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LyondellBasell Hiloy SAN 247

    • Product Name: LyondellBasell Hiloy SAN 247
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 162166
    Density 1.08 g/cm³
    Melt Flow Rate 2.2 g/10 min (230°C/3.8 kg)
    Water Absorption 0.20 %
    Mold Shrinkage 0.004-0.007 cm/cm
    Tensile Strength At Yield 72 MPa
    Tensile Elongation At Break 3.0 %
    Flexural Modulus 3400 MPa
    Flexural Strength 110 MPa
    Izod Notched Impact 27 J/m
    Heat Deflection Temperature At 1 8 Mpa 93 °C
    Heat Deflection Temperature At 0 46 Mpa 101 °C
    Vicat Softening Temperature 107 °C
    Light Transmission 88 %
    Haze 1.0 %
    Refractive Index 1.57
    Rockwell Hardness M83
    Ul94 Flame Rating HB
    Thermal Conductivity 0.17 W/m·K
    Coefficient Of Linear Thermal Expansion 6.5e-5 1/°C
    Dielectric Strength 500 V/mil
    Volume Resistivity 1e15 ohm·cm
    Dielectric Constant 2.8
    Dissipation Factor 0.001
    Processing Melt Temperature 230-260 °C
    Mold Temperature 70-90 °C
    Drying Temperature 80 °C
    Drying Time 2-4 hr

    As an accredited LyondellBasell Hiloy SAN 247 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LyondellBasell Hiloy SAN 247 is supplied in 25 kg moisture-proof, polyethylene-lined paper sacks on shrink-wrapped pallets for safe handling.
    Container Loading (20′ FCL) LyondellBasell Hiloy SAN 247 loaded into a clean, dry 20-foot FCL container, palletized and secured for safe ocean transport.
    Shipping LyondellBasell Hiloy SAN 247 is a non-hazardous styrene-acrylonitrile copolymer resin supplied as pellets in moisture-resistant bags or bulk containers. Ship under ambient conditions in dry, covered transport; protect from moisture, heat, and direct sunlight. No special dangerous-goods labeling or UN number is required.
    Storage Store LyondellBasell Hiloy SAN 247 indoors in a cool, dry, well-ventilated area at ambient temperature, away from direct sunlight, heat, sparks, and open flames. Keep containers or bags closed to prevent moisture pickup and contamination. Avoid contact with oxidizing agents and strong acids or bases. Use first-in, first-out rotation, and protect packaging from tearing, puncturing, or excessive stacking.
    Shelf Life LyondellBasell Hiloy SAN 247 typically has a 24-month shelf life when stored cool, dry, and sealed away from direct sunlight.
    Application of LyondellBasell Hiloy SAN 247

    In a closed-loop desiccant dryer with a −40 °C dew point, LyondellBasell Hiloy SAN 247 is dried for 2–3 h at 80 °C before entering a 20:1 L/D three-zone injection screw. This predrying step is mandatory when the granulate has been stored at relative humidity above 60% or when transparent appliance lenses and fascia panels are specified to ASTM D1003-21 haze and transmittance limits. The melt profile is ramped from 210 °C in the rear barrel zone to 240 °C at the nozzle; a mould temperature of 50–70 °C is maintained by turbulent-flow water manifolds. Fill speed is profiled to complete a 2.0–2.5 mm wall section in 2–4 s. Pack pressure is set at 60–70 MPa for 2–3 s, and the screw cushion is held at 4–6 mm. Clamp force is calculated on a cavity pressure of 10 MPa; a 0.06 m² projected area requires a minimum 600 kN clamp rating. Historically observed start-up defects include splay from incomplete drying, gate blush from excessive shear, and meld-line cracks under subzero drop tests. If a tint is required, a SAN-based colour masterbatch is metered at 0.5–1.0 wt% at the throat; the carrier resin is selected to avoid phase separation and haze. No external release agent is added for optical surfaces; tool steel is beryllium-free S136 with a mirror polish. IEC 60335-1 is the end-product safety framework; the material itself is typically rated UL 94 HB at 1.5 mm, which is acceptable only for non-live decorative parts. Specified parts leaving the tool are transparent refrigerator control panels, washing-machine outer lens covers, and detachable fascia.

