| HS Code | 342553 |
| Product Name | PetroChina Dushanzi HDPE DMDA-8008 |
| Manufacturer | PetroChina Dushanzi Petrochemical Company |
| Polymer Type | High Density Polyethylene (HDPE) |
| Grade | Injection Molding |
| Density | 0.956 g/cm³ |
| Melt Flow Rate | 7.5 g/10 min (190°C/2.16 kg) |
| Tensile Yield Strength | ≥ 25 MPa |
| Elongation At Break | ≥ 500% |
| Flexural Modulus | ≥ 1000 MPa |
| Notched Izod Impact Strength | ≥ 50 J/m |
| Vicat Softening Point | 126 °C |
| Brittleness Temperature | ≤ -70 °C |
| Shore D Hardness | 60 |
| Melting Point | 130 °C |
| Mold Shrinkage | 1.5-3.0% |
| Water Absorption | <0.01% |
As an accredited PetroChina Dushanzi HDPE DMDA-8008 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | PetroChina Dushanzi HDPE DMDA-8008 is supplied in 25 kg woven polypropylene bags, typically palletized for industrial transport and storage. |
| Container Loading (20′ FCL) | PetroChina Dushanzi HDPE DMDA-8008 is loaded in 20′ FCL containers as 25 kg bags, usually bulk-stacked, with approximately 18–20 MT per container. |
| Shipping | PetroChina Dushanzi HDPE DMDA-8008 is typically shipped as a non-hazardous polymer resin in 25 kg woven bags, palletized and stretch-wrapped, or in jumbo bags. Transport in clean, dry containers or trucks, protected from moisture, sunlight, heat, and contamination. Handle carefully to prevent bag tearing; store cool and dry. |
| Storage | Store PetroChina Dushanzi HDPE DMDA-8008 in a cool, dry, well-ventilated warehouse, away from direct sunlight, rain, moisture, heat, sparks, and open flames. Keep original bags sealed, palletized, and clean to prevent contamination. Avoid excessive stacking and prolonged high temperatures. Use appropriate handling to control dust/static. Store per local regulations, away from incompatible materials. |
| Shelf Life | Stored cool, dry, ventilated, away from sunlight, PetroChina Dushanzi HDPE DMDA-8008 typically has a 12-month shelf life in unopened packaging. |
PetroChina Dushanzi HDPE DMDA-8008 is a high-flow injection-moulding grade with a nominal melt mass-flow rate of 8 g/10 min at 190 °C/2.16 kg per ISO 1133-1:2022 and a density of 0.956 g/cm³ per ISO 1183-1:2019. In thin-wall dairy spread tubs and deli containers produced on 250–350 t clamp-force injection-moulding machines with a 22:1 L/D general-purpose polyolefin screw, the practical melt-temperature window is 210–250 °C measured at the nozzle, with a mould temperature of 20±5 °C; the feed-throat temperature is held below 60 °C to prevent bridging. The formulation is 96.0–98.0 wt% virgin DMDA-8008 and 2.0–4.0 wt% white masterbatch carried in an HDPE base that itself meets the same food-contact requirements. The injection profile is set to fill 0.6–1.2 mm sidewall sections in 0.8–1.5 s through hot-runner valve gates, with gate shear rates kept below 10,000 s⁻¹ to limit melt fracture and gate blush; holding pressure is 35–50 MPa, back pressure is 0.5–1.0 MPa, and screw recovery speed is trimmed so that melt residence time at 230 °C does not exceed 6 min. Food-contact compliance is based on FDA 21 CFR 177.1520 for olefin polymers, EU Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm² or 60 mg/kg in final articles, and GB 4806.7-2016 for finished food-contact plastics. If resin stored below 20 °C enters a high-humidity production hall, 2–4 h hopper warming is used; drying is not normally required because moisture absorption of this HDPE grade is below 0.01%. The terminal product types are thin-walled dairy spread tubs, deli containers, and portion cups in the 0.5–2.0 L range, where the high flow rate permits sink-free ribs and snap-fit lid undercuts without exceeding 12 s cooling time.
