| HS Code | 985916 |
| Density | 0.954 g/cm³ |
| Melt Flow Rate | 0.35 g/10 min (190°C/2.16 kg) |
| Tensile Strength At Yield | 25 MPa |
| Elongation At Break | >500% |
| Flexural Modulus | 1,000 MPa |
| Notched Izod Impact Strength | 100 J/m |
| Vicat Softening Temperature | 125°C |
| Heat Deflection Temperature | 70°C |
| Brittleness Temperature | -70°C |
| Environmental Stress Crack Resistance | >1000 h |
| Hardness Shore D | 65 |
| Melting Point | 130°C |
| Water Absorption | <0.01% |
As an accredited Hanwha TotalEnergies HDPE C910C factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Hanwha TotalEnergies HDPE C910C is typically supplied in 25 kg multiwall bags, 40 bags per pallet, shrink-wrapped for shipping. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): Hanwha TotalEnergies HDPE C910C, 25 kg bags, palletized, stretch-wrapped, approx. 20–22 MT, securely strapped. |
| Shipping | Hanwha TotalEnergies HDPE C910C is a non-hazardous high-density polyethylene resin, typically shipped as pellets in 25 kg bags, 1,000 kg jumbo bags, or bulk containers. Transport by standard sea, rail, or road freight. Store dry, away from heat, moisture, and UV. Not regulated as dangerous goods. |
| Storage | Store Hanwha TotalEnergies HDPE C910C in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, flames, and strong oxidizers. Keep original bags or containers sealed to prevent moisture, dust, and contamination. Use first-in, first-out stock rotation. Avoid excessive stacking, protect from ignition sources, and follow the manufacturer’s safety data sheet and local regulations. Ensure stable pallets and adequate ventilation. |
| Shelf Life | Shelf life is typically 24 months if stored in original packaging, cool, dry, well-ventilated area, away from direct sunlight. |
Injection moulding of 10 L to 60 L open-head pails from Hanwha TotalEnergies HDPE C910C is executed on hydraulic accumulator or servo-electric machines with clamp forces from 800 t to 1200 t and screw diameters between 70 mm and 90 mm. Melt temperature is maintained from 220 °C to 250 °C at the nozzle. Coolant inlet temperature is set from 10 °C to 20 °C. Injection pressure ranges from 70 MPa to 110 MPa. Hold pressure is set at 45% to 65% of peak pressure for 8 s to 14 s, depending on gate solidification. Pail sidewall thickness normally lies between 2.0 mm and 6.0 mm. Wall stock below 2.0 mm can freeze before adequate packing, causing sink marks around the handle bridge and top rim. Gate design uses a tab gate with land length below 1.5 mm or a two-drop hot runner with gate diameters from 3.0 mm to 6.0 mm to reduce jetting and surface splay. Batch-to-batch rheology is controlled by ISO 1133-1:2022 melt mass-flow rate measurement. MFR drift above 0.5 g/10 min against the approved production lot can shorten fill rate and disturb the hold-pressure window. Chemical resistance is assessed per ASTM D543-21 by immersion in 10% NaOH, 5% NaOCl, 30% H₂SO₄ and a commercial surfactant solution for 30 days at 23 °C. Acceptance is commonly based on tensile yield retention above 85% and the absence of visible stress cracking at the gate and handle weld line. Food-grade pails require compliance with 21 CFR 177.1520(c) and (EU) No 10/2011. Overall migration into food simulants must remain below 10 mg/dm². The same resin is not recommended for sustained contact with toluene, xylene, chlorinated solvents or oxidizing acids above 30% concentration at elevated temperature. Production-scale observations show that handle hinge webs below 3.0 mm thickness can develop weld lines and impact fracture at -18 °C. The hinge should be gated directly or thickened to at least 4.0 mm with an internal radius above 1.0 mm. Pigmented pails using 1.5% to 2.0% colour masterbatch do not require predrying when stored in sealed containers at relative humidity below 60%.
