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Angst+Pfister HDPE UH.429-01

    • Product Name: Angst+Pfister HDPE UH.429-01
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 289221
    Product Name Angst+Pfister HDPE UH.429-01
    Material High-density polyethylene (HDPE), ultra-high molecular weight
    Density 0.93-0.94 g/cm³
    Molecular Weight 3-6 million g/mol
    Tensile Strength 20-22 MPa
    Elongation At Break >500%
    Tensile Modulus 700-1000 MPa
    Shore D Hardness 60-65
    Charpy Notched Impact Strength No break
    Melting Point 130-135 °C
    Maximum Service Temperature +80 °C
    Minimum Service Temperature -200 °C
    Thermal Conductivity 0.4 W/(m·K)
    Coefficient Of Linear Thermal Expansion 2.0 × 10⁻⁴ 1/K
    Specific Heat Capacity 1.9 kJ/(kg·K)
    Water Absorption <0.01%
    Dielectric Strength 45 kV/mm
    Volume Resistivity >10^15 Ω·cm
    Dielectric Constant 2.3
    Coefficient Of Friction 0.10-0.20
    Abrasion Resistance Very high
    Chemical Resistance High; resistant to most acids, alkalis, alcohols, and solvents
    Uv Resistance Poor unless UV stabilized
    Flammability UL 94 HB
    Color Natural / Black

    As an accredited Angst+Pfister HDPE UH.429-01 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Angst+Pfister HDPE UH.429-01 is supplied in 25 kg sealed polyethylene bags, stored dry and away from direct sunlight.
    Container Loading (20′ FCL) 20′ FCL container loaded with palletized Angst+Pfister HDPE UH.429-01; non-hazardous cargo, securely strapped, labeled, with shipping documents, ready for export.
    Shipping Angst+Pfister HDPE UH.429-01 is a non-hazardous, solid HDPE polymer. It is not regulated as dangerous goods for transport (ADR/IMDG/IATA). Ship in clean, dry, sealed packaging; protect from UV, heat, moisture, and contamination. Normal handling applies; no special transport labels required. No UN number is assigned. Keep packaging closed until use.
    Storage Store Angst+Pfister HDPE UH.429-01 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep containers tightly closed and clearly labeled. Prevent contact with oils, solvents, or contaminants. Maintain stock rotation and follow local regulations. Avoid excessive stacking or physical damage. Use appropriate secondary containment if required. Store away from incompatible substances.
    Shelf Life Angst+Pfister HDPE UH.429-01 has no defined shelf life when stored cool, dry, ventilated, and protected from UV, heat, and contaminants.
    Application of Angst+Pfister HDPE UH.429-01

    In dry or slurry-based mineral handling circuits, the controlling variable in liner service life is low-stress sliding abrasion combined with intermittent impact at conveyor transfer points. Angst+Pfister HDPE UH.429-01 is specified for chute liners, hopper liners, dump truck tray liners, and belt skirting through compression-moulded slab stock that is CNC-machined into bolt-on panels. The exposed surface functions as a low-friction, hydrophobic wear face that reduces material hang-up and build-up on transfer chutes. Abrasion resistance is assessed by ASTM G65 Procedure A using a 229 mm diameter rubber-rimmed wheel rotating at 200 ± 10 rpm under a 130 ± 2 N normal load, with dry sand introduction calibrated between 300 g/min and 400 g/min. Wet slurry abrasion is characterised by ASTM G75 Miller Number testing, which gives a relative ranking under solid-liquid erosion in mineral slurries. Published data for this specific grade configuration is limited for high-impact service; where rock size exceeds 150 mm or free-fall height exceeds 1.5 m, the liner should be prototype-tested because the low-stress abrasion model does not capture impact fracture at high strain rate.

