| HS Code | 924290 |
| Density G Cm3 | 0.960 |
| Melt Flow Rate G 10min 190c 2 16kg | 9.5 |
| Tensile Yield Strength Mpa | 30 |
| Elongation At Break Percent | 500 |
| Flexural Modulus Mpa | 1300 |
| Notched Izod Impact Strength Kj M2 | 5 |
| Vicat Softening Temperature C | 125 |
| Melting Point C | 135 |
| Shore D Hardness | 70 |
| Environmental Stress Cracking Resistance H | 30 |
| Water Absorption Percent | <0.01 |
| Dielectric Constant 1mhz | 2.3 |
| Volume Resistivity Ohm Cm | >10^16 |
| Thermal Conductivity W Mk | 0.4 |
| Coefficient Of Linear Thermal Expansion Per C | 1.2×10^-4 |
| Mold Shrinkage Percent | 1.5-3.0 |
| Brittleness Temperature C | -70 |
| Crystallinity Percent | 80-90 |
As an accredited PetroChina Guangdong HDPE DGDZ-6095 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | PetroChina Guangdong HDPE DGDZ-6095 is typically packed in 25 kg woven bags, 40 bags per 1,000 kg pallet. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): PetroChina Guangdong HDPE DGDZ-6095, 25 kg bags, palletized, stretch-wrapped, and securely strapped for export shipment. |
| Shipping | PetroChina Guangdong HDPE DGDZ-6095 is shipped as non-hazardous high-density polyethylene pellets, typically in 25 kg bags or 1-ton jumbo bags, palletized and shrink-wrapped. Transport by truck or container at ambient temperature. Keep dry, away from direct sunlight. Not classified as dangerous goods for transport. Store in a cool, ventilated area. |
| Storage | Store PetroChina Guangdong HDPE DGDZ-6095 in a cool, dry, well-ventilated warehouse, away from direct sunlight, moisture, heat, flames, and strong oxidizers. Keep original bags sealed, palletized, and off the floor. Avoid package damage and excessive stacking. Use first-in, first-out rotation. Maintain clean, dust-free conditions, separate from food/feed, and follow local regulations. |
| Shelf Life | Typically, shelf life is 24 months when stored sealed in original packaging, cool, dry, ventilated, away from sunlight. |
In high-speed retail vest bag conversion, the molecular weight and die swell characteristics of DGDZ-6095 determine whether a continuous 6–10 µm per ply film can survive downstream slitting and perforation without blocking or tearing at the wicket insertion point. The resin is processed as the primary structural component at 96–98 wt%, with an LLDPE-rich trim recycle stream added at 2–4 wt% only where perforation tear demands exceed the values obtainable from the neat resin. Slip and antiblock masterbatch addition is limited to 0.5–1.5 wt% because overdosing shifts the coefficient of friction above the range required for automatic wicket insertion on continuous bag machines. The relevant conversion path is high-stalk tubular extrusion using a grooved-feed single-screw extruder with 28:1–32:1 L/D, die diameter 150–250 mm, die gap 0.8–1.2 mm, blow-up ratio 2.5:1–3.5:1, and frost line height maintained at 5–8 die diameters. Melt temperature at the adapter is held between 190 °C and 205 °C; excursions above 210 °C lower bubble stability and raise gel counts in continuous high-speed runs. Compliance for retail bags that may contact dry food is assessed under FDA 21 CFR 177.1520(c) and, for EU-bound distribution, Regulation (EU) No 1935/2004, with the finished film evaluated under Regulation (EU) No 10/2011 overall migration limits. Mechanical release limits are established by ASTM D1238-20, ASTM D882-18, ASTM D1709-21, and ASTM D1922-15. Finished product forms include T-shirt carrier bags, produce roll film, and bakery bag stock.
Three-layer blown film structures for cereal liners place DGDZ-6095 in the central layer at 60–75 wt% of total film mass. The outer skin layers, typically LDPE or EVA-modified LLDPE at 15–25 wt%, provide heat-seal response and low-temperature seal initiation, while the core contributes bending stiffness and water-vapour resistance. Tie layers or compatibilised reclaim may occupy 5–10 wt% in structures where edge scrap is returned to the extrusion hopper. On a three-layer die with 1.0–1.4 mm land gap, the layer distribution is set at 15/70/15 or 20/60/20, depending on the target seal strength and hot-tack window. Extrusion is carried out on a three-layer blown film line with a 200–300 mm die, internal bubble cooling, and melt temperatures of 195–210 °C. The frost line is controlled by chilled air at 10–20 °C; excessive cooling below 10 °C can induce gauge bands across the layflat and destabilise the bubble. Food-contact compliance follows GB 4806.7-2016 for the Chinese domestic market, EU 10/2011 for migration, and FDA 21 CFR 177.1520(c) for any US-bound laminate. Optical and mechanical specifications are determined with ASTM D1003-21 for haze, ISO 14782 for film haze, ISO 527-3:2018 for tensile modulus, and ISO 7765-1:2013 for dart impact. Terminal formats consist of cereal bag liners, dry snack pouches, and cracker sleeves.
