177.1520(c) 2.1; USP <661.1>Water and ethanol extractables at 70 °C for 24 h
    Aqueous oral liquidsUSP <661.1>; EP 3.1.3ESCR by ASTM D1693 in 10% Igepal CO-630 at 50 °C
    Ophthalmic dropper bodiesUSP <661.1>; EP 3.1.5UV absorbance 220–350 nm; total organic carbon after 80 °C water contact
    Diagnostic reagent bottlesUSP <661.1>; internal buffer-challenge protocolsGC-MS screening after hexane reflux; TOC at 80 °C for 24 h
    Topical personal careFDA 21 CFR 177.1520(c) 2.1; EU 10/2011Overall migration according to food-contact or cosmetic packaging conditions
    Nutritional canistersFDA 21 CFR 177.1520(c) 2.1; EU 10/2011Water vapor transmission by ASTM F1249 at 38 °C/90% RH

    Small-volume ophthalmic dropper bodies impose parison weight tolerances that press against the lower melt-flow boundary of the grade. A 7 mL dropper bottle with a 0.55–0.70 mm body wall requires a parison weight repeatability of ±0.15 g at total shot weights below 10 g; this is achieved on accumulator-head machines with servo-driven parison profiles rather than hydraulic cylinder stop adjustment. The high melt strength of the 0.76 g/10 min resin prevents excessive sag during transfer from head to mold, but the same melt strength reduces flow into embossed dropper tip threads. Molders compensate by raising die temperature to 190–200 °C and using high-cavity venting along the thread splits. For ophthalmic packaging, extractables are evaluated under USP <661.1> and, when required by regional submissions, EP 3.1.5 for polyethylene with additives for ophthalmic preparations. Color concentrates are avoided because FDA-compliant pigments can alter the extractable metal profile unless individually listed. Sterilization is usually performed with ethylene oxide or gamma irradiation at application-validated doses; HDPE retains baseline tensile yield after gamma doses up to 25 kGy, but transmission FTIR can show an upward carbonyl-index drift at higher accumulated exposure, indicating oxidative embrittlement. Repeated sterilization of the same container is therefore not permitted without dose audits. The finished dropper bottle is assembled with an LDPE or TPE dropper tip and an HDPE or PP cap; cap torque retention after sterilization is a more sensitive indicator of neck dimensional change than body-wall tensile strength.

    If Diagnostic Reagent Bottles Demand Lot-to-Lot Extractable Consistency, the Resin Must Be Evaluated Against Buffer Challenge Tests

    Diagnostic reagent bottles and buffer reservoirs introduce mixed-solvent exposure that is not covered by pharmaceutical aqueous extractables alone. A 250–1000 mL blow-molded bottle for phosphate-buffered saline or Tris-EDTA buffer is commonly filled with solutions containing trace surfactants, sodium azide, or organic solvents such as ethanol and dimethyl sulfoxide at concentrations below 5 vol%. Under these conditions, the critical resin attribute is not density but the concentration of low-molecular-weight oligomeric species that can migrate from the wall into the reagent and interfere with ultraviolet absorbance or fluorescence calibration curves. Lot-to-lot consistency is assessed by total organic carbon in purified water at 80 °C for 24 h, UV absorbance at 220–350 nm, and GC-MS screening after hexane reflux per USP <661.1> or internal release protocols. The HEALTH+ control is intended for low extractables, but diagnostic manufacturers must still verify the bottle under their specific buffer because phosphate species can extract external mold-release contamination if tooling maintenance is poor. On the production floor, the main defect is side-wall haze contacted by methanol-containing reagents because rapid cooling in unpolished aluminum cavities creates a fine spherulitic skin that scatters light. Polishing mold surfaces and raising mold temperature to 30–40 °C reduces haze but extends cycle time and can lower top-load creep resistance if the bottle is not ejected immediately from the cavity. Finished reagent bottles are normally packaged with leak-resistant PP closures and may require lot-specific leachables documentation for clinical diagnostic or laboratory accreditation.

