| HS Code | 112993 |
| Productname | PetroChina Daqing HDPE DGDB-6097 / 6097 |
| Manufacturer | PetroChina Daqing Petrochemical Company |
| Polymertype | High Density Polyethylene (HDPE) |
| Grade | DGDB-6097 / 6097 |
| Peclassification | PE100 |
| Form | Pellets |
| Appearance | White pellets |
| Chemicalformula | (C2H4)n |
| Casnumber | 9002-88-4 |
| Density | 0.949 g/cm³ |
| Meltflowrate | ≈0.25 g/10 min |
| Meltflowratecondition | 190°C/5.0 kg |
| Tensileyieldstrength | ≥25 MPa |
| Elongationatbreak | ≥600% |
| Flexuralmodulus | ≥1000 MPa |
| Vicatsofteningtemperature | ≥125°C |
| Brittlenesstemperature | ≤-70°C |
| Meltingtemperature | ≈130°C |
| Oxidationinductiontime | ≥20 min |
| Environmentalstresscrackresistance | ≥1000 h |
| Application | PE100 pressure pipes, water supply pipes, gas pipes, industrial pipes |
As an accredited PetroChina Daqing HDPE DGDB-6097 / 6097 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | PetroChina Daqing HDPE DGDB-6097/6097: typically packed in 25 kg bags or 1,000 kg jumbo bags; 25 MT per 20-foot container. |
| Container Loading (20′ FCL) | Standard 20′ FCL loading for PetroChina Daqing HDPE DGDB-6097/6097: 25kg bags, palletized, shrink-wrapped; approximately 17–18 MT net per container. |
| Shipping | PetroChina Daqing HDPE DGDB-6097/6097 is a non-hazardous thermoplastic resin, typically shipped as pellets in 25 kg bags or 500–1000 kg jumbo bags, palletized and stretch-wrapped. Transport in dry containers via ocean freight from China; keep cool, dry, away from moisture, sunlight, and ignition sources. |
| Storage | Store PetroChina Daqing HDPE DGDB-6097 / 6097 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, sparks, and flames. Keep original packaging sealed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and excessive stacking pressure. Maintain moderate temperatures. Use first-in, first-out rotation, handle bags carefully, and follow the manufacturer’s SDS and local regulations. |
| Shelf Life | Store in a cool, dry, ventilated area away from sunlight; shelf life is typically 36 months in unopened original packaging. |
For black PE100 potable water pipe, metering of DGDB-6097 at the throat of a 36D grooved-feed single-screw extruder is sequenced with a carbon black masterbatch let-down that yields 2.0–2.5 wt% carbon in the final compound; ISO 4427-2:2019 and GB/T 13663.2-2018 require black pressure pipe compound to remain inside this gravimetric band because lower loadings degrade ultraviolet resistance and higher loadings can reduce slow crack growth margins in solid-wall pressure pipe. Inline compounding is plant-specific: weight-loss feeders at the main feed port are preferred over volumetric screw feeders because carbon black masterbatch particle size, melt index mismatch, and hopper bridging can produce visible black specks and reduce notched pipe test performance. A hopper dryer at 70–80 °C is used only when storage relative humidity exceeds 60 %, since surface moisture on the pellets is carried into the melt and appears as fine splay on the inner wall. The extruder barrel zones are normally set between 180 °C and 220 °C, with the die head held at 210–230 °C; melt temperatures above 230 °C are undesirable because oxidative pre-gel can form as micro-pits in the pipe wall and reduce long-term hydrostatic strength. Vacuum calibration is applied at −0.6 to −0.8 bar, cooling water is controlled from 15 °C to 25 °C, and diameter is monitored by laser scanning because ovality in pressure pipe changes the effective wall thickness and SDR classification. Finished product is solid-wall PE100 pipe in DN 32 to DN 630 mm, typically SDR 11, SDR 13.6, SDR 17, and SDR 21, for municipal potable water distribution and service laterals. Hydrostatic tests are evaluated by ISO 1167-1, long-term strength is extrapolated by ISO 9080, rapid crack propagation is screened by ISO 13477, and design stress is classified under ISO 12162.
