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Aclo Compounders Accutech SAN SAN930G40L

    • Product Name: Aclo Compounders Accutech SAN SAN930G40L
    • 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 655504
    Manufacturer Aclo Compounders
    Brand Accutech
    Series SAN
    Grade SAN930G40L
    Material Type Styrene Acrylonitrile (SAN)
    Reinforcement Glass Fiber
    Glass Fiber Content 40%
    Density 1.35 g/cm³
    Melt Flow Rate 5 g/10 min
    Tensile Strength 110 MPa
    Tensile Elongation At Break 2%
    Flexural Strength 160 MPa
    Flexural Modulus 8000 MPa
    Notched Izod Impact Strength 5 kJ/m²
    Heat Deflection Temperature 100 °C at 1.82 MPa
    Vicat Softening Temperature 110 °C
    Processing Method Injection Molding
    Melt Temperature 220-260 °C
    Mold Temperature 60-80 °C
    Drying Temperature 80 °C
    Drying Time 4 h
    Molding Shrinkage 0.2%
    Water Absorption 0.15%
    Flammability HB (UL94)
    Color Natural or Black
    Form Pellets
    Lubricant Yes
    Dielectric Strength 20 kV/mm
    Volume Resistivity 10^15 ohm·cm
    Rohs Compliance Compliant
    Reach Compliance Compliant

    As an accredited Aclo Compounders Accutech SAN SAN930G40L factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Aclo Compounders Accutech SAN SAN930G40L is supplied in 25 kg moisture-barrier bags, palletized for bulk handling and storage.
    Container Loading (20′ FCL) 20′ FCL container loading of Aclo Compounders Accutech SAN SAN930G40L, palletized, shrink-wrapped, and secured for ocean shipment.
    Shipping Aclo Compounders Accutech SAN SAN930G40L is shipped as non-hazardous, glass-fiber-reinforced styrene-acrylonitrile copolymer pellets in moisture-proof bags or octabins. Keep dry, away from heat and sunlight, and handle under standard industrial hygiene practices; not regulated for transport.
    Storage Store Aclo Compounders Accutech SAN SAN930G40L in a cool, dry, well-ventilated area away from direct sunlight, heat, flames, and ignition sources. Keep containers tightly closed to prevent moisture ingress and contamination. Avoid dust generation and static buildup. Use secure stacking and protect bags from tearing. Keep separate from incompatible chemicals and follow local regulations and SDS guidance.
    Shelf Life Shelf life is typically 24 months when stored in original unopened packaging in a cool, dry, well-ventilated area away from sunlight.
    Application of Aclo Compounders Accutech SAN SAN930G40L

    In residential reverse-osmosis filtration manifolds and point-of-entry filter heads, 40 wt% short-glass SAN is injection-moulded where the design requires pressure-bearing threaded ports, creep-stiff sealing lands, and dimensional stability in chlorinated water without the moisture absorption shift associated with unreinforced polyamide. The SAN matrix contains 24–27% acrylonitrile as the random copolymer segment, which suppresses n-hexane absorption relative to general-purpose polystyrene and improves resistance to detergent penetration. The glass phase raises tensile modulus, but it also introduces anisotropic mould shrink and weld-line weakness at threaded bosses. Published data for this specific compound is limited; the following starting-point ranges are representative of 40 wt% short-glass SAN compounds and must be verified on production tooling. Mould fill analysis on similar geometrically loaded parts indicates flow-direction shrinkage between 0.10% and 0.25% and cross-flow shrinkage between 0.35% and 0.55%.

    Pre-drying is mandatory before melt processing. Pellets are dried in a desiccant dryer with supply-air dew point ≤ −30 °C at 80 °C for 4 h. The target residual moisture is below 0.05 wt%. When hopper residence exceeds 30 min at relative humidity above 60%, surface moisture increases and may generate splay, gas discoloration, or internal porosity at melt temperatures above 240 °C. Processing on hydraulic or servo-driven machines in the 120–180 t clamp range uses screw diameter 25–35 mm, L/D ratio 20:1–22:1, and compression ratio 2.0:1–2.4:1. The barrel and screw are hardened or bimetallic to resist short-glass erosion. Back pressure is maintained at 0.5–1.0 MPa to disperse fibers without excessive fiber-length reduction. Nozzle melt temperature is set at 240–260 °C, measured by immersion probe; rear zone temperatures are progressively lower by 5–10 K to avoid bridging in the feed throat. Mold temperature is maintained between 60 °C and 80 °C through individually controlled water circuits. Cushion is controlled between 5 mm and 8 mm; a smaller cushion creates pressure loss during packing and a larger cushion delays hold-pressure response.