    Processors compression-mould unfilled ultra-high molecular weight polyethylene grades at melt-contact temperatures generally between 200 °C and 230 °C, with holding pressure maintained above 10 MPa to consolidate the high-viscosity powder or granular feed. Platen parallelism and symmetrical cooling determine residual stress in the slab; panels that are unclamped too early can develop centre-to-edge thickness variation and subsequent fastener-tearing in the field. The bolt-and-cap arrangement on a chute liner uses countersunk or through-bolted stainless steel fasteners with polymer washers, and bore clearances are calculated using a thermal expansion coefficient in the range of 1.5 × 10⁻⁴ K⁻¹ to 2.0 × 10⁻⁴ K⁻¹. Continuous service above 60 °C reduces compressive creep resistance and requires re-torquing cycles. The terminal components are replaceable liner packs cut to the transfer chute geometry, including box-section wear plates, deflector plates, and cone liners for bin discharge.

    Test methodPurpose in mining liner qualificationReported parameter
    ASTM G65 Procedure ADry sand/rubber wheel abrasionVolume loss in mm³
    ASTM G75Wet slurry abrasion resistanceMiller Number
    ISO 11542-2Specification for compression-moulded sheetTensile strength, elongation, density
    ISO 62Water absorption after immersionPercent mass change

    What Limits Plaque Warpage When Machining Food Grade Guide Rails?

    Food-contact bottling and packaging lines use compression-moulded UHMWPE for guide rails, starwheel change parts, screw conveyor flights, and timing worms because the material can be machined into high-complexity cross-sections without external lubrication and offers low product-transport friction against PET, glass, and aluminium containers. The limiting processing variable is not melt flow but residual stress in the moulded plaque; asymmetrical cooling, premature unclamping, or non-uniform platen temperature above ±5 °C produces density gradients that appear as dimensional instability after slot cutting. To reduce distortion, the stock shape is annealed before machining at 80 °C to 100 °C in forced air for 1 h per 25 mm of cross-section. Machining uses sharp positive-rake tooling, typically polished carbide or polycrystalline diamond, with low cutting forces and high surface speeds to avoid linting and edge burr. Glass-fibre or mineral fillers are not introduced because any exposed filler at the guide surface can scratch container walls or increase contamination risk.

    Compliance is evaluated under FDA 21 CFR 177.1520 for olefin polymers and EU Regulation No 10/2011. Overall migration must not exceed 10 mg/dm² under the most severe food-contact conditions of time and temperature for the intended use. For dry and aqueous food types up to 40 °C, the material is commonly judged acceptable when supported by a grade-specific certificate; fatty foods, high-temperature filling, and retort conditions require additional migration testing using food simulants from EU 10/2011 Annex III, including 50% ethanol for fatty and alcoholic simulant conditions. Terminal components include bottle transfer rails, neck guides, variable-speed side-grip belts, and starwheel entries. The operational boundary is that continuous wet steam cleaning above 60 °C can cause localised creep at bolted joints, and the material is not suitable for direct contact with hot oil or hot lard above the tested conditions without a separate compliance assessment.

    Standard or regulationApplication boundaryRequired condition
    FDA 21 CFR 177.1520Olefin polymers in indirect or direct food contactGrade-specific compliance letter for food type and temperature
    EU No 10/2011Plastics intended for food contactOverall migration ≤ 10 mg/dm²
    EU 10/2011 Annex IIISimulant selection for migration testingSimulant and time/temperature per intended use
    ISO 1183-1Density verificationMaterial identity against specification