DGDZ-6095 at 25–60 µm gauge replaces LLDPE-rich refuse sack formulations where high modulus and low creep are required for municipal collection and heavy industrial handling. The formulation is typically 88–94 wt% virgin DGDZ-6095, 3–6 wt% LDPE or LLDPE from edge trim, and 2–4 wt% carbon black masterbatch when UV ageing in outdoor staging is specified. Processing aids are kept at 0.03–0.06 wt% only if the extruder head pressure exceeds the safety limit of the screen changer. The production route uses an air-cooled blown film tower with internal bubble cooling, extruder diameter 75–100 mm, L/D 30:1–33:1, die gap 1.2–1.6 mm, and blow-up ratio 3.0:1–4.0:1. Melt temperature is maintained between 200 °C and 220 °C. A reduction in die gap below 1.0 mm while raising output above 250 kg/h triggers melt fracture at the die lip; fluoropolymer process aid addition becomes mandatory at that boundary. The property envelope is verified with ISO 7765-1:2013, ASTM D1709-21, ASTM D882-18, and tear propagation according to ISO 6383-2. Carbon black dispersion and colour fastness are assessed with ISO 11468 or a manufacturer-specific visual standard. The finished stock is converted into municipal refuse sacks, construction cleanup bags, and industrial drum liners.
In five-layer flexible packaging lines where DGDZ-6095 is used as a stiffening layer within a 30–50 µm total structure, the HDPE layer is commonly specified at 20–35 wt% of the total mass. Below 20 wt%, the bending stiffness contribution becomes statistically indistinguishable from LLDPE-rich alternatives in ISO 527-3 modulus testing; above 35 wt%, the dart impact strength under ASTM D1709-21 Method A can decline to 80–120 g depending on gauge, leading to premature failure at non-seal flex points. The layer distribution is established on a five-layer blown film die with 1.3–1.8 mm die gap and typical A/B/C/B/D arrangements where the DGDZ-6095-containing B or C layer is 8–16 µm. Melt temperature is held at 200–215 °C, with a frost line height not exceeding 7 die diameters to prevent excessive orientation. Published data for this specific configuration is limited, so pilot runs should bracket the HDPE layer at 15 wt%, 25 wt%, and 35 wt% while measuring ASTM D1922-15 tear, ISO 7765-1:2013 impact, and ASTM D1003-21 haze. Food-contact structures must be confirmed under EU 10/2011 and FDA 21 CFR 177.1520; non-food packaging follows REACH and RoHS substance restrictions. The end product forms are form-fill-seal pillow pouches, stand-up pouch stiffening webs, and high-stiffness overwrap films.
The desired paper-like bending stiffness and reduced surface gloss of tissue and diaper overwrap film are produced by adding 5–15 wt% of a calcium carbonate or talc masterbatch to DGDZ-6095, which increases modulus while limiting total gauge to 18–35 µm. In this application, the resin is processed as the continuous phase at 85–95 wt%, with filler masterbatch compounding performed at the blown film hopper or via a gravimetric feeder. The downstream process is monolayer or three-layer blown film extrusion with a 200–350 mm die, die gap 0.9–1.3 mm, blow-up ratio 2.5:1–3.5:1, and melt temperature 190–205 °C. Die lip deposition from filler decomposition imposes a maintenance interval of 8–16 h for continuous runs; a 200–300 mesh screen pack is specified to control agglomerates. The material is oriented only lightly, because excessive frost line height above 6 die diameters promotes unbalanced MD tear in ASTM D1922-15. Regulatory review for hygiene packaging focuses on ISO 11607-1:2019 for terminally sterilised medical device packaging when the film is converted into sterile barrier overwrap, while general consumer packaging is evaluated under REACH Annex XVII and, for any dermal contact, Commission Regulation (EU) No 10/2011 if the film is positioned as a secondary food-contact wrapper. Optical and friction characteristics are measured with ASTM D2457-21 for gloss and ISO 8295 for coefficient of friction. The terminal product categories include diaper pack overwrap, tissue bundle film, and feminine care product wrapping.
