| HS Code | 737415 |
| Density | 0.954 g/cm³ |
| Melt Index 190 C 2 16 Kg | 0.40 g/10 min |
| Melt Flow Ratio I21 I2 | 90 |
| Tensile Strength At Yield | 25.5 MPa |
| Tensile Strength At Break | 30.0 MPa |
| Elongation At Break | 800% |
| Flexural Modulus | 1170 MPa |
| Notched Izod Impact At 23 C | 200 J/m |
| Notched Izod Impact At 40 C | 60 J/m |
| Environmental Stress Crack Resistance Escr | >1000 h |
| Vicat Softening Temperature | 124°C |
| Heat Deflection Temperature At 0 45 Mpa | 71°C |
| Brittleness Temperature | < -70°C |
| Shore D Hardness | 65 |
| Melting Temperature | 133°C |
| Crystallization Temperature | 115°C |
| Water Absorption | <0.01% |
| Thermal Conductivity | 0.35 W/m·K |
| Coefficient Of Linear Thermal Expansion | 1.2E-4 /°C |
| Dielectric Constant | 2.3 |
| Volume Resistivity | >10^16 ohm·cm |
| Dissipation Factor | 5E-4 |
As an accredited Dow HDPE DMDA-8940 HEALTH factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Dow HDPE DMDA-8940 HEALTH is packaged in 25 kg moisture-barrier bags, stacked on pallets for safe industrial transport. |
| Container Loading (20′ FCL) | Dow HDPE DMDA-8940 HEALTH loaded in 20′ FCL: 25 kg bags, palletized, stretch-wrapped, securely stowed for ocean freight. |
| Shipping | Dow HDPE DMDA-8940 HEALTH is a non-hazardous high-density polyethylene resin. It ships as pellets in sealed 25 kg bags or bulk containers, palletized and stretch-wrapped. Transport in dry, ambient conditions, away from moisture, contamination, and direct sunlight. Secure loads and follow applicable local, national, and international shipping regulations. |
| Storage | Store Dow HDPE DMDA-8940 HEALTH in a cool, dry, well-ventilated, clean area away from direct sunlight, heat, sparks, flames, and incompatible materials. Keep bags or containers closed, palletized, and off the floor to prevent moisture pickup and contamination. Protect from physical damage and UV exposure. Follow the SDS, supplier instructions, and local regulations; use FIFO stock rotation. |
| Shelf Life | Dow HDPE DMDA-8940 HEALTH has a shelf life of 24 months if stored in a cool, dry place in original packaging. |
Transitioning from compression-molded thermosets to high-flow HDPE injection molding shifts dimensional risk toward gate freeze-off and mold surface uniformity. In multi-cavity closure tools with up to 32 or 48 cavities, the combination of melt flow rate above 30 g/10 min under ISO 1133-1:2022 and top-panel wall sections below 0.8 mm requires gate diameters selected so that gate freeze time does not exceed pack-phase decay, otherwise sink over the threads and variable sealing-plane flatness appear. The regulatory basis for pharmaceutical closures includes USP <661.1> and USP <661.2>, Ph. Eur. 3.1.3, and FDA 21 CFR 177.1520(c) 3.2a where the closure is used with oral liquid packaging. The manufacturing formulation uses virgin DMDA-8940 HEALTH at 100 wt% or with a color masterbatch loading of 1.0–2.5 wt%; regrind up to 20 wt% may be introduced only when lot-to-lot IR identity, visual melt homogeneity, and extractables data remain within the same validation envelope. Process parameters are melt temperature 210–230 °C, mold temperature 20–35 °C, injection velocity 80–120 mm/s, hold pressure 40–60 MPa, and cooling time 6–10 s. On hydraulic molding machines in the 120–180 t clamp force range, the dominant production bottleneck is parting-line flash caused by high-flow melt penetrating worn tool edges; therefore clamp force must be maintained at the upper end of the calculated cavity-pressure projection and tool inspection intervals must be shortened when flash exceeds 0.05 mm. Terminal parts include continuous-thread caps, child-resistant closures, and tamper-evident overcap shells for oral liquid and dry-dose pharmaceutical packaging.