For screw caps on non-carbonated beverages, dairy bottles, and household chemical containers, the 8 g/10 min melt flow rate of DMDA-8008 moves the injection-pressure requirement below that of fractional-MFI HDPE closure grades, but it also narrows the sealing-torque retention window under creep loading. The closure formulation is typically 98.5 wt% DMDA-8008, 1.0–1.5 wt% colour masterbatch, and 0.5–1.0 wt% slip/anti-block masterbatch; total additive masterbatch is not allowed to exceed 2.0 wt% in food-contact closures to avoid destabilising the olefin polymer basis of FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011. Multi-cavity hot-runner cap moulds with valve gates of 0.8–1.2 mm diameter operate at melt temperatures of 220–240 °C, mould temperatures of 20±5 °C, holding pressures of 40–60 MPa, and cooling times of 6–9 s for a 1.8–2.0 mm nominal skirt wall. On production-scale equipment, the main failure mode is not short-shot filling but loss of removal torque after top-load stacking; therefore closure print torque retention is screened per ASTM D2063-22 over a 24 h interval, and environmental stress-cracking resistance is checked per ASTM D1693-15 condition B for formulations that will contact surfactant-containing liquids. The terminal products are tamper-evident screw caps for still water, dairy drinks, dry grocery jars, and household cleaner bottles; carbonated-beverage closures are excluded from this construct unless the neck finish and liner system are re-validated for carbon dioxide permeation and creep at 4 °C storage.
| Injection-moulded segment | Melt temperature at nozzle | Mould temperature | Injection/hold pressure | Typical clamp force |
|---|---|---|---|---|
| Thin-wall dairy food packaging | 210–250 °C | 20±5 °C | 35–50 MPa | 250–350 t |
| Non-carbonated beverage closures | 220–240 °C | 20±5 °C | 40–60 MPa | 200–350 t |
| Open-head industrial pails | 225–245 °C | 20–30 °C | 80–100 MPa | 700–1000 t |
| Stackable agricultural crates | 225–245 °C | 15–25 °C | 45–65 MPa | 800–1400 t |
Open-head pails of 5 L, 10 L, 20 L, and 25 L capacity for food powders, paints, and non-hazardous chemicals are injection-moulded with DMDA-8008 at 100 wt% for food-grade pails, or with up to 15 wt% clean in-house regrind from the same grade for industrial pails; in UN-certified dangerous-goods pails, recycled content is excluded or re-certified under the national competent authority. The downstream process uses single- or two-cavity cold-runner moulds, clamp forces of 700–1000 t, melt temperatures of 225–245 °C at the nozzle, mould temperatures of 20–30 °C, injection pressures of 80–100 MPa, and a stepped holding-pressure profile with total hold time of 12–18 s. Sink marks at the handle pinch-off are controlled by packing the undercut area with 45–60 MPa for 3–5 s after fill; wall thickness is maintained at 1.5–2.5 mm. Compliance is anchored to FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011 for food-grade pails, and to the UN Model Regulations Chapter 6.1 packaging performance tests for pails intended for regulated goods, including drop and stacking tests. Terminal product types include open-head pails with tamper-evident lids for food ingredients, decorative coatings, and industrial liquids, but hot filling above 60 °C or contact with oxidising acids requires chemical resistance validation beyond the standard food-contact test battery.