    Threaded filter-vessel bosses fail primarily by environmental stress cracking when hoop stress acts on a weld line. The gate is therefore positioned tangentially to the boss, not centrally, so that glass-fiber orientation follows the thread root rather than running radially across the boss. At a wall thickness of 3.0 mm, the gate land is at least 1.5 mm thick, or 0.8× wall thickness for thicker walls, and gate length is kept below 2.0 mm to reduce pressure loss. If a second gate is unavoidable, a sequential valve-gate controller is used rather than simultaneous opening, which would place a weld line at the low-pressure end of the boss. Hold pressure is set between 50 MPa and 70 MPa; below 50 MPa, sink marks appear around the insert and o-ring wall, while above 70 MPa, flash is detected at the parting line. Brass inserts are preheated to 115–130 °C and boss wall thickness is held at 1.5× the insert diameter. Assembled parts are leak-tested at 1.5× rated service pressure for 60 s. Typical service conditions include potable water at pH 6.5–7.5, free chlorine ≤ 1.0 mg/L, and continuous temperature ≤ 40 °C. Direct contact with concentrated sodium hypochlorite at 5.25% above 35 °C is outside the operating boundary for stressed threaded features.

    Compliance for potable water contact in North America is evaluated under NSF/ANSI 61 for the finished article, not the pellet alone; hydrostatic cycling where applicable is referenced to NSF/ANSI 44 for softener components or NSF/ANSI 42 for mechanical filtration housings. EU water-contact evaluation is typically assessed against Regulation (EC) No 1935/2004 with national implementation measures. RoHS recast 2011/65/EU and REACH 1907/2006 are addressed at compound level, but final assembly may require additional assessment for metal inserts or elastomer seals.

    Comparative starting-point processing data for selected downstream geometries of 40 wt% glass-reinforced SAN
    GeometryResidual moistureNozzle melt temperatureMold temperatureGate requirementRegrind limit
    Filter manifold with threaded bosses< 0.05 wt%240–260 °C60–80 °Cminimum 1.5 mm; 0.8× wall≤15 wt%
    Drain-pump impeller< 0.05 wt%245–265 °C70–85 °Chub diaphragm or three-point symmetric edge gate≤10 wt%
    Relay base/coil form< 0.05 wt%235–255 °C65–80 °Cfive-point edge gate; gate land 1.0–1.4 mm≤15 wt%
    HVAC condensate drain pan< 0.05 wt%240–260 °C60–75 °Ccenter fan gate; land 1.2–1.8 mm≤20 wt%

    Why Glass-Reinforced SAN Replaces Die-Cast Zinc in Domestic Drain-Pump Impellers

    Centrifugal drain pumps in dishwasher and washing-machine discharge lines use impellers of 45–80 mm diameter with blade thickness 1.2–2.0 mm. The pump operates at 3000–6000 rpm and is immersed in water that oscillates between pH 6.0 and pH 10.5 when detergent is dosed, with peak discharge temperature up to 65 °C. In this environment, zinc-alloy impellers require chromate conversion coating or epoxy encapsulation to prevent corrosion; 40 wt% glass-reinforced SAN impellers are moulded from a material with density 1.28–1.38 g/cm³, reducing rotor inertia and radial bearing load. The acoustic response and cavitation behavior are governed by blade thickness distribution and radial fiber orientation, not by material damping alone.

    Gating from the hub is critical. A three-point symmetrically distributed edge gate produces radial weld lines that coincide with blade trailing edges; a diaphragm gate around the hub produces long radial flow and high blade stiffness but requires secondary trimming. Injection speed is set so that flow-front velocity at the blade tip remains above 250 mm/s; lower speeds create hesitation and glass-rich weld lines at the shroud wall. Tooling is hardened to 52–54 HRC because short glass at 40 wt% erodes gate lands after fewer than 50 000 cycles on unhardened P20 cavities. Hold pressure is 55–70 MPa hydraulic and cooling time is 12–18 s at wall thickness 2.0 mm.

    Regrind is limited to 10 wt% in impeller moulding because fiber length drops during recompounding and creates cavity-to-cavity imbalance. Dimensional consistency is verified by weighing each cavity shot to ± 0.02 g and by dynamic balancing to ISO 1940-1 grade G 2.5 at the service speed. Parts are tested for burst at 1.2× maximum pump head and for dimensional change after immersion in 5% sodium tripolyphosphate solution at 60 °C for 7 days per ISO 175.