Closure moulding experiences a direct conflict between cycle-time compression and environmental stress crack resistance. HDPE C910C is injected into 12-cavity to 48-cavity hot-runner tools with valve gate diameters from 0.6 mm to 1.2 mm, melt temperatures from 220 °C to 260 °C, and mould coolant maintained at 8 °C to 20 °C. Shear rates above 50,000 s⁻¹ at the gate land can reduce molecular weight at the gate surface and produce streaked caps with lower ESCR. Residual hoop stress is generated when the cap is ejected before full thermal relaxation. This stress is highest at the thread root and the tamper-evident bridge. Thread root radii below 0.3 mm act as stress concentrators and should be increased to at least 0.4 mm. Bridge thickness from 0.25 mm to 0.45 mm must be validated against removal torque and ejection cracking. ESCR is measured by ASTM D1693-15 using notched plaques immersed in 100% Igepal CO-630 at 50 °C. The F50 time is used for lot acceptance against a target established by the closure user. Removal torque is recorded with a calibrated torque meter after 24 h at 23 °C. For 30/25 mm neck finishes, torque values below 1.2 N·m may indicate leakage risk and values above 2.0 N·m may generate consumer rejection. Published data for HDPE C910C in this exact geometry is limited. Closure performance must be confirmed on the production tool intended for use. Food-contact caps and closures are assessed under (EU) No 10/2011 and 21 CFR 177.1520(c). Bleach and detergent closures are exposed to 5% sodium hypochlorite at 40 °C for 30 days. Acceptance should show no visible cracks and no torque loss above 20% of the as-moulded value.
| Application area | Standard or regulation | Test condition | Purpose |
|---|---|---|---|
| Industrial pails | ASTM D543-21 | Aqueous chemical immersion, 23 °C, 30 days | Chemical resistance, no stress cracking |
| Food-contact pails | (EU) No 10/2011; 21 CFR 177.1520(c) | Overall migration limit 10 mg/dm² | Food-contact compliance |
| Closures | ASTM D1693-15 | 100% Igepal CO-630, 50 °C | Environmental stress crack resistance |
| Pallets | ISO 8611-1:2021 | Racking load deflection | Structural stability |
| Refuse bins | EN 840:2020 | Cold impact at -20 °C | Impact durability |
| Underground boxes | EN 124:2015 | Static load class, B125 | Load-bearing integrity |
Nestable and rackable pallets produced from HDPE C910C are typically moulded on large two-platen machines with clamp forces from 2,000 t to 3,500 t and shot capacities above 25 kg. Sequential valve gating is used across the 1,200 mm × 1,000 mm mould face to reduce weld-line depth and prevent premature freezing at the mid-rib. Pallet weight ranges from 12 kg to 28 kg. Top deck thickness ranges from 4.0 mm to 8.0 mm. Rib thickness is set from 3.0 mm to 6.0 mm. Cycle time falls between 60 s and 100 s. Melt temperature is kept from 220 °C to 250 °C. Mould temperature is set from 12 °C to 25 °C with independent cooling circuits under the bosses. Static and dynamic tests follow ISO 8611-1:2021. Racking deflection under load commonly must remain below 25 mm at ambient temperature. Creep tests are performed under ISO 899-1:2017 at 23 °C and 40 °C for 1,000 h to verify that ribbed sections do not exhibit progressive deflection. Cold impact is a critical gate. Production records show that pallets with internal corner radii below 1.5 mm can crack at -20 °C when struck by forklift tines. For outdoor storage, UV stabilization with 1.5% to 2.5% carbon black masterbatch or a hindered amine stabilizer package is required. Accelerated weathering under ASTM D2565-21 for 2,000 h should not lower notched Izod impact below the application-specific minimum. Regrind from pallet reject grinding is reused at rates up to 25% by weight if the melt mass-flow rate under ISO 1133-1:2022 remains within 0.8 g/10 min of the virgin value. Paper label contamination must be removed before granulation. The resin should not be used for racking loads exceeding the pallet design envelope. Published data for HDPE C910C in racking creep beyond 1,000 h is limited.