    Because wastewater clarifiers and sludge thickeners operate with continuous low-speed drag of polymer blades over concrete or steel track surfaces, the acceptance criterion for scraper blade profiles is creep-dominated dimensional retention combined with low water absorption. Grade UH.429-01 is ram-extruded into rectangular or tapered profile sections, then CNC-machined for bolt slots, wear strips, and end connections on collector flights. Water absorption after 24 h immersion by ISO 62 is below 0.01%, which prevents dimensional swelling in continuously submerged service. Creep modulus measured by ISO 899-1 at the design temperature, typically 20 °C to 40 °C, is used to calculate bolt-hole bearing stress and blade deflection. Failure modes observed on production-scale clarifier lines include bolt-hole elongation from over-tightening, edge notching at concrete panel joints, and abrasive wear at the lower edge contact. Screw conveyor and clarifier builders specify slotted mounting holes and polypropylene or stainless backing washers to accommodate thermal expansion and avoid compressive creep under fastening load. The terminal components are rectangular scraper blades, tank-bottom squeegees, chain guides, and rail spacers; blades are replaced based on measurable thickness loss at the contact edge rather than on a fixed operating-hour interval.

    Battery Separator Extrusion Vent Port Pressure and Molecular Orientation

    In microporous membrane manufacturing for lithium-ion cells, ultra-high molecular weight polyethylene is processed by gel extrusion in which a high-molecular-weight resin is compounded with an extractable plasticiser before calendering, orienting, and solvent extraction. The resulting separator is a microporous film inserted between anode and cathode to block electronic contact while permitting ionic transport. For this process stream, vent port pressure, melt filtration, and plasticiser distribution are more critical than standard mechanical properties. A grade intended for battery separator use must exhibit consistent solution viscosity measured by ISO 1628-3, narrow molecular-weight distribution, and low residual metal or ash content. Published data for the specific Angst+Pfister HDPE UH.429-01 configuration in battery separator service is limited; qualification requires additional testing for Gurley permeability, pore size distribution, pin-pull strength, ionic conductivity, and electrochemical stability that is not covered by conventional polyolefin data sheets. Processors evaluating this niche should confirm that the grade is available in a dedicated battery-separator powder or pellet form and that the lot-level purity meets cell-maker specifications.

    At the extruder, gel feed stages use intermeshing twin-screw extruders with controlled barrel zones and high-torque drives; vent port pressure must be held stable to avoid plasticiser flashing or gel starvation. The material cannot be characterised by conventional ISO 1133-1 melt flow rate because ultra-high molecular weight polyethylene exhibits extremely high viscosity at low shear rates. Instead, solution viscosity or capillary rheometry at shear rates below 0.01 s⁻¹ is used. Process conflicts arise from the high melt elasticity and gel-phase memory: too much shear orientation in the die can produce anisotropic shrinkage after extraction, and insufficient draw-down produces non-uniform film thickness. Terminal separator film thickness is commonly in the range of 5 µm to 25 µm, but validation on a full production line is required for any lot not previously used in cell assembly.

    When HDPE UH.429-01 Replaces Cast Nylon in Chain Guides

    Packaging and general conveying lines select UHMWPE chain guides to replace cast nylon when moisture absorption, lubrication carryover, and chain wear are concurrent problems. In bottle and carton transport, stainless steel or acetal chains slide against guide strips that are CNC-machined from compression-moulded sheet. The specific advantage over cast nylon is lower water absorption by ISO 62 and lower kinetic coefficient of friction against the chain surface, which reduces drive motor current and chain tension. Hardness is measured by ISO 868 or ASTM D2240 Shore D, and tensile properties are verified by ISO 527-2 or ASTM D638. The guide profile has a low-PV sliding contact limit; continuous dry sliding velocity above approximately 1 m/s or accumulation of heat above 60 °C can soften the wear face and accelerate material transfer. Production-scale bottling lines therefore install guides with a machined clearance of 0.5 mm to 1.5 mm against the chain side edge, and water spray is used when line speed exceeds the rated PV limit. Terminal components include corner tracks, chain support rails, return guides, and transfer fingers for modular belt conveyors.