In gas distribution pipe production, the limiting property is slow crack growth resistance, not short-term burst strength; DGDB-6097 is compounded with 2.0–2.5 wt% carbon black and the antioxidant package is held below 0.3 wt% to avoid depletion effects during repeated extrusion and outdoor storage. Standards ISO 4437-2 and EN 1555-2 govern PE100 gas pipe dimensions and material classification; resistance to slow crack growth is verified by ISO 13479 notched pipe test at 80 °C, and rapid crack propagation is screened by ISO 13477 S4 test at 0 °C. The production line for black gas mains with co-extruded yellow identification stripe uses a primary 36D extruder and a satellite 45 mm extruder for the stripe layer; stripe masterbatch is metered at 5–7 wt% into the satellite melt stream to maintain colour saturation without contaminating the core compound. Melt temperature is maintained at 200–230 °C, and the die head pressure is deliberately kept stable to prevent stripe-core interface instability. Finished products include PE100 gas distribution mains and service lines in DN 20 to DN 400 mm, commonly SDR 11 and SDR 17.6, for buried natural gas and manufactured gas service. Butt-fusion joint qualification follows ISO 21307, and peel testing of fusion beads is performed to detect cold welds.
| Test method | Property assessed | Typical condition |
| ISO 1167-1 | Hydrostatic strength | 20 °C, 80 °C |
| ISO 13479 | Slow crack growth | 80 °C |
| ISO 13477 | Rapid crack propagation | 0 °C |
For twin-wall corrugated HDPE drainage pipe, the production target shifts from hydrostatic rating to ring stiffness and impact tolerance in thin corrugated webs. The DGDB-6097 stream is combined with 2.0–2.5 wt% carbon black masterbatch; where melt fracture appears on the inside wall at high line speed, a fluoropolymer processing aid is added at 0.2–0.4 wt% to reduce die lip buildup and permit stable draw-down into the corrugator. Compliance is evaluated under ISO 21138-1:2020, EN 13476-3:2018, and ASTM F667/F667M-19; ring stiffness is confirmed by parallel-plate crush at 3 % deflection and is a function of profile height, wall thickness, and corrugation spacing rather than material alone. Production uses a 30–36D single-screw extruder feeding a vacuum corrugator with water-cooled aluminium mould blocks; melt temperature is held at 195–220 °C, lower than pressure pipe to maintain the corrugated profile without sagging. Vacuum is applied to the mould blocks to draw the outer wall, while an inner die forms the smooth inside surface; differential vacuum between the two sides of the mould can cause axial thickness variation that is observable as alternating stiff and soft bands. Finished product types include subsurface agricultural drainage coil, stormwater culvert, landfill gas collection lateral, and twin-wall conduit.
Flat die extrusion of HDPE geomembrane from DGDB-6097 imposes thickness uniformity and non-destructive test-frequency obligations that are absent in pipe processing. The compound is let down to 2.0–3.0 wt% carbon black, with an antioxidant package in the 0.2–0.5 wt% range to withstand long-term oxidative ageing in exposed liner applications; GRI-GM13 sets the testing sequence, including carbon black dispersion, thickness by ASTM D5199, tensile properties by ASTM D6693, and density by ASTM D1505. Production equipment includes a 33D barrier-screw extruder, a flat die, and a three-roll calendering stack with either smooth or textured rolls; sheet thickness ranges from 1.0 mm to 3.0 mm, and width can exceed 9 m on high-output lines. Roll gap pressure is held constant to avoid gauge bands, and laser thickness scanning is used across the sheet width; thickness covariance is a direct measure of melt distribution across the manifold. Finished product includes landfill bottom liner, cap liner, mining heap leach pad, and wastewater lagoon geomembrane. Published data for DGDB-6097 on very high-output geomembrane lines is limited; processing stability must be confirmed by melt pressure and thickness covariance rather than by pipe-grade flow data alone.