Below a wall thickness of 0.9 mm, high-speed injection of HDPE C910C is limited by freeze-off during fill and by residual stress generated from extreme thermal gradients. Filling time is commonly 0.2 s to 0.5 s. Peak injection pressure rises to 90 MPa to 130 MPa. Melt temperature at the nozzle is kept from 230 °C to 270 °C. Mould coolant is held at 7 °C to 15 °C to achieve cycle times from 4 s to 8 s. Valve-gated hot runners with 8 to 24 drops and gate diameters from 0.6 mm to 1.0 mm deliver polymer into the cavity. Gate land shear rates above 50,000 s⁻¹ can create melt fracture, gate blush and reduced cold-chain impact resistance. Packing pressure is applied for 0.5 s to 1.5 s before gate freeze. Too short a pack creates sink marks near the rim. Too long a pack increases frozen-in stress and warpage. Warpage is controlled by measuring shrinkage according to ISO 294-4:2018 and adjusting differential coolant flow in the core and cavity halves. Drop impact at 0 °C to 4 °C is evaluated by ISO 6603-2:2023 or an equivalent instrumented puncture test. Cracks at the base corner indicate cold gate freeze. Cracks through the sidewall indicate shear-induced orientation. Top-load stability of filled and stacked tubs is assessed by ISO 12048:1994. Load levels are selected by the brand owner for the intended pallet height. Food-contact compliance is evaluated under (EU) No 10/2011 using 3% acetic acid and 10% ethanol simulants. Overall migration must not exceed 10 mg/dm². Published data for HDPE C910C in sub-0.5 mm dairy tubs is limited. Process validation on the specific hot-runner stack and downstream filling line is required before production approval.
Because buried water meter boxes and valve pit chambers are subjected to continuous soil pressure and occasional surface load, HDPE C910C requires a creep-resistant rib layout and controlled orientation. Typical wall thickness is 4.0 mm to 12.0 mm, with part weights from 2.0 kg to 10.0 kg. Structural evaluation is performed per EN 124:2015. Load class B125 specifies a static load of 125 kN with no structural failure. Creep behaviour is measured by ISO 899-1:2017 at 23 °C and 60% relative humidity. Deflection of load-bearing ribs after 1,000 h is compared with the initial deflection to identify progressive creep. Chemical exposure to groundwater contaminants is assessed under ASTM D543-21 using pH-adjusted water, 3% NaCl, 10% NaOH and mineral oil. Tensile yield retention after 30 days at 23 °C should remain above 85% with no surface cracking. For above-ground cable joint pits, UV stabilization is required. Addition of 1.5% to 2.5% carbon black masterbatch reduces surface chalking under ASTM D2565-21 for 2,000 h. Injection is performed at melt temperatures from 220 °C to 250 °C and mould temperatures from 15 °C to 25 °C. Clamp forces range from 500 t to 1,000 t. A single central gate is avoided because the resulting radial orientation can cause cracking at the base corners. Two or four submarine gates or a fan gate along the sidewall are used instead. Published data for HDPE C910C under long-term soil burial beyond 5 years is limited. Buried component qualification should include site-specific soil chemistry and load testing.