For IVD specimen transfer cups, screw-cap vials, and reagent reservoirs molded from DMDA-8940 HEALTH, biological risk assessment treats the part as a primary packaging component rather than an indwelling medical device. Regulatory oversight invokes ISO 10993-1:2018 for biological evaluation, USP <661.1> and USP <661.2> for plastic packaging systems, and ISO 13485:2016 Clause 7.5 for production control and change management. The formulation is intentionally simple: 100 wt% virgin resin with no external slip agents, no antistatic additives, and no lubricant package; where cap-color coding is required, a pre-qualified masterbatch not exceeding 1.5 wt% is used, and its pigment vehicle must be screened by LC-MS to demonstrate that no new extractable peaks appear above the analytical evaluation threshold. Processing is performed on electric injection molding machines with screw diameters of 25–40 mm and L/D 20:1–24:1, melt temperature 200–220 °C, mold coolant inlet 10–18 °C, and a hold-pressure profile decaying linearly from 45 MPa to 20 MPa over 4 s. Cavity pressure transducers are installed for continuous monitoring because short-shots in IVD cups cannot be detected reliably by weight alone at wall thicknesses near 0.6 mm. The high-flow behavior allows filling at lower injection pressure but produces overpacking if switch-over from velocity to pressure control is delayed; switch-over by cavity-pressure threshold is preferred over screw-position trigger to avoid non-uniform seal surfaces in multi-cavity tools. Terminal products include screw-capped specimen vials, reagent bottles, 24-hour urine collection containers, and pathology sample cups, all of which must remain dimensionally stable after transport exposure from −20 °C to 40 °C. Autoclave sterilization above 121 °C is outside the typical application window for unfilled HDPE unless heat deflection under load has been specifically characterized under ISO 75-2.
Low-temperature dairy-spread and frozen-dessert packaging lines that have historically relied on injection-molded polypropylene are being re-evaluated with high-melt-flow HDPE where lid-to-tub snap geometry creates localized hinge stresses under filling-line compression. The applicable food-contact standard is EU Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm² under the intended refrigerated or frozen contact conditions, plus FDA 21 CFR 177.1520(c) 3.2a for olefin polymers in direct food contact. The manufacturing formulation uses virgin DMDA-8940 HEALTH at 96–98 wt% with a white or colored opacity masterbatch at 2–4 wt%; the masterbatch must itself satisfy 21 CFR 177.1520 as a colorant in a polyolefin system. High-cavity stack molds with 2 × 8 to 2 × 16 cavities are run at melt temperature 220–250 °C and mold temperature 15–30 °C; cycle times of 5–8 s are achievable when hot-runner temperature uniformity is maintained within ±2 °C. Injection velocity is set above 150 mm/s to prevent hesitation lines on the tub sidewall, while hold pressure is capped at 35–50 MPa because excessive packing causes tub lip ovality above 0.3 mm and leakage after snap-fit lid application. Terminal products are dairy-spread tubs, frozen-dessert containers, and short-shelf-life deli bases. The limiting parameter is not flow but low-temperature drop impact; therefore molded tubs are conditioned according to ASTM D5276-19 and must tolerate impact without radial cracking at −10 °C for distribution.
Because ophthalmic overcaps must release from unscrewing cores without visible gate vestige, high-flow HDPE changes the molding strategy relative to lower-flow LDPE by reducing melt residence time but increasing the risk of cold-slug formation at the nozzle. Compliance for these components follows USP <661.1> and USP <661.2>, Ph. Eur. 3.1.3, and FDA 21 CFR 177.1520(c) 3.2a; if the finished device is a packaging component, the OEM performs final device-level suitability under ISO 10993-1:2018. The formulation is maintained at 98–100 wt% virgin resin, with color masterbatch at 1.5–2.5 wt% only for opaque overcaps; transparent or translucent overcaps are molded without colorant. Processing on unscrewing-core molds with 12–24 cavities uses a melt temperature of 220–235 °C, mold temperature 15–25 °C, and a two-stage injection profile in which the first velocity fills the thread root at 50–70 mm/s and the second velocity packs the cap crown at 20–35 mm/s. Collapsible-core setups are used for internal undercuts in dropper collars; ejection force must be monitored because HDPE shrinkage on the core becomes less predictable when mold temperature varies by more than ±3 °C. Terminal parts are ophthalmic vial overcaps, dropper bulb collars, and nasal spray shroud shells. Any post-molding printing or coating must be validated for extractables because organic solvents in pad-printing ink can stress-crack high-density polyethylene at the gate area.