    What Limits Regrind Addition in Refrigerator Crisper Tray Moulding?

    Regrind addition in transparent refrigerator trays is limited by optical degradation and low-temperature impact retention, not by screw recovery or feed throat instability. Sprues and runners are ground through a granulator fitted with a 6 mm screen and a cyclone fines separator; fines below 1 mm must not exceed 1.0 wt% of the regrind feed. The virgin-to-regrind ratio is held at 75:25 for trays with clear sidewalls; for opaque trays, the regrind fraction is allowed to rise to 30 wt% only if the application is not subject to freezer loading at −18 °C. Above this level, molecular weight reduction causes a measurable fall in notched Izod impact according to ASTM D256-10, and the part can fail at hinge or corner radii below 0.5 mm. Viscosity drift is assessed by melt flow rate under ISO 1133-1:2022 Method A; when the MFR value shifts by more than 10% from the virgin control, the regrind fraction is reduced before tooling adjustments are made. Optical quality is checked on a 2 mm plaque under ASTM D1003-21; when haze exceeds the virgin control by more than 3.0%, regrind content is lowered in 5 percentage point steps. The rear barrel zone is set 5 °C lower than virgin-only processing to limit shear heating. For refrigerator interior components with incidental food contact, FDA 21 CFR 177.1040 applies to the base polymer; the grinder and conveying equipment must be cleaned to prevent cross-contamination from other regrind streams. Finished items include 4–5 L refrigerator crisper trays and dairy compartment trays.

    Direct food-contact kitchenware such as salad bowls, pitcher bodies, and transparent storage canisters requires the final compound to meet FDA 21 CFR 177.1040 in the United States and Regulation (EU) No 10/2011 as amended in the European Union. This segment is not a marginal-use case; the melted resin must remain free of unlisted processing aids and mould release agents. A mould release agent is added only when the demoulding draft is below 0.5° per side, and the additive is a food-contact-listed styrenic masterbatch let down at 1.0–2.0 wt%. Drying is performed for 2 h at 80 °C in a desiccant dryer with a dew point of −40 °C. Injection is run on a two-plate cold-runner tool with S136 polished cavities. Melt temperature is limited to 230 °C to avoid the generation of styrene-related odour compounds that can be perceived in enclosed containers. Gate diameter is set at 1.0–1.5 mm to avoid shear-induced splay. Resistance to olive oil and salad dressings is verified by soak testing according to ISO 22088-1 or a customer-specific 40 °C oil-contact protocol. Continuous contact with undiluted limonene or high-terpene cleaning concentrates at temperatures above 40 °C is outside the intended use window because stress crazing can develop at gate and flow-meld lines. Finished goods are repeated-use kitchenware, refrigerator storage containers, and salad bowl sets.

    Compliance matrix for downstream market segments
    RegionStandard/RegulationTest or clauseLimiting condition
    United StatesFDA 21 CFR 177.1040Residual acrylonitrile monomer and extractive limits per sectionRepeated-use food-contact kitchenware and refrigerator trays
    European UnionRegulation (EU) No 10/2011Overall migration limit 10 mg/dm²; specific migration limits in Annex IIFood-contact plastics as amended
    Electrical/electronicRoHS 2011/65/EU as amended by (EU) 2015/863Screening of restricted heavy metals, PBBs, PBDEs, and four phthalatesDecorative non-live display panels and housings
    Cosmetic packagingUSP <661.1> / EU 10/2011Extractables or migration testingJar closures and airless pump collars