Buried HDPE cable duct manufactured from DGDB-6097 is specified by low-temperature impact and ring stiffness rather than hydrostatic design stress. The compound is set to 2.0–2.5 wt% carbon black; internal lubricant layers are co-extruded where pull-in distance exceeds 500 m, using a separate satellite extruder and a low-friction HDPE slip layer. Compliance references IEC 61386-24, UL 651, and ASTM D3485; impact tests at −5 °C are used to ensure that duct walls do not crack during winter installation. Extrusion is run on a 24–33D single-screw extruder with vacuum calibration and online bell forming; melt temperature is held between 200 °C and 220 °C, and the line runs slower than pressure pipe to maintain roundness of the bell socket. The bell socket is formed immediately after calibration, and its inner diameter is checked with go/no-go gauges because out-of-round sockets create cable hang-up points during installation. Finished product types include power cable duct, telecom raceway, and fibre optic protection conduit in DN 40 to DN 250 mm diameters.
Thick-wall HDPE pipe for mineral slurry transport moves away from high-speed vacuum sizing toward slow cooling and internal air pressure to manage shrinkage and ovality. The DGDB-6097 feed is combined with 2.0–2.5 wt% carbon black and no inorganic filler; the base polymer toughness is retained for abrasive service, while the carbon black provides ultraviolet protection for outdoor installations. No single ISO product standard fully defines abrasive slurry service; material classification follows ISO 4427-1, long-term strength is extrapolated by ISO 9080, and butt fusion welding is qualified by ISO 21307. Production equipment includes a 36D grooved-feed extruder, internal air cooling, and vacuum sizing; melt temperature is held at 210–230 °C, and wall thickness above 10 mm demands longer cooling baths and lower line speeds than thin-wall pipe. Residual thermal shrinkage is controlled by internal air pressure during cooling; excessive shrinkage can lead to axial stresses that produce cracking at fusion joints after installation. Finished product includes mine tailings line, dredge discharge hose replacement pipe, and abrasive slurry transfer line. Published data for DGDB-6097 in highly abrasive thick-wall configurations is limited; the long-term hydrostatic extrapolation remains based on ISO 9080 rather than abrasion-specific data.
Sewage force mains fabricated from this HDPE grade are solid-wall pipe intended for intermittent pressure pulsation and suspended solids, not continuous potable water service. The black compound is set to 2.0–2.5 wt% carbon black; material classification and dimensions follow ISO 4427-2 and EN 12201-2, while North American practice may reference ASTM F714. Processing is similar to potable water pipe extrusion: a 36D grooved-feed extruder with barrel zones from 180 °C to 220 °C, die head at 210–230 °C, vacuum calibration, and water cooling. The key production control is wall thickness consistency in SDR 11 and SDR 17 pressure classes, because pulsation fatigue and surge pressure are more demanding than static head conditions. Butt fusion joints are made and qualified under ISO 21307, with tensile testing of specimen welds. Finished product types include wastewater force main, pumping station discharge line, and sludge transfer pipe in DN 32 to DN 630 mm diameters.
Irrigation mainlines fabricated from DGDB-6097 are typically black PE100 pressure pipe with a design envelope that includes above-ground ultraviolet exposure and cyclic pump operation. The compound is set to 2.0–2.5 wt% carbon black to suppress photodegradation, and the extrusion line uses a 30–36D single-screw extruder with laser diameter scanning and inline marking; melt temperature is kept at 200–230 °C. Compliance for agricultural irrigation pipe is evaluated under ISO 8779, with material classification under ISO 12162 and long-term strength under ISO 9080. Small-diameter pipe is coiled immediately after cooling, while larger diameters are cut into straight lengths; coil memory in small diameters must be controlled by uniform cooling because residual curvature can cause installation difficulties in drip mainline. Finished product types include drip irrigation mainline, sprinkler manifold, and agricultural water distribution pipe in DN 16 to DN 315 mm diameters. Published data for this specific grade in above-ground ultraviolet service beyond ten years is limited; carbon black dispersion must be confirmed by ISO 18553 and the dispersion rating should not exceed the specified maximum.
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PetroChina Daqing HDPE DGDB-6097, also listed as grade 6097 in procurement records, is a bimodal high-density polyethylene pipe extrusion compound produced at the Daqing Petrochemical complex. The material is classified as PE100 under ISO 12162-1 on the basis of a minimum required strength of 10.0 MPa at 20 °C and 50 years when evaluated by the long-term hydrostatic strength methodology of ISO 9080. The bimodal molecular weight distribution separates the high-molecular-weight fraction, which controls slow crack growth resistance and long-term creep rupture strength, from the low-molecular-weight fraction, which provides shear thinning during extrusion. The grade is supplied as a black compound with carbon black content in the 2.0–2.5 wt% range and is intended for solid-wall pressure pipe used in potable water, natural gas distribution, and industrial fluid transport.