For stackable agricultural crates, meat/fish totes, and distribution boxes, DMDA-8008 is blended at 70–85 wt% with 15–30 wt% recycled HDPE crate regrind in non-food industrial applications; where the crate contacts food directly, only virgin DMDA-8008 is used to keep the material declaration within the olefin polymer boundary of EU Regulation (EU) No 10/2011 or FDA 21 CFR 177.1520. The injection-moulding process involves two-plate cold-runner tools with clamp forces of 800–1400 t, melt temperatures of 225–245 °C, mould temperatures of 15–25 °C, and a profiled injection velocity that starts at 60–80 mm/s to fill the lower ribbed sections before decelerating in the rim area. Holding pressure is 45–65 MPa, cooling time is 18–30 s for 3.5–5.0 mm nominal wall thickness, and the mould opening is delayed until the rib root temperature falls below 80 °C to reduce warpage. Field-scale data from production lines indicates that the lower notched impact of an 8 g/10 min HDPE relative to fractional-MFI crating grades, as measured by ISO 179-1:2010, makes sharp internal corners and gate placement more critical; ribs must be radiused at no less than 0.5 mm and gates should not be located in load-bearing corners. Stacking performance is evaluated under ISO 2234:2000 or ASTM D642-20, while pallet-box versions are tested under ISO 8611-1:2011; terminal product types are stackable crates, ventilated agricultural totes, and fold-down logistics containers in the 20–70 L volume class.
DMDA-8008 is used in toy blocks, storage boxes, and housewares where fast filling and short cycle time are decisive; the formulation is 98.0–99.0 wt% DMDA-8008 with 1.0–2.0 wt% heavy-metal-free masterbatch selected against EN 71-3:2019+A1:2021 migration thresholds and ASTM F963-17 total heavy-metal limits. Multi-cavity cold-runner injection tools produce parts with wall thicknesses of 1.2–2.5 mm at melt temperatures of 210–240 °C, mould temperatures of 15–25 °C, injection/hold pressures of 30–50 MPa, and total cycle times of 12–20 s. Compliance is established under REACH Regulation (EC) No 1907/2006 Annex XVII for phthalate restrictions, EN 71-3:2019+A1:2021 for soluble element migration, and ASTM F963-17 for heavy-metal content in toy substrates. The terminal product type covers injection-moulded toy construction blocks, storage boxes with integrally moulded snap-fit closures, and household hangers; components requiring prolonged hot-water immersion above 70 °C or dishwasher exposure in load-bearing parts are excluded from the standard DMDA-8008 processing window unless post-moulding annealing is introduced.
As a masterbatch and additive-compound carrier, DMDA-8008 is used at 60–80 wt% as the HDPE matrix with 20–40 wt% pigment or mineral additive in a co-rotating twin-screw extruder with 40:1 L/D, barrel temperatures of 160–200 °C, screw speeds of 400–800 min⁻¹, and strand pelletizing under a water bath; the carrier is subject to REACH Regulation (EC) No 1907/2006 registration and the masterbatch must be re-certified for EU Regulation (EU) No 10/2011 or FDA 21 CFR 177.1520 if it enters food-contact end-articles; terminal product types are pelletized HDPE masterbatches and filled compound granules for injection moulding and blow moulding.
Competitive PetroChina Dushanzi HDPE DMDA-8008 prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618136850665
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
PetroChina Dushanzi HDPE DMDA-8008 is a high-density polyethylene supplied by PetroChina Dushanzi Petrochemical Company for injection moulding of short-cycle, thin-wall, and load-bearing packaging articles. The grade is characterised by a nominal melt mass-flow rate of 8.0 g/10 min measured under 190 °C/2.16 kg according to ISO 1133-1:2022 or ASTM D1238-20, and a nominal density of 0.956 g/cm³ according to ISO 1183-1:2019 or ASTM D1505-18. These two values place DMDA-8008 in the high-flow HDPE injection segment, where cavity filling and cycle time depend more on rheology than on the melt strength required in blow moulding or blown film. The product is supplied as natural pellets with an internal additive package intended for general-purpose injection moulding; it is not positioned as a pipe, extrusion blow moulding, rotational moulding, or outdoor weatherable grade.