    Historically, port and shipyard fender facings have moved from hardwoods to rubber, then from rubber to high-density polyolefins where low friction against hull plating and reduced marine growth adhesion are required. UHMWPE fender pads are machined from compression-moulded slabs and bolted onto quay walls, lock gates, and vessel berthing dolphins. The material is selected when a berthing structure must tolerate angular approach without high friction spikes. ISO 62 water absorption below 0.01% eliminates swelling and dimensional change during tidal immersion cycles. The low dry and wet coefficient of friction reduces horizontal reaction transmitted to quayhead structures. However, the operational boundary is thermal distortion: ISO 75-2 heat deflection temperature and ISO 306 Vicat softening temperature for unfilled UHMWPE are well below those of cast metals or glass-reinforced thermosets, so fender pads must be shielded from direct sunlight-induced surface heating above 60 °C where possible. Abrasion loss is commonly rated by ISO 9352 or ASTM D4060 abrasive wear. The terminal product is a dock fender facing system combining UHMWPE pads, high-yield anchor bolts, and elastomeric backing pads; bolt preload is limited to avoid creep thinning and subsequent loosening.

    Control Preload in Acid Slurry Pump Casing Wear Plates

    Immersion testing in mineral acids is conducted by ISO 175 and ASTM D543 to determine mass change, dimension change, and appearance after exposure. For unfilled ultra-high molecular weight polyethylene, dilute sulfuric acid at ambient temperature normally produces negligible mass change when the concentration is below 60% and temperature is below 40 °C. At concentrations above 80% or temperatures above 50 °C, oxidative attack accelerates, and the material should not be used with strong nitric acid, oleum, or halogen-containing oxidising process streams. In pump casing wear plate configurations, the dominant failure mode is not chemical attack but compressive creep under metal fastener preload. The wear plate is a circular or volute-shaped insert machined from compression-moulded slab, fitted into the pump casing to protect the casting from high-solids acidic slurry. Bolt preload must be torque-controlled and limited because UHMWPE under continuous compression loses thickness over the first 24 h to 72 h of load relaxation. Manufacturers use polymer washers, slotted holes, and measured torque below the value that produces 1 mm of initial compressive displacement. The terminal components are machined casing liners, wear rings, and filter press plate linings for centrifugal pumps handling abrasive acidic slurries. Dimensional inspection after installation should include thickness measurement at six radial positions and re-torqueing after the initial relaxation period.

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    Certification & Compliance
    More Introduction

    Angst+Pfister HDPE UH.429-01 is a semi-finished high-density polyethylene product whose vendor code combines the base polymer family with an internal modification or colour reference. The material belongs to the PE-HD class under ISO 1043-1; the suffix UH is not an ISO standardized designator but is commonly associated with higher molar mass relative to standard PE-HD grades. The designation 429-01 is best read as a supplier-specific formulation and colour field rather than a mechanical property class. Published data for this specific configuration is limited; therefore, the following technical description uses the documented family behaviour of PE-HD semi-finished stock shapes tested under ISO 1183-1, ISO 527-2, ISO 179-1, and ISO 306, with values reported as bands when the exact sub-grade certificate is not referenced. Regulatory status cannot be assumed from the commercial designation alone. Unpigmented high-density polyethylene can be formulated to meet EU Regulation 10/2011 and FDA 21 CFR 177.1520, but the specific UH.429-01 product may contain processing aids or colourants that alter compliance. A REACH SVHC statement under Regulation (EC) No 1907/2006 and RoHS verification under 2011/65/EU should be obtained from Angst+Pfister for the actual batch.

    What tests should govern incoming inspection of HDPE UH.429-01?

    Because semi-finished HDPE is processed by extrusion or compression moulding, orientation and skin-core effects can influence mechanical values. Incoming inspection therefore should not rely solely on supplier datasheet medians; the certificate of analysis should carry the actual batch melt-mass-flow rate or melt-volume-flow rate under ISO 1133-1, density under ISO 1183-1, and, where process-critical, tensile yield stress under ISO 527-2. For high-molar-mass PE-HD, the melt-flow rate may be too low to measure with the standard 2.16 kg load; a 21.6 kg or 5 kg condition is often reported. If the UH designation reflects a molecular-weight increase, an MFR under 2.16 kg at 190 °C below 0.1 g/10 min may be observed, but the exact figure must be read from the batch certificate.