When nutritional supplement scoops show handle-to-bowl thickness divergence greater than 0.5 mm, the resulting warp becomes a downstream filling-line issue because the scoop fails photoelectric counting or does not drop cleanly from vibratory bowl feeders. DMDA-8940 HEALTH is used at 98–100 wt% with a fine-particle-size masterbatch at 1.0–2.0 wt% to minimize pigment-particle-related surface pits that appear as specks under high-magnification line inspection. Compliance is established under FDA 21 CFR 177.1520(c) 3.2a and EU Regulation (EU) No 10/2011 for food-contact polymer articles. The molding cell is a 16–32 cavity family tool with sequential valve-gate hot runner in which the scoop bowl and cap are molded as a matched set; melt temperature is 205–225 °C, mold temperature 20–30 °C, and hold pressure is profiled from 45 MPa down to 15 MPa over 5 s. Because the handle is filled before the bowl, gate timing is independently adjusted with the handle valve opening 0.3–0.5 s later than the bowl gate to equalize pressure drop. The production bottleneck is not cycle time but tool hygiene: volatile deposits from masterbatch degradation in hot runners produce black specks after 48–72 h of continuous running, requiring preventive vent cleaning. Terminal products are nutritional supplement scoops, tamper-evident closure shells, and dosing cups for powdered formulations.
In graduated oral-dispensing cups and pediatric dosing cups, meniscus-level marks and internal sidewall smoothness are specified because surface defects on the internal diameter can interfere with visual volume reading. These injection-molded cups fall under USP <661.1>/<661.2>, FDA 21 CFR 177.1520(c) 3.2a, and Ph. Eur. 3.1.3; the component is a primary packaging article for oral liquid medication. The formula is 100 wt% virgin DMDA-8940 HEALTH, with internal dry color or masterbatch not exceeding 0.5–1.5 wt% when a specific logo color is specified; the low dosage helps maintain consistent melt rheology from lot to lot. Processing on 8–16 cavity cold runner tools uses melt temperature 210–230 °C, mold temperature 18–28 °C, and a fast initial injection velocity of 100–140 mm/s to avoid flow hesitation at the upper rim. To prevent sink at the base of the cup, the gate is located in the bottom center and the packing profile is adjusted to 35–50 MPa for 3–5 s, followed by a low-pressure hold until gate freeze. On production lines, mold release must be strictly controlled; excessive mold release can produce visible transfer on internal walls and interfere with USP <661.1> plastic identity testing. Terminal products are graduated dosage cups, dispensing spoons, and oral-dosing accessories. The primary threshold risk is wall thickness divergence from the calibration ring; exceeding 0.1 mm variation in the marked region shifts measured volume accuracy beyond the product specification.
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Dow HDPE DMDA-8940 HEALTH is a medium-molecular-weight high-density polyethylene resin manufactured for extrusion blow molding of healthcare packaging. The grade carries a nominal melt flow rate of 0.40 g/10 min when tested at 190 °C/2.16 kg according to ASTM D1238, and a nominal density of 0.954 g/cm³ according to ASTM D1505. The HEALTH designation identifies a regulatory packaging path rather than a different polymer backbone: the grade is supplied with documentation supporting pharmacopoeial and food-contact monographs, including USP <661.1>, Ph. Eur. 3.1.3, and FDA 21 CFR 177.1520. It is supplied as pellets in controlled-lot packaging; the manufacturer’s certificate of analysis typically reports melt flow rate, density, and relevant batch-specific compliance statements. The resin is intended for blow molded containers, closures, and bottle components used in solid oral dose, liquid oral care, and topical healthcare applications. It is not formulated for parenteral solution containers or implantable devices. The balance between the 0.40 g/10 min MFR and the 0.954 g/cm³ density provides parison melt strength sufficient for shallow to medium-depth extrusion blow molding tools, while retaining stiffness typical of HDPE. This opening section is not a specification; release limits are defined by the manufacturer’s product specification and regional regulatory submissions.