In melt-index terms, 8.0 g/10 min is sufficiently high to reduce injection peak pressure and permit filling of long flow-length sections at lower hydraulic demands than a 3–4 g/10 min general-purpose injection HDPE. The same parameter lowers intrinsic melt strength compared with extrusion-blow-moulding HDPE grades whose melt mass-flow rate is typically <1.0 g/10 min. The molecular weight distribution of DMDA-8008 is controlled during polymerisation to favour shear thinning without excessive die swell. During screw plastication, apparent viscosity decreases as screw speed rises; a melt-temperature window from 190 °C to 230 °C is generally applied to balance flow-length ratio against thermal-oxidative degradation. Because density is held at 0.956 g/cm³, the crystalline fraction is high enough to provide stackability and top-load retention in crates and pails, but the material still depends on wall thickness and radius design to avoid brittle crack propagation at sub-ambient temperatures.
A representative property profile for PetroChina Dushanzi HDPE DMDA-8008 is summarised in Table 1. The values are drawn from typical published datasheet ranges and should be verified against the lot-specific certificate of analysis; they do not constitute a minimum or maximum specification. Lot-to-lot MFR variation of ±0.5 g/10 min is industrially meaningful in multi-cavity tools and should trigger revalidation of fill balance when switching production batches.
| Property | Test Method | Typical Value |
|---|---|---|
| Melt mass-flow rate, 190 °C/2.16 kg | ISO 1133-1:2022 / ASTM D1238-20 | 8.0 g/10 min |
| Density | ISO 1183-1:2019 / ASTM D1505-18 | 0.956 g/cm³ |
| Tensile stress at yield | ISO 527-2:2012 / ASTM D638-14 | 23–26 MPa |
| Nominal strain at break | ISO 527-2:2012 / ASTM D638-14 | >300 % |
| Flexural modulus | ISO 178:2019 / ASTM D790-17 | 950–1150 MPa |
| Notched Izod impact, 23 °C | ISO 180/A:2023 / ASTM D256-23 | 4.0–6.0 kJ/m² |
| Vicat softening point, A50 | ISO 306:2022 / ASTM D1525-17e2 | 122–126 °C |
| Heat deflection temperature, 0.45 MPa | ISO 75-2/B:2020 / ASTM D648-18 | 68–75 °C |
| Hardness, Shore D | ISO 868:2003 / ASTM D2240-15 | 60–64 |
In high-speed injection moulding, the practical advantage of a high-MFR HDPE such as DMDA-8008 is shorter packing time and lower residual stress, provided the gate geometry and hold-pressure profile are correct. Barrel profiles are typically flat or reverse from feed zone 190 °C to nozzle 215–225 °C; mould temperature is maintained between 10 °C and 40 °C with turbulent chilled water at a linear velocity of 2–4 m/s through cooling channels. On machines with clamp force between 350 t and 800 t, injection pressure commonly ranges from 70 MPa to 120 MPa hydraulic pressure, depending on gate diameter and hot-runner pressure drop. General-purpose polyolefin screws with L/D ratios of 20:1 to 24:1 and compression ratios of 2.5:1 to 3.5:1 are used; screw speed is normally set between 60 min⁻¹ and 120 min⁻¹ on a 50 mm screw, with back pressure below 10 MPa to avoid excessive shear heating.
Gate freeze is managed by maintaining hold pressure until the part reaches approximately 95 % of its mass plateau, after which additional packing provides little dimensional benefit and can increase warpage in flat lids and crate side panels. Sink marks and warpage in pail bases are reduced by placing gates at the nominal wall centre and by keeping flow-path length-to-wall-thickness ratio below 150:1; for a 1.5 mm wall, this equates to a maximum flow length of 225 mm from gate to last fill. In multi-cavity tooling with 16–32 cavities, the runner system must be naturally balanced; a cavity wall-temperature variation of ±1 °C can produce measurable mass deviation and ovality in round lids. When a line stops for more than 10–15 min at melt temperatures above 240 °C, residual residence time can produce viscosity drift; the preferred shutdown practice is to purge with a lower-MFR HDPE or reduce barrel temperature to 150 °C.