    Moisture uptake of PE-HD is below 0.01 % after 24 h immersion in water at 23 °C under ISO 62, so pre-drying is generally unnecessary unless the stock has surface condensation from low-temperature storage. Conditioning is still advised before dimensional inspection: polyethylene expands roughly 150–200 × 10⁻⁶ K⁻¹; a temperature difference of 10 °C across a 1000 mm sheet can change its length by approximately 1.5–2.0 mm. These values are family-level calculations and do not replace the supplier coefficient for the specific UH.429-01 batch.

    Documented family reference bands for PE-HD semi-finished materials
    Property Test method Typical PE-HD band Significance for UH.429-01 selection
    Density ISO 1183-1 0.94–0.97 g/cm³ Confirms base resin classification and filler absence
    Tensile yield stress ISO 527-2 22–32 MPa Used for initial load-bearing calculations
    Tensile modulus ISO 527-2 800–1100 MPa Indicates stiffness relative to PP and engineering plastics
    Notched Charpy impact strength, 23 °C ISO 179-1/1eA 4–10 kJ/m² High-molar-mass sub-grades may approach or exceed the upper band
    Vicat softening temperature ISO 306/A50 120–130 °C Determines short-term hot-contact limit only
    Water absorption, 24 h ISO 62 <0.01 % Supports use in humid and aqueous environments

    These bands are not vendor guarantees for HDPE UH.429-01. They are reference ranges for PE-HD semi-finished materials and must be superseded by the approved technical data sheet for the specific colour and sheet thickness.

    In fabricated acid-etching fixtures, HDPE UH.429-01 is specified where a non-porous low-drag surface reduces sludge adhesion on weir plates and immersion grids. For a 20 wt% sulfuric acid bath at 40 °C, PE-HD generally withstands continuous immersion, but oxidising acids such as concentrated nitric acid above 30 wt% can embrittle the polymer and should be excluded without specific compatibility testing. Alkaline cleaning cycles using 5–10 wt% sodium hydroxide at 60 °C are within the documented resistance band of PE-HD; however, surfactant-laden solutions may alter the surface free energy and reduce paint or adhesive bonding after exposure. In gluing operations, untreated PE-HD is poorly bondable and requires flame, plasma, or corona treatment; polar adhesives alone typically delaminate from PE-HD because surface energy remains below 36 mN/m unless activated.

    Thermal joining and machining performance of HDPE UH.429-01 stock shapes

    On three-axis CNC machining centres, HDPE stock is often machined with carbide end mills having high positive rake and deep flutes; excessive spindle speed or low feed per tooth can melt the chip and cause rewelding on the flank. For a 12 mm diameter two-flute cutter, a surface speed of 300–600 m/min and a feed of 0.1–0.3 mm/tooth has been reported in workshop guidance as a starting point; published data for this specific grade is limited. Unlike acetal or glass-filled materials, HDPE does not produce hard abrasive particles, but cutters must be sharp because the material’s low modulus allows workholding distortion. Vacuum pods may pull thin sheets out of flatness if the cutting depth exceeds 1.5 mm per pass for sheet thickness below 20 mm.

    Heated-tool butt welding of PE-HD typically uses a plate temperature of 200–220 °C and a joining pressure of 0.15–0.25 MPa; hot gas welding with PE-HD rod requires a gas temperature of 250–300 °C at the nozzle and clean, oxidation-free weld prep. Because higher molar mass raises melt viscosity and reduces melt-flow under pressure, the UH-coded product may require a longer heating phase than standard PE-HD. Welding parameters should be qualified to DVS 2207-1 or supplier procedure specifications rather than transferred directly from other PE-HD grades.