    Topical health and personal care packages with snap-hinged dispensing closures add an impact and hinge-fatigue requirement to the same blow-molded monolayer. A 150 mL oval HDPE bottle for emollient lotion or medicated shampoo must survive closure hinge cycling of 200–300 open/close events after the bottle has been filled and capped with a PP closure. The hinge region is not part of the bottle, but cap-land ovality and flash at the neck ring change rotational alignment of the closure and can produce a visible lean that consumers detect. The density of 0.958 g/cm3 provides high wall stiffness, allowing down-gauging to 0.55–0.75 mm for lotion bottles; however, the same stiffness reduces flexural fatigue resistance when panels are repeatedly squeezed. Designers avoid sharp shoulder radii below 2 mm and use radiused transitions to reduce strain concentration. In this segment the packaging is generally not sterile, so the regulatory anchor is FDA 21 CFR 177.1520(c) 2.1 plus food-contact or cosmetic packaging requirements; no additional USP drug master file is invoked unless the product is an OTC topical drug with a monographed packaging requirement. Molders report that gloss variation across the bottle surface is the most frequent batch-to-batch observation; this is governed by mold core temperature distribution rather than resin lot variation and is minimized by turbulent flow in drilled cooling channels with 10–15 °C water and balanced circuit lengths.

    Nutritional Powder Canisters and Effervescent Tablet Tubes Under Multi-Lane Extrusion Blow Molding

    Nutritional powder canisters and effervescent tablet tubes place the grade in a heavier parison range where melt strength and die swell must be balanced against output. Typical canister volumes range from 400 mL to 1500 mL, with body-wall thickness from 0.9 mm to 1.8 mm; effervescent tablet tubes are smaller but require a tight internal diameter to prevent tablet rattling and a desiccant-canister interference fit. On multi-lane extrusion blow molding lines, parison weight variation across cavities must be held below ±0.3 g for canisters because fill-line capacity sensing rejects underweight containers before filling. The resin is hydrophobic, so pre-drying is not required unless surface condensation has formed during outdoor storage in humid environments; wet regrind produces splay at the die lip. In nutritional packaging, moisture ingress is the primary barrier concern, and water vapor transmission is determined by ASTM F1249 at 38 °C/90% RH. HDPE provides a moderate moisture barrier for powder products with low hygroscopicity, but desiccants or foil inner seals are still required for high-moisture-sensitive formulations. Compliance is anchored to FDA 21 CFR 177.1520(c) 2.1 and EU 10/2011, and the HEALTH+ organoleptic control supports products where taste and odor carry-over from packaging is unacceptable. Production experience shows that the heaviest canister parisons can fold against the mold face if the pre-blow delay is too long; the delay is therefore set between 0.3 s and 0.8 s after mold closure, depending on parison length. The finished canisters are deflashed, leak-tested, and packed with snap-on lids or screw closures, with pinch-off welds inspected for thickness uniformity because a wedge-shaped weld can reduce drop-impact retention at refrigerated storage temperatures.

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    Certification & Compliance
    More Introduction

    Dow HDPE DMDA-8007 HEALTH+ is a blow-molding-grade high-density polyethylene homopolymer supplied in pellet form for healthcare packaging applications. The HEALTH+ designation reflects raw-material selection, additive discipline, and supply-chain documentation rather than a change to the polyethylene backbone. Representative physical and mechanical values are provided in Table 1. The melt flow rate is nominally 0.80 g/10 min when measured at 190 °C under a 2.16 kg load according to ASTM D1238; this places the grade in the high-viscosity region of extrusion blow-molding resins and differentiates it from injection-molding HDPE grades with melt flow rates above 10 g/10 min. Density is approximately 0.959 g/cm³ by ASTM D792, and the associated crystalline fraction contributes to elevated modulus and moisture barrier while reducing low-temperature impact relative to linear low-density polyethylene. The grade is intended for rigid containers in which parison hang strength, pinch-off integrity, and consistent wall thickness are critical. Published data for the exact extractables profile under every pharmacopeial monograph is limited; specification locking should therefore rely on lot-specific certificates of analysis and the finished-container manufacturer’s migration and biocompatibility studies.