End-use selections for DMDA-8008 centre on injection-moulded packaging and industrial containers where the 8.0 g/10 min MFR keeps cycle times below those of 3–4 g/10 min general-purpose HDPE grades. The grade is used for beverage crates, pails up to 25 L, thin-wall food trays, caps and closures, and collapsible industrial containers. In these applications, top-load retention and environmental stress-crack resistance under detergent or dilute acid contact are common fitness-for-service requirements. Part design for pails should avoid sharp corner radii below 1.5 mm and abrupt wall-thickness transitions exceeding 1:1.4 to avoid notched impact concentration and stress cracking at the gate region. Mould shrinkage in the flow direction is approximately 1.5–2.0 %, with transverse shrinkage in the range of 1.2–1.8 %, depending on gate geometry, packing pressure, and part thickness; these values are for process design and must be confirmed on the production tool.
Because DMDA-8008 is an olefinic thermoplastic, it absorbs negligible moisture during storage; pre-drying is not normally required when the resin is stored in an unopened container at <35 °C and RH <60 %. If silo or hopper condensation occurs, a low-temperature dry-air purge at 60–70 °C for 1–2 h can be applied, but drying above 80 °C risks pellet agglomeration and bridging in the feed throat. The material should not be stored in direct sunlight for prolonged periods because UV stabilization is not present at levels sufficient for outdoor service unless a separate UV package is compounded. The grade is not recommended for extrusion blow moulding, blown film, or rotational moulding because the low melt strength of an 8.0 g/10 min MFR resin leads to parison drawdown, bubble instability, or pinhole formation.
Processors using DMDA-8008 in food-contact packaging should evaluate the finished article under US FDA 21 CFR 177.1520 for olefin polymers, EU Regulation (EU) No 10/2011 and its amendments for plastic materials and articles intended to come into contact with food, and GB 4806.6-2016 in the Chinese regulatory context. Compliance is determined by the finished article, which means migration testing and organoleptic evaluation are the converter’s responsibility. The grade is not intentionally formulated with substances of very high concern above 0.1 wt% under the REACH candidate list, but converters must confirm their own supply-chain documentation for the specific lot. Combining DMDA-8008 with halogenated flame retardants or amine-based additives should be avoided without pre-testing because the stabiliser package may be antagonised, reducing long-term thermal-oxidative stability and shifting melt-flow stability during extrusion.
The practical separation between DMDA-8008 and other HDPE product families rests on its balance of melt flow and density. Extrusion blow moulding grades with MFR less than 1.0 g/10 min have higher melt strength but longer cooling-dominated cycle times and are unsuitable for thin-wall injection. Lower-flow injection grades near 3–4 g/10 min often provide higher notched impact but may require higher injection pressure and exhibit more gate blush in thin-wall tools. High-flow injection HDPE grades above 12 g/10 min permit faster filling but generally sacrifice ESCR and top-load stiffness unless density is raised. Table 2 summarises the differentiation against the most common processing families.
| Parameter | DMDA-8008 Injection HDPE | Extrusion Blow Moulding HDPE | General-Purpose Injection HDPE | High-Flow Injection HDPE |
|---|---|---|---|---|
| Nominal MFR, 190 °C/2.16 kg | 8.0 g/10 min | 0.3–0.8 g/10 min | 3.0–4.0 g/10 min | 12–20 g/10 min |
| Nominal density | 0.956 g/cm³ | 0.950–0.954 g/cm³ | 0.954–0.958 g/cm³ | 0.953–0.960 g/cm³ |
| Typical melt temperature | 190–230 °C | 190–210 °C | 200–240 °C | 180–220 °C |
| Primary process | Injection moulding | Extrusion blow moulding | Injection moulding | Injection moulding |
| Limiting processing property | Melt strength, ESCR | Melt strength, swell control | Impact, injection pressure | ESCR, warpage |