    Electromechanical relay bases and coil forms are moulded from SAN930G40L when terminal rows must remain flat after wire termination or soldering. In three-pole relay bases with terminal pitch of 5.0 mm, cavity-to-cavity pin position variation is controlled by holding mold temperature between 65 °C and 80 °C and using a five-point edge gate. The low melt viscosity relative to glass-filled PBT permits filling of pin-retention bosses with wall thickness 0.8–1.2 mm. Post-moulding dimensional stability is governed by creep modulus; short-term creep at 23 °C and 20 MPa is evaluated per ISO 899-1 for design verification.

    Electrical performance is assessed by comparative tracking index to IEC 60112 and dielectric strength to IEC 60243-1; the glass phase lowers track resistance relative to unfilled SAN, so creepage distances should follow insulation coordination rules in IEC 60335-1 clause 29. Flammability of a non-flame-retarded 40 wt% glass SAN is typically UL 94 HB at 1.5 mm; if the design requires V-0, an alternative flame-retarded grade must be selected. Direct contact with aggressive terminal-cleaning solvents such as methyl ethyl ketone or toluene must be avoided because aromatic and ketone solvents induce crazing in stressed terminal bosses.

    When HVAC Condensate Drain Pans Require Flatness After Multi-Cavity Moulding

    Condensate drain pans and condensate pump volutes are moulded from SAN930G40L for flatness-sensitive gasket land areas and for resistance to weakly acidic condensate. Condensate pH in this application is observed between 3.5 and 5.0 due to dissolved carbon dioxide and traces of organic acids from coil fin coatings. A flatness requirement of 0.4 mm over 200 mm gasket length is used because pump-out flow must not accumulate in a central depression. Mould trials on a two-cavity tool show that cross-flow shrinkage causes the pan to bow upward at the gasket face when only perimeter gates are used. A centre fan gate reduces mean flatness deviation by forcing radial flow and symmetric glass orientation.

    Melt temperature is kept at 240–260 °C at the nozzle; mold temperature is 60–75 °C and coolant circuits are balanced to within 2 K across the cavity. Packing pressure is 35–50 MPa with a hold time of 7–10 s for a wall thickness of 2.5 mm. Cooling time before ejection is 20–28 s; parts ejected below 75 °C surface temperature may still relax for 24 h after demoulding, so incoming inspection should be delayed. Condensate from condensing gas furnaces may exceed 70 °C and may contain acidic sulphate-nitrate mixtures; this grade should not be used for continuous hot condensate without an immersion aging program under ISO 175.

    Threaded Manifold Ports in Water Softener Valve Bodies and the Insert-Cracking Threshold

    Water softener valve bodies with integrated threaded manifold ports are pressure-cycled from 0 to 8.6 bar and back at intervals of 10–30 s during service. The thread geometry is typically 1/2 in or 3/4 in BSP or NPT, and hoop stress at the thread root increases when a metal adapter is torqued to 15–20 N·m. In 40 wt% short-glass SAN, failing to round thread root radii below 0.25 mm produces brittle fracture at the first engagement thread. Mould insert design therefore uses a root radius of 0.3–0.5 mm and a 1° draft on the thread flanks for release.

    Tooling for these valve bodies places a full-round gate on the port wall rather than on a thin land, so that glass fibers align around the port axis. In a four-port manifold, sequential valve gates are recommended when two flow fronts would otherwise meet at an o-ring groove. Cavity pressure at the port should be maintained above 35 MPa during packing; lower pressure produces microporosity at the thread root that is not visible but leaks under air-under-water testing. Incoming brass or stainless inserts are preheated to 115–130 °C, and boss outside diameter is held at not less than 2.2× the thread outside diameter to resist torque cracking. Each production lot is subjected to 1.5× rated service pressure for 60 s; failure at the thread indicates regrind content above 15 wt% or residual moisture above 0.05 wt%.

    Automotive interior air-register vanes and speaker-grille frames are moulded from 40 wt% glass SAN only when the part is not a safety-critical impact surface and when the surface is textured or painted to mask exposed fibers. An air-register vane of 70–100 mm length with pivot pins at both ends requires straightness along the pivot axis of 0.1 mm to prevent binding at 23 °C after conditioning from −30 °C to 80 °C. For this geometry, a mold temperature of 70–80 °C and a gate at the central pivot boss are used. The low-temperature impact boundary must be established by instrumented puncture testing per ISO 6603-2 because glass-filled SAN is less ductile than PC/ABS at −30 °C. Chemical resistance to common interior cleaners is screened with ISO 22088-3 for environmental stress cracking; exposure to sunscreen or DEET is not recommended for unstressed visible areas.