When DGDZ-6095 is run on high-stalk towers at output rates exceeding 0.6 kg/h/mm of die circumference, the onset of shark skin on the bubble exterior becomes the limiting factor rather than bubble stability. In such a regime, the formulation is adjusted with a fluoropolymer-based polymer processing aid at 300–600 ppm by weight, while the resin remains at 98–99 wt% and the remaining fraction is a slip/antiblock masterbatch at 1–2 wt%. The extruder configuration includes a barrier screw with a 30:1–33:1 L/D, spiral mandrel die with 1.0–1.2 mm die gap, and die diameter between 250 mm and 400 mm. Melt pressure ahead of the screen changer is monitored continuously; sustained pressure above 350 bar requires either reducing screw speed by 5–8% or raising the adapter temperature by 2–3 °C, the latter only if the resin temperature measured by IR pyrometer does not exceed 210 °C. The compliance framework is process-focused: ISO 1133-1:2022 for MFR, ASTM D1238-20 for independent verification, and ASTM D1505-18 for density. Surface quality is graded against ISO 2813 gloss measurements and a 5× magnified visual reference for melt fracture. The film produced under these conditions is used as rigid overwrap, transparent bag stock, and packaging film where gel count and surface uniformity determine printability.
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PetroChina Guangdong HDPE DGDZ-6095 is a high-density polyethylene extrusion blow moulding grade manufactured at the Guangdong petrochemical complex. The grade designation follows PetroChina’s HDPE suffix convention, in which the digits 60 denote the density class and the digits 95 denote the high-load melt flow index class. The resin is therefore positioned in the 0.958–0.963 g/cm³ density envelope and the 0.85–1.05 g/10 min melt flow rate envelope measured at 190 °C under a 5.0 kg load. Because the specific PetroChina Guangdong technical data sheet is not widely published in English, the values in Table 1 are a representative property envelope for the 0.960/0.95 HDPE blow moulding class and are not intended as a replacement for the lot certificate of analysis.
| Property | Test method | Unit | Representative envelope |
|---|---|---|---|
| Density | ISO 1183-1 | g/cm³ | 0.958–0.963 |
| Melt flow rate, 190 °C/5.0 kg | ISO 1133-1 | g/10 min | 0.85–1.05 |
| Tensile stress at yield | ISO 527-2 | MPa | 26–31 |
| Elongation at break | ISO 527-2 | % | >400 |
| Flexural modulus | ISO 178 | MPa | 1,000–1,400 |
| Charpy notched impact strength, 23 °C | ISO 179-1 | kJ/m² | 15–30 |
| Vicat softening temperature, A50 | ISO 306 | °C | 120–127 |
| Shore D hardness | ISO 868 | — | 63–68 |
| Environmental stress-cracking resistance, F50, 10% Igepal CO-630 | ASTM D1693 | h | 30–150 |
Molecular architecture in the DGDZ-6095 class is balanced for parison melt strength rather than for blown-film bubble stability or pressure-pipe hydrostatic durability. The density is controlled by short-chain branching from an olefin comonomer, but the comonomer type and concentration are not consistently disclosed in publicly available documentation for the Guangdong plant configuration. A broader molecular weight distribution is expected within the grade class because extrusion blow moulding resins require a combination of die swell, shear thinning, and resistance to parison sag. The high-load/standard-load melt flow ratio is used in compounding and conversion plants to assess molecular weight distribution; for blow moulding HDPE near 0.960 g/cm³ density and 0.95 g/10 min high-load melt flow rate, high-load/standard-load ratios above 20 are common. The exact ratio for DGDZ-6095 should be obtained from the certificate of analysis or measured by capillary rheometry.
Rheologically, the material is not Newtonian. Shear thinning is significant at the die lip, and the shear viscosity in the die range of 100–1,000 s⁻¹ determines head pressure and output. At lower shear rates, the elongational viscosity controls parison sag and blow-up ratio stability. A capillary rheometer operated in accordance with ISO 11443 is recommended for incoming lot verification. A drift in high-load melt flow rate greater than ±0.10 g/10 min can change parison weight, die swell, and wall-thickness distribution in accumulator-head tooling. Batch-to-batch variation in density greater than ±0.002 g/cm³ can also shift top-load stiffness and container volume because crystallinity and shrinkage are density dependent.