Manufacturer-published typical values for DGDB-6097 are summarised below. These values are determined on compression-moulded plaques or extruded pipe according to the listed procedures; lot-release specification limits may be narrower or wider depending on the production campaign. The density of the black compound is typically 0.959 g/cm³ when measured by ISO 1183-1. The melt mass-flow rate under 190 °C and 5 kg is 0.22–0.25 g/10 min by ISO 1133-1. The high-load melt index under 21.6 kg is not commonly used as a primary release parameter for this grade but may fall in the 7–10 g/10 min range. Tensile yield stress according to ISO 527-2 is 23 MPa, elongation at break exceeds 600 %, and flexural modulus is approximately 900 MPa by ISO 178. The notched Charpy impact strength at 23 °C is typically above 25 kJ/m²; at -30 °C it remains above 10 kJ/m². The oxidation induction time at 200 °C by ISO 11357-6 is greater than 20 min.
| Property | Method | Typical value or range |
|---|---|---|
| Melt mass-flow rate, 190 °C, 5.0 kg | ISO 1133-1 | 0.22–0.25 g/10 min |
| Density | ISO 1183-1 | 0.959 g/cm³ |
| Tensile yield stress | ISO 527-2 | 23 MPa |
| Elongation at break | ISO 527-2 | >600 % |
| Flexural modulus | ISO 178 | 900 MPa |
| Notched Charpy impact strength, 23 °C | ISO 179-1/1eA | >25 kJ/m² |
| Oxidation induction time, 200 °C | ISO 11357-6 | >20 min |
| Carbon black content | ISO 6964 | 2.0–2.5 wt% |
| Carbon black dispersion | ISO 18553 | ≤3 |
On conventional single-screw pipe extrusion lines, DGDB-6097 is processed with a grooved-barrel feed section and a screw length-to-diameter ratio of 30:1 to 33:1. The screw compression ratio is typically 3.0:1 to 3.5:1, and the barrel temperature profile is set from 180 °C at the feed zone to 220 °C at the metering zone, with die head temperatures maintained at 210–220 °C. Melt temperature measured at the die entry is normally kept between 210 °C and 230 °C. At these settings, the high-molecular-weight fraction remains stable, and melt pressure fluctuations on a 75 mm extruder are generally below 0.5 MPa when the screen pack is clean. Residence time must be minimised; above 240 °C or beyond 20 min of hold-up, oxidative chain scission can generate gel particles and increase the melt flow rate beyond the specification ceiling.
Pre-drying is not required for sealed packaging. If the resin is exposed to ambient air with relative humidity above 75 %, surface moisture can create micro-voids in the extrudate; hopper drying at 80 °C for 2 h is then recommended. Grooved-barrel feed zones require sufficient back-pressure control because the high-molecular-weight fraction produces a pronounced shear-thinning response. Melt fracture at the die lip is less common than with unimodal grades of equivalent density, but excessive screw speeds above 120 rpm on a 75 mm machine can generate localised thermal peaks and should be validated with melt-pressure transducers at the breaker plate. Calibration sleeves are ordinarily held at 20–30 °C with a sizing vacuum of 0.03–0.06 MPa; these values are equipment-specific rather than material constants.
The grade’s bimodal architecture raises the apparent viscosity in extensional flow, which improves sag resistance during large-diameter pipe extrusion relative to conventional unimodal HDPE pipe grades. However, this also increases the sensitivity of the melt to stagnant zones in spiral mandrel dies. Pipe converters should avoid abrupt cross-sectional transitions at the adaptor and use purged, streamlined flow channels to prevent gel accumulation. Batch-to-batch variation in carbon black dispersion is typically low but should be monitored by ISO 18553 when changing raw-material lots because poor dispersion can nucleate slow crack growth in notched pipe tests.