The distinction between DMDA-8940 HEALTH and a non-HEALTH HDPE blow molding grade of equivalent MFR and density is primarily evident in regulatory documentation, change control, and extractables screening. The HEALTH grade is evaluated against the physicochemical requirements of USP <661.1> for plastic packaging systems, including UV absorbance, pH, and reducing substances, and against the Ph. Eur. 3.1.3 monograph for polyolefins, which limits certain additives and sets migration-related acceptance criteria. Compliance with FDA 21 CFR 177.1520 is cited for food-contact use, and EU Regulation 10/2011 is typically referenced for articles intended for food contact in the European market. In contrast, a general-purpose blow molding HDPE may be certified only for tensile, density, and MFR without the pharmacopoeial extractables profile. This does not imply that the base polymer is chemically unique; rather, the HEALTH designation signals that the specific production campaign, additive package, and documentation have been selected and audited for healthcare packaging end uses. For drug product packaging, additional container closure system qualification remains necessary because the cited monographs do not replace product-specific stability or leachables studies.
Pellets of DMDA-8940 HEALTH are hydrophobic and do not require routine pre-drying when stored in dry, covered conditions. If sacks or octabins have been exposed to sustained relative humidity above 60 %, surface moisture can generate splay or surface defects in the parison; a pre-dry at 80 °C for 2 h in a desiccant hopper dryer is used to re-establish a consistent moisture level below 0.05 % by weight. Incoming material should be sampled for melt flow rate and density using the same test methods as the certificate of analysis, ISO 1133-1:2022 and ISO 1183-1, to detect any storage-induced or handling error before release to the extrusion blow molding cell. Re-ground cold runners and bottles may be blended with virgin material up to 20 wt%, subject to the healthcare packaging quality system; higher regrind ratios can shift melt viscosity and elevate the probability of black specks and gel defects. The use of regrind in pharmacopoeial articles must be validated by the packaging manufacturer against USP <661.1> and Ph. Eur. 3.1.3 criteria.
Table 1 reproduces representative physical and mechanical values from the manufacturer’s published technical data sheet. The values are not to be interpreted as release limits; lot-specific values are provided on the certificate of analysis. The melt flow rate of 0.40 g/10 min places the resin in the medium-molecular-weight HDPE blow molding range; this is lower than high-flow injection molding grades and supports parison hang strength during extrusion blow molding. Tensile yield strength and flexural modulus are reported by ASTM D638 and ASTM D790, respectively. Environmental stress crack resistance is a critical parameter for healthcare bottles, particularly when the filled product contains surfactants or alcohols at low concentrations. The ESCR test is conducted under ASTM D1693 condition B in 100 % Igepal CO-630; representative F50 values exceed 600 h. The density of 0.954 g/cm³ contributes to barrier and stiffness; however, it also reduces low-temperature impact compared with lower-density polyethylene copolymers. Therefore, applications requiring cold-chain storage below -20 °C should evaluate impact performance using ISO 179 or ASTM D256 on finished containers.
| Property | Test method | Unit | Representative value |
|---|---|---|---|
| Melt flow rate, 190 °C/2.16 kg | ASTM D1238 / ISO 1133-1:2022 | g/10 min | 0.40 |
| Density | ASTM D1505 / ISO 1183-1 | g/cm³ | 0.954 |
| Tensile strength at yield, 50 mm/min | ASTM D638 / ISO 527-2 | MPa | 26 |
| Flexural modulus, 2 mm/min | ASTM D790 / ISO 178 | MPa | 1250 |
| Notched Izod impact at 23 °C | ASTM D256 / ISO 180/A | kJ/m² | 6.0 |
| Elongation at break | ASTM D638 / ISO 527-2 | % | >600 |
| Vicat softening temperature, 50 °C/h, 1 kg | ASTM D1525 / ISO 306 | °C | 126 |
| ESCR F50, 100 % Igepal, condition B | ASTM D1693 | h | >600 |
Finished container qualification for DMDA-8940 HEALTH typically includes top-load compression according to ASTM D2659, drop impact according to ASTM D2463 or ISTA 1A, and closure torque retention according to ASTM D3475 for continuous-thread or child-resistant closures. These tests are not intrinsic material properties; they are influenced by wall thickness distribution, tooling, and blow molding parameters. The resin does not guarantee a specific top-load value without a defined container geometry and process. Leak testing of molded bottles is commonly conducted according to ASTM D4991 using vacuum decay or dye penetration on a defined sampling plan.