Recovery of post-industrial regrind from edge trim, start-up purges and rejected bins alters the melt rheology and low-temperature impact behaviour of HDPE C910C in wheeled refuse bins produced to EN 840:2020. Wheeled bins with capacities from 60 L to 360 L are injection-moulded on machines with clamp forces from 2,000 t to 4,000 t and screw diameters from 90 mm to 130 mm. L/D ratios from 24:1 to 28:1 with mixing sections are specified to homogenize regrind without excessive shear heating. Regrind addition rates from 20% to 30% by weight are common in non-food service bins. A shift in melt mass-flow rate under ISO 1133-1:2022 of more than 1.0 g/10 min compared with virgin granules indicates molecular weight reduction. At that threshold, Charpy notched impact at -20 °C measured by ISO 179-1:2010 may fall below the user’s minimum acceptance value. Bins are also tested by EN 840:2020 drop and body-impact methods at -20 °C and 23 °C. Cracking at the bottom skid or sidewall ribs is a rejection mode. Contamination by PP, PET or silicone gaskets from mixed post-industrial waste causes delamination and surface defects. Granulation must be preceded by metal separation and polymer sorting. UV stabilization for outdoor kerbside bins is achieved with 1.5% to 2.5% carbon black masterbatch. Accelerated ageing under ISO 4892-2:2021 for 2,000 h should show no surface cracking and a Delta E colour shift below the customer limit. When regrind is used, the material cannot be declared as food-contact under (EU) No 10/2011 unless the regrind stream is controlled under a specific quality system and authorized. The use of more than 30% regrind is not recommended for bins exposed to frequent sub-zero impact. Published data for HDPE C910C at high regrind fractions is limited.
In agricultural storage applications, HDPE C910C must resist UV irradiation, ozone, fertilizer salts and wetting agents used in crop protection formulations. Wall thickness is generally 2.0 mm to 5.0 mm, with stiffening ribs at 1.5 mm to 4.0 mm. Melt temperature from 220 °C to 250 °C and mould temperature from 10 °C to 20 °C are used to balance impact and shrinkage. Fertilizer contact is evaluated under ASTM D543-21 by immersion in 10% urea, 5% potassium chloride, 5% ammonium nitrate and a non-ionic wetting agent at 23 °C and 40 °C for 30 days. Tensile yield retention above 85% and no visual cracking are common acceptance criteria. ESCR under pesticide formulations is assessed by ASTM D1693-15 using the actual formulation or a surrogate agreed with the agrochemical supplier. Standard Igepal testing alone may not predict crack formation in concentrated ester-based solvents. UV resistance requires 1.5% to 3.0% carbon black masterbatch or a separate UV stabilizer system. Outdoor exposure under ISO 4892-2:2021 for 2,000 h is used to compare lot-to-lot resistance. In production, sharp internal ribs below 1.0 mm radius and gate weld lines at the base of the carry-handle area are common locations for low-temperature impact failure at -20 °C. Published data for HDPE C910C in prolonged pesticide contact is limited. Pre-production immersion tests with the actual commercial formulation are required.
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Hanwha TotalEnergies HDPE C910C is a bimodal high-density polyethylene compound supplied as black pellets and classified within the PE 100 pressure-pipe category. The PE 100 designation under ISO 12162:2009 and ISO 9080:2022 corresponds to a minimum required strength of 10 MPa at 20 °C for a 50-year lower-prediction limit. Melt flow rate is reported as 0.30–0.40 g/10 min at 190 °C/5 kg (ISO 1133-1:2022), with density reported as 0.955–0.960 g/cm³ (ISO 1183-1:2019). Carbon black loading of 2.0–2.5 wt% (ISO 6964) provides ultraviolet screening for outdoor storage and exposed piping. Principal applications include pressurised water distribution, industrial fluid transfer, and gas distribution lines in which long-term hydrostatic strength, slow crack growth resistance, and extrusion consistency are specified. The grade is specifically designed for pipe and thick-wall profile extrusion; it is not intended for thin-wall injection moulding or cast film processing where low melt viscosity and short cycle times govern.
| Parameter | Standard | Typical or specified value |
|---|---|---|
| Melt flow rate | ISO 1133-1:2022 | 0.30–0.40 g/10 min at 190 °C/5 kg |
| Density | ISO 1183-1:2019 | 0.955–0.960 g/cm³ |
| Tensile stress at yield | ISO 527-2 | 23–26 MPa |
| Elongation at break | ISO 527-2 | >500 % |
| Flexural modulus | ISO 178 | 850–950 MPa |
| Carbon black content | ISO 6964 | 2.0–2.5 wt% |
| Oxidative induction time | ISO 11357-6 | ≥20 min at 210 °C |
The structural distinction of C910C lies in its bimodal molecular weight distribution. The high molar mass fraction is produced with short-chain branches that form tie molecules between crystalline lamellae; the lower molar mass fraction reduces melt viscosity and improves extrudability. In service, this architecture raises the stress intensity required for slow crack growth, as reflected in notched pipe evaluations conducted under ISO 13479 and full-scale hydrostatic creep under ISO 9080.