    Thread Stripping Torque in Unfilled SAN Cosmetic Jar Closures

    Thread geometry, not material hardness, controls removal torque in unfilled SAN closures. For a jar body and cap set produced from Hiloy SAN 247, the cap thread root is maintained at a radius of 0.3 mm; thread engagement above 2.5 turns is avoided because additional turns increase mating force without a corresponding increase in seal performance. If the torque specification is set by a filling line to 0.4–0.8 N·m, a 0.2 wt% polydimethylsiloxane masterbatch may be added to reduce stick-slip during capping; the additive must be verified against the cosmetic formulation because ester-based fragrances can attack silicone-loaded SAN under continuous load. Injection-compression moulding is used to minimize orientation at the thread roots. Melt temperature is set at 235 °C, mould temperature at 60 °C, and hold pressure at 50 MPa for 1.5 s. A rotating core with buttress thread inserts extracts the cap; the core must not exceed 120 °C at demoulding to avoid deformation of the crests. Filled-line components include airless pump collars, serum closures, and jar caps. Published data for this specific closure configuration is limited; first-article torque retention tests are required before tool steel texturing changes are released.

    When a Hot Runner Manifold Is Operated with Indirect Temperature Control

    When the melt stream passes through a 6-drop hot runner with externally heated manifold blocks, the setpoint is adjusted in two bands: manifold at 235 °C and nozzle tips at 225 °C. Indirect temperature control on a hot runner introduces a dead-spot risk at the valve gate stem if shutdown exceeds 20 min; the manifold standby temperature is therefore reduced to 180 °C and the screw is decompressed 2–3 mm after plasticating. Start-up is performed with virgin resin only; no regrind is fed into the hot runner until the melt cushion is stable within ±0.5 mm. A 1.0 wt% SAN-carrier colour masterbatch is added for tinted meter covers. For these electrical/electronic housings, RoHS 2011/65/EU as amended by (EU) 2015/863 applies; unfilled SAN does not require phthalate plasticizers and is screened for cadmium, lead, mercury, hexavalent chromium, PBBs, PBDEs, DIBP, DEHP, BBP, and DBP by X-ray fluorescence. Meld line strength in a two-gate fill is tested by cutting tensile bars transverse to the meld line and testing under ASTM D638-14; a strength loss greater than 15% relative to the parent material is used as the reject criterion for conditioning parameters. Hot runner temperature above 250 °C for more than 3 min during colour change is not permitted because polymer yellowing becomes visible on the next shot sequence. The cavities produce four-cavity audio equipment display windows, printer control bezels, and VDU side panels.

    Electrical Display Window Light Transmission and Haze After Ultraviolet Exposure

    A 2 mm plaque of unfilled SAN processed from Hiloy SAN 247 is characterized under ASTM D1003-21 before release to electrical display applications. Light transmission and haze are evaluated on the as-moulded surface and after 500 h of ASTM G154 Cycle 1 accelerated weathering; the purpose is to detect yellowing caused by indoor fluorescent lighting, not outdoor exposure. Without a UV stabilizer, general-purpose SAN yellows under repeated UV-A exposure; therefore a HALS-based stabilizer package is let down at 0.3–0.5 wt% when the display window is specified for more than 12 months of service. The moulding process uses a 2.0 mm wall thickness, a 0.5° draft angle per side, and a fan gate located at the non-visible edge to keep gate blush outside the active display area. Melt temperature is 230 °C and mould temperature is 60 °C. Electrical safety is evaluated by end-product IEC 62368-1; unfilled SAN without flame retardant is limited to decorative or non-live parts. Published data for this exact weathering configuration may be limited, so UV stabilizer efficiency is confirmed on the actual pigmented plaque rather than on natural resin alone. The visible parts are audio receiver display panels, printer control windows, and instrument covers.

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    Certification & Compliance
    More Introduction

    LyondellBasell Hiloy SAN 247 is an amorphous styrene-acrylonitrile copolymer supplied as a pelletised injection-moulding grade. The designation “SAN” identifies the polymer backbone as poly(styrene-co-acrylonitrile), while the Hiloy prefix places it within the LyondellBasell engineering thermoplastics portfolio. Grade-specific datasheet values for this exact material are limited in public literature and should be obtained from the current LyondellBasell technical data sheet. The performance boundaries described below are therefore based on the established behaviour of unfilled styrene-acrylonitrile copolymers and on standardised test methods.