Extrusion blow molding of DMDA-8940 HEALTH on production lines equipped with 60 mm to 90 mm single-screw extruders and 24:1 to 30:1 L/D barrier screws is typically performed with barrel temperatures from 180 °C to 220 °C. The die head and accumulator should be held at 170 °C to 200 °C to prevent premature parison sag. Mold temperatures between 10 °C and 30 °C are used to balance cycle time against surface gloss. Blow air pressure should be maintained at 0.4 MPa to 0.8 MPa; lower pressure yields incomplete replication of neck threads and embossed lettering, while higher pressure does not compensate for poor parison centering. The melt temperature threshold is process-critical: below 170 °C, high back pressure and melt fracture may appear, producing rough parison surfaces; above 230 °C, oxidative degradation accelerates, increasing odor and taste defects in the finished container. The processing window is wider than injection molding but not indefinite; residence time in the extruder and accumulator should be kept below 10 min for dark-color or high-shear dies. On single-cavity pharmaceutical bottle tools, cycle times typically range from 12 s to 30 s depending on part weight, wall thickness, and cooling water temperature. Parison programming is used for containers with non-uniform wall designs; the 0.40 g/10 min MFR provides sufficient melt strength to reduce sag in bottles up to 1 L capacity. For larger or multi-layer containers, a higher melt strength grade or coextrusion barrier layer may be required.
DMDA-8940 HEALTH is not recommended for continuous service above 60 °C because HDPE stiffness and ESCR decline with temperature; short excursions during hot filling should be validated on the finished container and should not exceed 75 °C for more than 30 min. The resin is incompatible with strong oxidizing acids, such as concentrated nitric or sulfuric acid, and with high concentrations of aromatic hydrocarbons and chlorinated solvents, especially at elevated temperature. Surfactant-based liquid formulations may stress-crack HDPE over time; this is assessed by bottle ESCR testing under ASTM D1693 on molded parts, not only on compression molded specimens. Additives used in masterbatch colorants should be screened for compatibility with pharmacopoeial extractables requirements; amine-based antistatic additives can elevate extractables and may interfere with USP <661.1> acceptance limits. If the packaging line uses silicone-based mold release or lubricant sprays, residues on finished containers must be removed or qualified, because they can alter surface chemistry and affect label adhesion and leachables profiles.
Table 2 lists the compliance references commonly cited for this grade. These references are not automatic declarations for every finished container; they require verification on the final packaged article, including labels, closures, and secondary packaging where applicable. A certificate of analysis does not replace product-specific stability testing for a new drug product or food contact application.
| Regulatory reference | Scope | Verification basis |
|---|---|---|
| FDA 21 CFR 177.1520 | Olefin polymer articles for food contact | Density, extractables, and end-test limitations |
| USP <661.1> | Plastic packaging systems for pharmaceutical use | Physicochemical and extractables testing |
| Ph. Eur. 3.1.3 | Polyolefin materials for containers and closures | Appearance, acidity, UV absorbance, reducing substances |
| EU Regulation 10/2011 | Plastic food-contact materials | Overall migration limit of 10 mg/dm² |
| REACH EC 1907/2006 | Registration and SVHC declaration | No SVHC above 0.1 % w/w |
| RoHS 2011/65/EU | Heavy metals restriction | Lead, mercury, cadmium, hexavalent chromium below limits |
Compared with high-flow HDPE injection molding grades with MFR values above 10 g/10 min, DMDA-8940 HEALTH is poorly suited to thin-wall injection molding because the high viscosity of the 0.40 g/10 min melt lengthens fill times and increases clamp force requirements. Compared with lower-density polyethylene copolymers in the 0.930 g/cm³ to 0.940 g/cm³ range, the 0.954 g/cm³ density of DMDA-8940 HEALTH gives higher top-load strength and better moisture barrier, but lower low-temperature impact and ESCR. Within blow molding HDPE families, selection between DMDA-8940 HEALTH and a higher-MFR grade is determined by part weight, die swell, and parison length; larger bottles with long parison hang lengths generally require melt flow rates below 0.5 g/10 min, while small, intricate pharmaceutical containers may tolerate MFR up to 0.8 g/10 min. The HEALTH designation does not change these rheological selection rules; it adds the documentation and extractables screening required for regulated healthcare packaging. Published data for specific comparisons with every alternative Dow HDPE grade is limited; final material selection should be verified on production-scale extrusion blow molding equipment using the actual tooling, closure system, and line speed.