Compared with a PE 80 compound, the 10 MPa MRS of a PE 100 material permits higher allowable hoop stress at the same pipe dimension. Using the ISO pipe wall-thickness calculation in ISO 4427-2, a transition from PE 80 to PE 100 can reduce wall thickness by approximately 20–25 % at equivalent diameter and pressure rating, or can increase pressure rating by roughly 25 % at constant wall thickness. The benefit is derived from the higher hydrostatic design basis and the corresponding reduction in pipe mass per metre; however, the thinner wall also increases the requirement for controlled fusion and handling damage prevention.
Against monomodal HDPE grades of similar density, C910C exhibits higher slow crack growth resistance and longer notched pipe failure times, although the comparison is method-dependent and should be verified on the specific pipe geometry. Unimodal grades used in blow moulding or film lack the same balance of 0.30–0.40 g/10 min melt flow and 10 MPa hydrostatic classification; their lower elongational viscosity may improve parison expansion but reduces long-term pressure containment. Where C910C is compared with natural PE 100 grades, the carbon black loading changes melt pressure drop and weld-line strength in spiral-mandrel dies; fusion and welding parameters must be adjusted.
In polyethylene pipe classification, the difference between PE 80 and PE 100 is not a simple tensile-strength increment. PE 100 compounds must demonstrate a lower-prediction hydrostatic strength of 10 MPa at 20 °C for 50 years under ISO 9080, while PE 80 compounds are accepted at 8 MPa. The practical effect appears mainly in pipe dimensioning calculations; for a given SDR, the allowable operating pressure rises when the MRS increases, or for a given pressure class, the wall thickness may be lowered.
On production-scale grooved-barrel single-screw extruders with L/D ratios of 30:1 to 38:1, C910C is processed with barrel temperature profiles commonly set between 190 °C and 220 °C and an adapter melt temperature of 210–230 °C. High-density polyethylene pipe compounds in this viscosity range require sufficient head pressure to fill calibration sleeves and maintain pipe roundness; measured head pressures often fall between 25 MPa and 40 MPa depending on screw diameter, die gap, and output. Output stability depends on grooved-feed barrel temperature control; excessive feed-section temperatures above 90 °C can reduce conveying efficiency and increase melt temperature variation.
If pellet surface moisture is found after storage in humid environments, hopper drying at 80 °C for 2 h may be applied before extrusion; the producer’s processing guide defines the moisture limit for C910C. Extrusion rate is also constrained by die-lip shear stress. When shear stress approaches the critical value for sharkskin surface defects, melt temperature or die gap must be adjusted. C910C is not intended for cast film or sheet gauges below 1 mm; draw resonance and web instability occur earlier than in low-viscosity extrusion grades.
For weld-line integrity and wall-thickness uniformity, spiral-mandrel dies with a low-weld-line overlap angle are preferred over spider-leg dies when C910C is used for pressure pipe. The elongational viscosity of the bimodal high molar mass fraction stabilises the parison and reduces sag in large-diameter thick-wall pipe. Published data for C910C in coextruded multilayer pipe structures is limited; if the material is considered for an outer black layer over natural PE 100, interfacial fusion and melt-strength compatibility must be evaluated at the producer level.
Joints in C910C pipe are butt-fused or electrofused using equipment calibrated to ISO 21307 or national equivalents. For butt fusion, the heater plate surface temperature is normally held near 220 °C; interfacial bead geometry and fusion pressure depend on pipe wall thickness and SDR. Weld procedures must account for the high molar mass fraction because insufficient soak time can produce a weld with lower slow crack growth resistance than the parent pipe. The cooling time in butt fusion is extended as wall thickness increases, and the pipe must be held against lateral movement during cooling to prevent microcracks.