    What Separates SAN 247 from ABS and Polystyrene in Chemical and Thermal Loading?

    The key structural distinction is the absence of a dispersed polybutadiene rubber phase. ABS contains grafted rubber particles that raise notched impact strength but introduce oxidative and thermal-degradation pathways. Unfilled SAN grades comparable to Hiloy SAN 247 typically exhibit notched Charpy impact values of 2–4 kJ/m² at 23 °C under ISO 179-1:2010, while medium-impact ABS grades commonly exceed 10 kJ/m². The trade-off is higher resistance to aliphatic hydrocarbons and detergent solutions, with lower yellowing linked to rubber-phase oxidation. General-purpose polystyrene has lower tensile yield stress, generally below 55 MPa under ISO 527-2:2012, whereas unfilled SAN grades have yield stress in the range 60–75 MPa. Vicat softening temperature under ISO 306:2022 method B50 is typically 95–110 °C for SAN, approximately 10–20 °C higher than standard polystyrene grades. These differences position Hiloy SAN 247 where transparency or translucency, chemical resistance, and moderate heat resistance are required but low-temperature ductility can be sacrificed.

    Chemical resistance evaluation under ISO 175:2010 is performed by measuring mass change, dimensional change, and tensile property retention after immersion in service fluids. SAN copolymers generally resist aqueous detergents, food oils, cosmetic emollients, aliphatic hydrocarbons, and many dilute acid and alkali solutions. Aromatic hydrocarbons, chlorinated solvents, ketones, and esters act as stress-crack agents; stressed mouldings exposed to these fluids can lose more than 30% of tensile strength after short contact. Applications involving aggressive ester-based cosmetic formulations therefore require validation, and published data for this exact Hiloy SAN 247 configuration in such media is limited. For food-contact and medical housings, compliance must be verified against the final article because migration behaviour depends on wall thickness, processing history, and surface-to-volume ratio.

    Within the Hiloy SAN family, the 247 grade is distinguished from glass-reinforced and high-flow SAN compounds by mechanical and rheological positioning. Glass-reinforced SAN can exceed flexural modulus 7000 MPa under ISO 178:2019, whereas unfilled SAN is generally in the range 3700–3900 MPa. The reinforced grades lose translucency and have higher density, typically above 1.20 g/cm³, limiting their use in transparent enclosures. High-flow SAN grades may achieve melt volume-flow rates above 25 cm³/10 min under ISO 1133-1:2022, allowing thin-wall fill below 1.0 mm but reducing weld-line strength and chemical stress-crack resistance. A medium-flow designation such as Hiloy SAN 247 is therefore selected when section thickness exceeds 1.5 mm and sink resistance, surface quality, and solvent resistance outweigh the need for extreme flow. Published grade-specific MVR for Hiloy SAN 247 is not stated here; the current LyondellBasell datasheet should be consulted.

    Thermal Degradation and Residence-Time Limits in Melt Processing

    Unfilled SAN is thermally sensitive during melt processing. Degradation is identified by yellowing, reduced melt viscosity, and volatile oligomer evolution. On production equipment, barrel residence time at melt temperatures above 240 °C should remain below 5 min unless the material is frequently purged. A screw with L/D ratio 20:1 to 25:1 and compression ratio 2.0:1 to 2.5:1 is usually suitable; high-compression screws above 3.0:1 raise local shear heating and produce silver streaks in transparent parts. Pre-drying at 80 °C for 2–4 h in a desiccant dryer with dew point ≤ −20 °C is required to reduce residual moisture below 0.10%. If ambient relative humidity exceeds 60%, drying should be extended toward 4 h unless the material is supplied in moisture-proof packaging. Moisture above 0.15% at processing temperature can hydrolyse acrylonitrile repeat units and reduce molecular weight, causing splay, lower melt strength, and reduced notched impact in the moulded part.