The grade’s primary application is solid-wall pressure pipe for buried potable water and natural gas distribution. Pipe made from DGDB-6097 is evaluated under ISO 9080 for PE100 classification, and the hydrostatic design stress is derived at 20 °C for 50 years. The compound is used in SDR 11 and SDR 17 pipe dimensions; the actual pressure rating depends on the service coefficient and operating temperature defined in ISO 4427-2 for water or ISO 4437-2 for gas. Notched pipe tests under ISO 13479 at 80 °C and 4.0 MPa are employed to confirm slow crack growth resistance. Rapid crack propagation resistance for gas pipe in cold regions is assessed by the S4 test of ISO 13477 at 0 °C. Published field data for this specific compound in large-diameter DN 250 SDR 11 configurations are limited, but PE100 formulations with comparable density and MFR typically withstand critical pressures exceeding 10 bar in the S4 test. The carbon black dispersion grade of ≤3 per ISO 18553 provides resistance to ultraviolet degradation during outdoor storage for periods up to 12 months under temperate conditions.
The principal difference is the raising of the minimum required strength from 8.0 MPa for PE80 to 10.0 MPa for PE100. This permits wall thickness reduction of approximately 20 % at the same nominal pressure rating when pipe design follows ISO 12162-1 and ISO 4427-2. The bimodal architecture also changes the failure mode distribution. Unimodal PE80 materials under constant internal pressure can exhibit an earlier ductile-to-brittle transition than bimodal PE100, particularly in notched pipe tests. DGDB-6097 typically shows longer failure times under ISO 13479 conditions at 80 °C and 4.0 MPa than unimodal PE80 grades of similar density, because the high-molecular-weight fraction ties together crystalline lamellae and resists crack propagation.
Processability is not proportionally reduced. The low-molecular-weight fraction contributes high shear thinning, so extrusion line output on a grooved-barrel 75 mm machine can remain within 10 % of a unimodal grade with similar density, despite a higher weight-average molecular weight. This differs from conventional unimodal HDPE, where raising molecular weight increases both low-shear and high-shear viscosity. In film extrusion grades with melt flow rates of 0.5–1.0 g/10 min at 190 °C and 5 kg and densities of 0.948–0.953 g/cm³, the molecular architecture lacks sufficient slow crack growth resistance and cannot carry a PE100 classification. Blow-moulding grades with similar density but narrower molecular weight distribution exhibit lower melt strength and cannot sustain the long-term hydrostatic design basis required for pressure pipe.
The carbon black package differentiates DGDB-6097 from natural PE100 base resins. The 2.0–2.5 wt% carbon black content provides ultraviolet stabilisation for above-ground storage and is specified for black pressure pipe under ISO 4427-2 and ISO 4437-2. Natural PE100 grades used for indoor industrial pipe may omit carbon black and require separate UV stabilisation if exposed to sunlight. The carbon black dispersion limit of ≤3 per ISO 18553 is tighter than many non-pressure HDPE grades and is directly linked to long-term hydrostatic strength because carbon black agglomerates act as stress concentrators. The comonomer type and catalyst system used in DGDB-6097 are not fully disclosed in public trade literature, but the bimodal distribution and PE100 classification indicate a hexene- or butene-based copolymer architecture optimised for slow crack growth rather than stiffness alone.
Daqing DGDB-6097 is not recommended for injection moulding of thin-wall articles, rotational moulding, or cast film. Its high melt viscosity and carbon black content make those processes economically and technically unsuitable. The product should be stored in a dry, ventilated area away from direct sunlight at ambient temperatures below 40 °C. Reclaimed material can be used only if the quality plan of the pipe manufacturer verifies conformance to ISO 4437-2 or ISO 4427-2. The maximum permissible rework ratio depends on the final pipe standard and is typically limited to 10–20 % by mass for pressure pipe with no more than one additional heat history. Combination with amine-based additives or certain phenolic antioxidants may alter oxidation induction time; additive packages must be validated by ISO 11357-6 before production. Avoid blending with low-molecular-weight polyethylene waxes above 1 wt% because the resulting melt flow rate shift can move the material outside the PE100 slow crack growth window. If rework introduces moisture, vacuum-vented extrusion is insufficient at relative humidities above 85 %; conditioned rework drying at 70–80 °C for 3 h is required to maintain melt homogeneity.