    Table 1. Representative physical and mechanical values for Dow HDPE DMDA-8007 HEALTH+
    PropertyTest methodRepresentative value
    DensityASTM D7920.959 g/cm³
    Melt flow rate, 190 °C/2.16 kgASTM D12380.80 g/10 min
    Tensile strength at yieldASTM D63828 MPa
    Elongation at breakASTM D638>200%
    Flexural modulusASTM D7901,380 MPa
    Notched Izod impactASTM D2566.5 kJ/m²
    Vicat softening temperatureASTM D1525128 °C
    Shore D hardnessASTM D224068

    Extrusion blow molding of DMDA-8007 HEALTH+ is commonly performed on continuous shuttle or reciprocating screw machines equipped with 24:1 to 30:1 L/D single-screw extruders and accumulator heads. Melt temperatures between 180 °C and 210 °C are preferred. At melt temperatures below 170 °C, the high viscosity of this resin increases backpressure, reduces output, and may produce surface roughness at high shear rates. Above 220 °C, thermal oxidation can generate odour-active and taste-active compounds unless oxygen is excluded from the feed path. Die-head settings between 180 °C and 205 °C commonly provide stable parison formation. Mold temperatures from 10 °C to 25 °C aid dimensional recovery of the cooled container. Predrying is not routinely required if the pellets remain sealed; surface moisture above <0.05 wt% should be removed by desiccant drying at 80 °C for 2 h to avoid splay in thin walls. In-house trim can be re-extruded at up to 20 wt% without measurable loss of drop impact in many processes, provided the regrind is free of polyvinyl chloride, polyethylene terephthalate, and paper fibre. Higher regrind fractions, particularly above 30 wt%, may depress environmental stress crack resistance and should be validated on the target packaging line.

    What regulatory starting points apply to DMDA-8007 HEALTH+?

    The base polyolefin is covered by 21 CFR 177.1520(c) as a high-density polyethylene for food-contact articles, but that status does not constitute approval of a finished medical device or pharmaceutical container. For the European market, polyethylene containers may be evaluated against European Pharmacopoeia monograph 3.1.3 for polyolefins and 3.1.5 for polyethylene with additives, depending on the route of administration and the container function. Biocompatibility of the finished container is article-dependent and is generally assessed under ISO 10993-1:2018, with in vitro cytotoxicity evaluated by ISO 10993-5:2009 and irritation and sensitisation by ISO 10993-10:2014. Chemical characterisation of the finished device may be required under ISO 10993-18:2020. A raw resin cannot be certified as ISO 10993 compliant by itself; the blow-molding process, mold release agents, regrind fractions, and sterilization dose all contribute to the final biological risk profile. Suppliers may provide regulatory statements or change-control documentation for the HEALTH+ grade, but the responsibility for device-level evidence remains with the finished-container manufacturer.

    Blow-fill-seal lines impose tighter parison heat-history control than conventional shuttle blow molders. On blow-fill-seal platforms, DMDA-8007 HEALTH+ is typically processed at melt temperatures from 190 °C to 220 °C. The resin’s low melt flow rate and narrow molecular weight distribution provide enough melt strength to resist sag across multiple die openings, but the high viscosity may raise extruder discharge pressure when narrow die gaps are used. Surface melt fracture can occur if extruder output exceeds the critical shear stress of the polymer; die geometry and melt temperature should be adjusted before increasing screw speed. The pinch-off weld formed at the base and shoulder of the container remains the most mechanically vulnerable region. Burst testing under ASTM F1140-19 and bubble leak testing under ASTM F2096-12 are commonly used for container integrity. Dye penetration or vacuum decay can further resolve sub-visible channels in the weld. Tool alignment, clamp force, and melt temperature must be held within narrow limits because the grade’s narrow molecular weight distribution reduces tolerance for weld-line variation.