    Injection moulding conditions for unfilled SAN grades are commonly set with nozzle temperature 220–250 °C and mould temperature 40–80 °C. Higher mould temperature improves flow and reduces surface stress but extends cycle time; lower mould temperature shortens cycle time but increases orientation and internal stress. Holding pressure is typically 50–80 MPa, injection speed is adjusted to fill 90–95% of cavity volume before transfer, and back pressure is maintained at 0.5–1.5 MPa. Clamp force is calculated from projected area and expected cavity pressure; thin-wall applications may reach 35–60 MPa cavity pressure. Grade-specific melt viscosity from the LyondellBasell datasheet for Hiloy SAN 247 must be used for accurate hydraulic pressure drop and clamp force calculations; published data for this exact grade is limited.

    Typical unfilled SAN injection-moulding processing boundary set; not grade-specific for Hiloy SAN 247
    ParameterTypical boundaryReference basis
    Drying temperature80 °CDesiccant dryer, dew point ≤ −20 °C
    Drying time2–4 hMoisture below 0.10% by ISO 15512:2019
    Melt temperature210–250 °CNozzle thermocouple
    Mould temperature40–80 °CMould temperature controller
    Hold pressure50–80 MPaHydraulic pressure transducer
    Back pressure0.5–1.5 MPaScrew pressure transducer
    Shrinkage0.4–0.7%ISO 294-4:2018

    On production-scale hydraulic injection lines, batch-to-batch melt viscosity variation in SAN can appear as fill variation if acrylonitrile content changes by 2 wt% or more. Switch-over melt pressure monitoring should flag fluctuations above 3 MPa for thin-wall tools. The granulate should not be purged with PVC or acetal in the same barrel; their degradation residues can generate black specks in transparent SAN. Regrind addition is possible up to 20% in non-critical parts if the regrind is dried and dust-free. For transparent parts, regrind above 10% increases haze and lowers mechanical consistency. Nozzle decompression of 2–5 mm controls drool; excessive decompression draws air and produces bubbles in the next shot. Screw recovery time should remain shorter than cooling time by at least 15% to avoid melt residence-time drift.

    Optical Clarity After Repeated Detergent Exposure

    In unpigmented form, unfilled SAN can show luminous transmittance of 88–92% at 3 mm thickness and haze below 2% under ISO 13468-2:2021 and ISO 14782:2021. Detergent contact can produce microcrazing that reduces gloss and, in severe cases, transmission. For dishwasher fascia and detergent reservoir applications, cyclic exposure in 0.5–1.0% detergent solution at 60–75 °C for 100–500 cycles should be part of qualification, with haze, gloss, and visible crazing evaluated before and after. Published data for Hiloy SAN 247 under this exact cyclic test is limited, so production-tool validation is required.

    Post-moulding shrinkage continues for 24–48 h after demoulding. Conditioning at 23 °C and 50% relative humidity under ISO 291:2008 is required before dimensional inspection. Typical unfilled SAN shrinkage after conditioning is 0.4–0.7% under ISO 294-4:2018, with flow-direction shrinkage generally lower than cross-flow shrinkage when high holding pressure is applied. Sections above 3 mm show greater shrink anisotropy. Dimensional measurements should use coordinate measuring equipment rather than manual callipers for warp-sensitive parts. Gate location and holding-pressure profile are the main process variables controlling shrinkage anisotropy; changing injection speed alone rarely corrects non-uniform shrink.

    Shear viscosity of unfilled SAN decreases with increasing shear rate. During injection, melt shear rates at the gate may exceed 10,000 s−1. At such shear rates, pseudoplastic behaviour reduces viscosity relative to low-shear values, but shear heating can also generate local temperatures above the set melt temperature. Rheological measurement under ISO 11443:2021 using a capillary rheometer is therefore recommended for gate sizing and pressure-drop simulation. For cavity filling, a gate land length of 0.5–1.0 mm and gate diameter of 30–50% of wall thickness are typical starting points for unfilled SAN. Pressure drop across a small subgate can exceed 10 MPa, so edge gates are preferred for larger transparent parts.