In shuttle and accumulator blow moulding lines with screw L/D ratios from 24:1 to 30:1, DGDZ-6095 is processed with a barrel-temperature profile from 170 °C in the feed zone to 200 °C in the metering zone. Die-head temperature is normally held between 190 °C and 210 °C. Melt temperature measured at the die exit should remain below 220 °C to limit thermal oxidative degradation. At the lower boundary, melt temperatures below 175 °C can produce melt fracture, poor pinched-off weld strength, and high parison swell variability. At the upper boundary, sustained melt temperatures above 230 °C accelerate chain scission, reduce die swell, and increase odour, colour formation, and environmental stress-cracking sensitivity.
The die gap is typically set between 1.5 mm and 3.0 mm depending on container volume and target wall thickness. Blow pressure is commonly maintained between 0.6 MPa and 1.0 MPa. Mould temperature is controlled between 10 °C and 30 °C to balance cooling shrinkage against surface quality. On accumulated-head machines, low head pressure or a worn spiral mandrel can cause wall-thickness drift during continuous cycles. For containers above 5 L, parison programming with 10 to 30 points is applied to compensate for parison sag and variable stretching. A converging die with a land length-to-gap ratio of 10:1 to 15:1 is used in practice to stabilise die swell and reduce melt fracture.
Moisture is not the primary drying-limited variable for high-density polyethylene; nevertheless, surface condensation on pellets stored in ambient relative humidity above 60% can produce steam splay and parison pinholes. A pre-dry step at 80 °C for 2 h to 4 h is applied when cold silo pellets are moved into a humid processing hall. Regrind addition up to 20% is common on container lines, but higher fractions require retention testing of environmental stress-cracking resistance according to ASTM D1693 and notched impact strength according to ISO 179-1. Repeated heat history narrows the molecular weight distribution, raises crystalline orientation, and can reduce ESCR before the melt index changes enough to be detected by routine melt flow testing.
Application fit for DGDZ-6095 is governed by density, high-load melt index, and environmental stress-cracking resistance. Containers with capacities from 0.5 L to 20 L are produced on shuttle blow moulders for industrial chemical packaging, lubricant bottles, and household chemical containers. Wall thickness is generally specified from 0.6 mm to 3.0 mm. The density near 0.960 g/cm³ contributes to top-load strength and dimensional stability; the high-load melt index permits practical head pressure and output on single-screw extruders. Chemical compatibility is screened for the intended fill using ASTM D543. For food-contact use, a resin compliance statement is required; generic olefin polymer coverage under FDA 21 CFR 177.1520 and EU Regulation 10/2011 does not replace migration testing on the finished container.
The substitution of a film-grade or pipe-grade HDPE with DGDZ-6095 is not compositionally neutral. Film-grade HDPE is typically engineered with a lower melt index and higher molecular weight for bubble stability in stalk-bubble or pocket-bubble blown film lines. If DGDZ-6095 is substituted into film extrusion, the higher 0.95 g/10 min high-load melt index class broadens the bubble operating window but can lower tear propagation resistance measured by ASTM D1922 and dart impact measured by ASTM D1709. Conversely, when a film-grade resin is substituted on an extrusion blow moulding line, excessive parison sag and poor wall-thickness control are observed because the film resin typically has lower die swell and higher extensional viscosity at hang-time conditions.
Compared with PE100 pipe grades classified under ISO 9080 and ISO 12162, DGDZ-6095 does not possess the bimodal comonomer distribution and long-term hydrostatic strength required for 10 MPa minimum required strength applications. Pipe-grade substitution in blow moulding often produces high melt pressure, lower output, and unacceptable parison surface texture. Injection-moulding HDPE grades, with standard melt flow rates from 5 g/10 min to 20 g/10 min, are also not interchangeable because they sacrifice melt strength and make long parison hang times unattainable. Conversely, DGDZ-6095 is not optimized for fast-cycle injection moulding because its lower melt index increases fill pressure and packing requirements in thin-wall tools.
Ultraviolet exposure, melt residence time, and additive interactions define the operational boundary. The resin is stored in closed silos or hoppers to prevent moisture and contaminant pickup. Melt residence time at 220 °C should not exceed 15 min; start-up and shutdown purges with a lower-viscosity polyolefin are recommended to prevent deposit accumulation in the die and accumulator head. Halogenated flame retardants and certain peroxide additives can induce premature chain extension or degradation and are not recommended without a stabiliser compatibility study. Outdoor storage of finished containers requires carbon black or UV stabilisation; xenon-arc exposure per ASTM D2565 is used to verify retention of tensile elongation after 1,000 h for non-black grades. Published data for the specific Guangdong DGDZ-6095 configuration remains limited; therefore incoming lot testing and certificate-of-analysis verification are required before locking process parameters.