    Thermoforming of HDPE for orthotic shells uses sheet temperatures between 150 °C and 180 °C. The sheet should be heated until the core reaches forming temperature but not above 200 °C, where surface oxidation can generate carbonyl groups and reduce weldability. A double-sided IR oven with ceramic elements is preferred; single-sided heating can curl the sheet because the unheated side remains below the forming window. If the UH code denotes a higher molar mass, sag resistance may be greater than standard PE-HD, allowing slightly higher sheet temperatures but requiring higher vacuum or plug assist to force the sheet into the mould. Clinicians and fabricators should not extrapolate forming cycles from unfilled PP or copolyester without running a pilot plaque.

    When HDPE UH.429-01 replaces standard extruded PE-HD in wear-prone guide rails

    Changeover from standard PE-HD to a higher-molecular-weight HDPE in chain guides and bottling line rails is driven by two failure modes: abrasive loss from filler particles in return baths and environmental stress cracking around press-fitted bushes. If the UH code behaves as a high-molar-mass PE-HD, the product should shift the abrasion and stress-crack resistance toward the PE-UHMW side while retaining easier machinability than PE 1000. However, the exact improvement cannot be claimed without a direct sand-slurry abrasion test under ISO 4649 or a taber abrasion test under ASTM D4060 using the product’s own certificate. Published data for this specific configuration is limited. Operators should monitor guide-rail clearance after the first 500 h of production; if the UH-sub-grade has a higher melt viscosity, recycled grind from edge trim may require a more powerful granulator with a screen size above 8 mm to avoid fines generation during reclaim.

    For polymer-lined steel tanks handling mixed aqueous and hydrocarbon phases, HDPE UH.429-01 can be specified only where the continuous phase remains aqueous. Prolonged contact with aromatic hydrocarbons, chlorinated solvents, or ketones causes swelling, softening, and loss of pressure-bearing capacity. In one documented failure pattern on a horizontal storage tank, a PE-HD liner subjected to condensed toluene vapour blistered and detached from the steel substrate; the retrofit used a different lining system. Published data for this specific product in mixed-phase hydrocarbon service is limited, so a chemical resistance declaration under ISO 175 should be requested from the supplier before finalizing the design.

    Comparing HDPE UH.429-01 to PE-UHMW, PP-C, and filled thermoplastics

    Relative to PE-UHMW, the UH-coded HDPE grade is expected to occupy an intermediate position in abrasion resistance and notched impact strength, assuming the designation represents a molecular-weight increase and not merely a colour code. PE-UHMW is processed primarily by compression moulding or ram extrusion and is specified where maximum sliding wear resistance is required; HDPE UH.429-01 remains within the high-density polyethylene family and may be more readily available in standard sheet formats. Exact placement between PE-HD and PE-UHMW requires the melt-flow ratio or solution viscosity data from the supplier, preferably under ISO 11542-2 for PE-UHMW or ISO 1133-1 for melt-processable PE-HD.

    Against copolymer polypropylene classified as PP-C under ISO 1873-2, HDPE UH.429-01 would generally show lower tensile modulus and lower upper service temperature in hot air, but superior environmental stress crack resistance and lower notch sensitivity in chilled aqueous service. Glass-filled polypropylene or glass-filled polyamide provides higher stiffness and lower thermal expansion, but introduces abrasive filler that accelerates tool wear and can create a harsher wear counterpart against stainless steel shafts. HDPE UH.429-01 should therefore be evaluated not as a stiffness substitute for filled thermoplastics, but as a low-moisture, chemically resistant bearing or guide material where deflection limits allow its lower modulus.

    When the application involves dry-running contact against stainless steel at surface pressure above 0.5 MPa, wear performance should be tested under the actual PV condition rather than inferred from material family alone. A block-on-ring test under ASTM G176 or a pin-on-disc test under ISO 7148-2 can provide comparative wear factors, but the values are highly dependent on counterface roughness and generated heat. Published data for this specific configuration is limited, and no universal wear coefficient should be assigned to the product without a controlled test.

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