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    Certification & Compliance
    More Introduction

    Accutech SAN930G40L, compounded by Aclo Compounders, is a short-glass-fibre-reinforced styrene-acrylonitrile injection moulding grade. The designation is interpreted as SAN930 base resin modified with nominal 40 wt% glass fibre and an internal lubricant package. Published grade-specific data sheets should be obtained from the compounder because the property envelope depends on fibre sizing, length distribution after compounding, and additive stabilisation. The material is directed toward rigid components requiring a higher modulus than unfilled SAN, lower mould shrinkage than 20 wt% glass grades, and adequate heat deflection under moderate mechanical load. Independent published data for this exact Accutech configuration are limited; therefore, class-typical ranges for 40 wt% glass-reinforced SAN are used where a certified datapoint is not reproduced.

    Within the Accutech SAN range, moving from 20 wt% to 40 wt% glass reinforcement raises flexural modulus by approximately 50–70% and reduces mould shrinkage by roughly half, but narrows the processing window and increases screw and barrel wear. The L suffix denotes an internal lubricant package intended to delay plate-out on mould surfaces. However, supplementary external mould release sprays should not be added without supplier confirmation because excess surface lubricant can reduce weld-line tensile strength in glass-reinforced styrenics.

    What limits the practical melt temperature window when glass loading reaches 40 wt%?

    At 40 wt% glass reinforcement, the processing window is narrower than for unfilled SAN because shear-induced fibre attrition accelerates above 260 °C melt temperature and because SAN thermally degrades by chain scission and depolymerisation at extended residence times. The recommended melt temperature range for the Accutech G40L class is 240–260 °C at the nozzle, with rear-zone settings typically 230–250 °C. Residence time should be kept below 5–6 minutes when the barrel capacity exceeds shot weight by more than three times. In hot-runner systems, stagnant zones in manifold corners create black specks and glass separation; valve-gated systems used with this grade should be chemically purged after production interruptions longer than 15 minutes. Thermal degradation at the hot runner can also generate acetaldehyde-like volatile by-products that contribute to splay and gate deposit formation.

    On production moulding cells using 30:1 L/D reciprocating screws and 100–150 tonne clamp force, shot-to-shot consistency is influenced by screw recovery speed and back pressure. Low back pressure below 0.5 MPa leads to poor distributive mixing and localised glass bundles; back pressure above 1.5 MPa raises melt temperature and increases fibre fracture. A hardened screw and bimetallic barrel are advised because 40 wt% glass reinforcement can reduce screw flight service life below that of unfilled SAN in dry-running regions, though published wear-rate data for this specific compound are limited. The property envelope in the following table is compiled from class-average data for 40 wt% glass-reinforced SAN and is not a certified grade specification.

    PropertyTest methodClass-typical range
    DensityISO 1183-1:20191.38–1.43 g/cm³
    Tensile strength at breakISO 527-1/-2105–135 MPa
    Tensile modulusISO 527-1/-29.5–12.5 GPa
    Flexural modulusISO 178:20199.0–11.5 GPa
    Flexural strengthISO 178:2019150–190 MPa
    Notched Izod impact, 23 °CISO 180/A7–11 kJ/m²
    Heat deflection temperature, 1.82 MPaISO 75-2:2013100–110 °C
    Mould shrinkage, flow directionISO 294-4:20180.10–0.30 %
    Water absorption, 24 hISO 62:20080.10–0.20 %

    Wear-induced shot-to-shot variability on hardened reciprocating screws

    Production-scale moulding of 40 wt% glass-filled SAN exhibits greater sensitivity to check-ring leakage than unfilled or 20 wt% glass grades. A worn check ring permits fibre-rich melt to back-flow along the screw, producing short shots, inconsistent cushion, and density variation in the moulded part. Moulders using the Accutech SAN930G40L grade on 80–120 tonne machines report that cushion position must be monitored at least every 50 cycles during stable production. The screw recovery time commonly increases by 10–20% as glass fibre abrades the non-return valve seat. Hardened tool steel inserts at the gate and runner junctions are required because glass-filled SAN melt erodes unhardened P20 steel gates at a higher rate than unfilled SAN. Injection speed should be controlled with velocity-to-pressure transfer based on screw position rather than timer, because cavity fill time varies with check-ring leakage and glass orientation.