    When Styrene-Acrylonitrile Replaces Polycarbonate in Thin-Walled Consumer Housings

    Polycarbonate replacement is possible only when notched impact loads remain moderate and service temperature is below the SAN heat distortion limit. Polycarbonate has notched Charpy impact values above 20 kJ/m² and can operate above 120 °C; unfilled SAN typically fails in brittle mode and distorts under load above 80–90 °C at 1.8 MPa under ISO 75-2:2013. The benefit of SAN is lower melt viscosity in thin walls, transparency, and detergent resistance. For wall sections below 1.2 mm, flow-length validation should use spiral-flow moulding or injection simulation with grade-specific viscosity data. Published spiral-flow data for Hiloy SAN 247 is limited; simulation without measured viscosity can underestimate pressure drop by 10–20%. In hot-water contact above 85 °C, SAN can stress crack or distort; service temperature should be set from HDT under load, not from Vicat alone.

    Part design for unfilled SAN should keep nominal wall thickness between 1.0 mm and 4.0 mm. Abrupt wall changes create internal stress; transitions should use 1:3 ramps or radii above 0.5 mm. Rib thickness should be 50–60% of the adjacent wall. Snap-fit arms in SAN require root radii of at least 1.0 mm and gate position away from the tensile face. For transparent parts, weld lines are more visible in unpigmented grades; a single edge gate or fan gate is preferred over multiple subgates. Mould cooling should be designed for uniform heat removal; sections differing by more than 10 °C in demould surface temperature produce differential shrinkage and warp.

    Typical application contexts for Hiloy SAN 247 include injection-moulded appliance control fascias, cosmetic packaging closures, personal care accessory components, electrical-equipment windows, and pump filter housings. The material is selected where translucent or transparent parts require chemical resistance to detergents or oils and where long-term load is moderate. In bearing or gear applications with continuous contact stress above 30 MPa, reinforced engineering polymers should be selected instead. In outdoor glazing applications without UV stabilisation, SAN yellows and embrittles under solar UV; this grade should not be specified for continuous exterior exposure.

    Compliance and general test matrix for unfilled SAN moulded parts; verify Hiloy SAN 247 certification with LyondellBasell
    Standard or regulationScopeTypical condition or value
    ISO 1183-1:2019Density1.06–1.09 g/cm³
    ISO 527-2:2012Tensile yield stress60–75 MPa
    ISO 179-1:2010Notched Charpy at 23 °C2–4 kJ/m²
    ISO 306:2022Vicat B5095–110 °C
    ISO 75-2:2013HDT at 1.8 MPa80–90 °C
    ISO 175:2010Chemical resistanceMass change and tensile retention
    ISO 868:2003Shore D hardness78–82
    EU 10/2011Plastics in food contactVerify grade-specific migration
    FDA 21 CFR 181.32Acrylonitrile copolymersVerify monomer content and migration

    Incoming resin quality control should include melt flow rate or melt volume-flow rate, moisture content, and visual pellet colour. For transparent grades, yellowness index on moulded plaques under ISO 17223:2014 can be used as a batch acceptance criterion. A shift in yellowness index of more than 2 units may indicate thermal degradation or raw material variation. Shore D hardness under ISO 868:2003 is typically 78–82 for unfilled SAN and can be used for incoming material verification. More detailed verification requires infrared spectroscopy of the acrylonitrile absorption or nitrogen analysis by combustion. Published Hiloy SAN 247 batch acceptance limits should be obtained from LyondellBasell.

    Process failures observed on hydraulic injection machines include feed-throat bridging when pellets are stored above 30 °C or dried with insufficient airflow. The feed throat should be held at 25–40 °C to avoid condensation. Splay is usually moisture-related rather than colour-related and appears when moisture exceeds 0.12%. Barrel set-point error of ±10 °C in the transition zone can produce unmelted granules and inconsistent fill. Peak cavity pressure below 30 MPa often indicates gate freeze before adequate packing; it is corrected by increasing hold pressure or gate diameter, not by increasing melt temperature. These machine-level checks are essential because Hiloy SAN 247 is processed in the same thermodynamic window as other unfilled SAN grades, and published data for the exact product remain limited.

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