    Gamma irradiation stress crack resistance and mechanical retention

    Sterilization by gamma irradiation at 25 kGy to 50 kGy can initiate free-radical reactions that continue after the container leaves the irradiation cell. In high-density polyethylene, post-irradiation oxidation may reduce elongation at break and increase sensitivity to environmental stress cracking in the presence of aqueous surfactants or alcohol-water solutions. Published data for this specific DMDA-8007 HEALTH+ configuration is limited; general HDPE behaviour indicates that oxygen-barrier overwrap, minimum headspace oxygen, and controlled post-sterilization aging are necessary to reduce embrittlement. Electron-beam processing at equivalent dose often causes less oxidative damage because of shorter exposure time, but dose uniformity across thick flanges or closures must be validated. Steam autoclaving is not recommended above 110 °C for load-bearing containers because the Vicat softening temperature of the grade is approximately 128 °C; distortion can occur under pressure and cavity vacuum. If steam cycles above 110 °C cannot be avoided, the container must be rigidly fixtured and the cycle qualified for dimensional stability and closure-torque retention.

    Compared with injection-molding HDPE grades with melt flow rates of 10 to 30 g/10 min, DMDA-8007 HEALTH+ exhibits higher melt strength and greater parison hang time but is not suitable for fast thin-wall injection molding because high cavity pressures and premature gate freeze overwhelm conventional injection equipment. Compared with broad-molecular-weight film or sheet HDPE, the grade has fewer low-molecular-weight species and is controlled for high-molecular-weight tail, which can support lower extractables after correct processing; this does not remove the need for finished-container migration and leachable studies. Among blow-molding HDPE grades of similar density, differences in die swell ratio, swell recovery time, and orientation-induced impact can be larger than the difference indicated by melt flow rate alone. These processing parameters should be compared on the target machine because product data sheets rarely report die swell or sag time.

    When polypropylene random copolymer is considered as a replacement

    If a substitution from polypropylene random copolymer to DMDA-8007 HEALTH+ is evaluated, the design must account for lower flexural modulus, higher density, and lower continuous service temperature. The HDPE grade provides better moisture barrier and often better environmental stress crack resistance in aqueous surfactant formulations, but it will not survive autoclave cycles at 121 °C that are routine for some polypropylene containers. The material is incompatible with strong oxidising acids, concentrated aromatic solvents, and some chlorinated hydrocarbons; prolonged contact can soften the polymer, initiate stress cracking, or increase extractable levels. Contact with unsaturated oils at elevated temperatures should be assessed case by case because swelling can occur. Whenever a polymer substitution is made, dimensional stability, closure interference, and drop impact at cold-chain temperatures must be revalidated on the finished package.

    The following checklist is a starting point for specification review; it does not represent a finished-device regulatory file or a supplier certification for a specific container.

    Table 2. Compliance checklist for specification review
    DesignationScopeApplication to DMDA-8007 HEALTH+
    21 CFR 177.1520(c)Olefin polymers for food contactBase HDPE falls within scope; finished-article extraction testing required
    EU 10/2011Plastic food-contact materialsOverall migration and specific migration limits apply to the finished article
    Ph. Eur. 3.1.3 / 3.1.5Polyolefin and polyethylene containersCompliance is established on the container, not the resin alone
    ISO 10993-1:2018Biological evaluation of medical devicesDevice-level risk assessment required
    ISO 10993-5:2009In vitro cytotoxicityTesting on final container or extracts
    ISO 10993-10:2014Irritation and sensitisationArticle-specific; cannot be claimed from resin type alone
    REACH (EC) 1907/2006SVHC contentSupplier statement required; no intentional SVHC addition
    RoHS 2011/65/EURestricted substancesPolyolefin typically compliant; analytical confirmation needed

    Resin storage should be in sealed original packaging at ambient temperatures below 40 °C and away from direct sunlight. If the material is used within 12 months of the certificate date, drying is usually not required if packages remain closed. Bags exposed to condensation or airborne contamination should be quarantined, dried at 80 °C for 2 h, and requalified before use.

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