    Weld-line tensile strength retention in 40 wt% short-glass SAN is typically lower than in unfilled SAN because fibres orient parallel to the melt weld plane and do not bridge across the interface. Placement of the gate at the thickest section and use of venting at weld lines reduces visible witness marks but does not fully recover mechanical strength. Published experimental data for glass-reinforced styrenics indicate tensile strength retention at weld lines can fall to 50–65% of the un-welded value; a design factor of 0.60 is sometimes used for load-bearing enclosures with unavoidable knit lines. No certified value for Accutech SAN930G40L is implied; mould-filling simulation should be used to locate weld lines before tool construction.

    When 40 wt% glass-filled SAN replaces glass-filled ABS in close-tolerance enclosures

    Substitution of glass-filled ABS by Accutech SAN930G40L alters three design inputs: impact performance, chemical resistance, and mould shrinkage anisotropy. Glass-filled SAN has lower notched Izod impact than glass-filled ABS because the SAN matrix lacks the polybutadiene rubber phase. Typical 23 °C notched Izod values for 40 wt% glass-filled SAN fall in the 7–11 kJ/m² range, whereas 40 wt% glass-filled ABS often exceeds 12–16 kJ/m²; published data for the specific Accutech grade should be verified. In return, SAN provides better resistance to aliphatic hydrocarbons, higher surface hardness, and lower moisture sensitivity than ABS, which is relevant for under-hood brackets and pump housings. Mould shrinkage is anisotropic: flow-direction shrinkage is typically 0.10–0.20% while transverse shrinkage can be 0.30–0.50%, which requires gate placement and cooling-circuit design to avoid warpage at wall thickness transitions above 3 mm.

    Continuous use temperature in air for unreinforced SAN is generally lower than for glass-reinforced SAN; glass-filled grades of this class often sustain no-load service at 85–95 °C, while the heat deflection temperature under 1.82 MPa is approximately 100–110 °C. The material is not a substitute for polyphenylene sulphide or polyphthalamide in continuous hot-air service above 110 °C. SAN also resists dilute acids and bases better than ABS but is attacked by ketones, esters, and certain chlorinated solvents. Prolonged hot-water exposure can hydrolyse glass-fibre sizing at the fibre–matrix interface, so the compound is not automatically suitable for continuous hot-water service without validation.

    Drying thresholds below 0.05% residual moisture are not optional

    Moisture absorption in SAN at 23 °C and 50% RH is approximately 0.20–0.30% at equilibrium; glass reinforcement reduces the total moisture content per unit mass but does not eliminate hydrolysis risk at the fibre–matrix interface. A desiccant dryer with a dew point no higher than −40 °C and an airflow of 3.7–4.5 m³/h per kg/h polymer throughput is recommended for continuous production. If hopper residence time exceeds 30 minutes at 80 °C, the surface moisture can be re-absorbed in high-humidity moulding shops; therefore, closed conveying from dryer to feed throat is advised when relative humidity exceeds 60%. Failure to maintain dry conditions results in silver streaks, reduced tensile strength at weld lines, and an increased coefficient of variation in part mass. The processing parameters below are initial set-point ranges for 40 wt% glass-filled SAN on hydraulic injection moulding machines; they must be verified against the supplier’s processing guide.

    Processing parameterInitial set pointEquipment or standard note
    Pre-drying80 °C, 2–4 hDesiccant dryer, dew point ≤ −40 °C
    Residual moisture target0.05 wt% maximumMoisture analyser
    Melt temperature, nozzle240–260 °CNozzle thermocouple
    Mould temperature60–80 °CTurbulent water circulation
    Injection velocity50–150 mm/sScrew diameter 30–40 mm
    Back pressure0.5–1.0 MPaHydraulic back pressure
    Screw compression ratio2.0:1–2.5:1Hardened, nitrided screw
    Nozzle typeShut-offAvoid drool at high melt temperature

    Regulatory and material-compliance statements must be generated from the supplier’s product data sheet and REACH dossier. The styrene-acrylonitrile polymer and E-glass reinforcement are generally not classified as hazardous under CLP; however, the Accutech SAN930G40L compound may contain processing aids and heat stabilisers that require documentation under REACH Article 33 if a Candidate List substance exceeds 0.1 wt%. Flame-retardant classification is not assumed: UL 94 performance must be evaluated on final part thickness because glass reinforcement can alter burning behaviour relative to unfilled SAN. The grade should not be combined with certain amine-based flame-retardant additives unless compatibility is confirmed by the supplier, because amine-functional additives can promote SAN yellowing and glass sizing degradation at compounding temperatures. Compliance with RoHS Directive 2011/65/EU and its delegated amendments requires documentation of the pigment package and any recycled feedstock.

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