As melt temperature or screw speed exceeds the safe processing boundary, thermal-oxidative degradation of the polyethylene backbone becomes detectable. The stabilisation package in C910C is quality-controlled by oxidative induction time at 210 °C according to ISO 11357-6; a typical value of ≥20 min is reported for compound-level pipe grades. However, OIT is not a direct predictor of long-term service life; hydrostatic pressure testing under ISO 9080 and chlorine-resistance pipe testing remain the relevant design evidence. Extruder melt temperatures above 240 °C or extended residence times can consume phenolic antioxidant and phosphite stabiliser components, resulting in gel streaks, microgel formation, and surface roughness at the die exit.
Such defects observed on production lines are frequently associated with worn screw/barrel surfaces, insufficient backpressure, or low head-pressure operation. When C910C is processed on twin-screw compounding equipment, lower-stress mixing is preferred to avoid over-smearing the carbon black and high molar mass fraction. If project specifications require a minimum OIT after extrusion, the measurement should be conducted on the pipe wall rather than on pellets because melt processing history reduces antioxidant concentration.
Under the test ladder for PE 100 pipe materials, extruded pipe specimens of C910C are evaluated for hydrostatic strength over time-temperature windows in ISO 9080:2022. The minimum required strength of 10 MPa is a statistical lower prediction limit, not a short-term yield value. Slow crack growth resistance is assessed on notched pipe specimens under ISO 13479; published data for C910C in a specific diameter and SDR should be obtained from the producer when project specifications require notched pipe lifetimes. Rapid crack propagation resistance for gas distribution can be assessed by the full-scale critical pressure method in ISO 13478; PE 100 compounds are ordinarily specified for smaller diameter gas mains where this property is controlling.
Short-term tensile data for C910C indicate a yield stress of 23–26 MPa (ISO 527-2), elongation at break above 500 % (ISO 527-2), and flexural modulus of 850–950 MPa (ISO 178). These values demonstrate the stiffness and ductility expected of a high-density pipe compound but do not replace long-term creep and slow crack growth data. For pipe applications, the relevant mechanical qualification is not single-point tensile testing; it is the time-to-failure curve at 20 °C and elevated temperatures, including the 50-year lower-prediction limit.
The carbon black loading of 2.0–2.5 wt% functions as both ultraviolet stabiliser and opacity source. Dispersion quality is assessed by ISO 18553, which classifies pigment agglomerates and undispersed particles in polyolefin pipe compounds. Poor carbon black dispersion creates local stress concentrations that can initiate brittle slow crack growth; pipe standards such as ISO 4427-1 and EN 12201-1 require dispersion ratings that exclude visible agglomerates above defined size thresholds. Above-ground exposed pipe stock should be protected from long-term contact with organic solvents, aromatic hydrocarbons, and strong oxidising acids. Ultraviolet exposure is acceptable for carbon black-stabilised pipe during prescribed storage periods, but long-term above-ground service in high-UV geographies requires project-specific engineering review and is not resolved solely by carbon black loading.
For potable water service, approvals for C910C are jurisdiction-specific. The compound is generally supplied for pipe conforming to ISO 4427, EN 12201, or national derivatives, but certification for water-contact programmes such as AS/NZS 4020 or NSF/ANSI 61 must be confirmed with the producer. The base polyethylene may be referenced against food-contact requirements of FDA 21 CFR 177.1520 when used in food processing water transfer, though this is not the primary service profile. Combustion of the compound releases carbon monoxide and carbon dioxide; processing fumes should be controlled by local exhaust ventilation during extrusion. Melt mixing with acidic additives, chlorinated polymers, or materials that liberate halogens at processing temperatures can accelerate degradation and should be avoided. Published data for C910C in hot chlorinated water above 40 °C under sustained pressure is limited; design life predictions in such oxidising environments require specific pipe testing not captured by ISO 9080 alone.