| HS Code | 703889 |
| Productname | Lotte Chemical ABS HR-5300 |
| Polymertype | Acrylonitrile Butadiene Styrene (ABS), heat-resistant grade |
| Density | 1.05 g/cm3 |
| Meltflowrate | 6 g/10 min (220 °C/10 kg) |
| Tensilestrength | 47 MPa |
| Elongationatbreak | 20% |
| Flexuralstrength | 75 MPa |
| Flexuralmodulus | 2300 MPa |
| Izodimpactstrengthnotched | 15 kJ/m2 (23 °C) |
| Rockwellhardness | 105 (R-scale) |
| Heatdeflectiontemperature | 95 °C (1.82 MPa) |
| Vicatsofteningtemperature | 105 °C |
| Flammabilityrating | UL 94 HB |
| Moldingshrinkage | 0.4–0.6% |
As an accredited Lotte Chemical ABS HR-5300 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Lotte Chemical ABS HR-5300 is packaged in 25 kg moisture-resistant bags, supplied on pallets for industrial handling. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with 25 kg bags of Lotte Chemical ABS HR-5300 resin, palletized, shrink-wrapped, and securely braced for export. |
| Shipping | Shipping description: Lotte Chemical ABS HR-5300 is supplied as ABS resin pellets in 25 kg bags or jumbo bags. It is non-hazardous, not UN-regulated, and should be transported in dry, covered containers/trucks away from moisture, direct sunlight, and excessive heat. Avoid bag damage and static buildup. |
| Storage | Store Lotte Chemical ABS HR-5300 in a cool, dry, well-ventilated warehouse, protected from direct sunlight, heat, flames, and strong oxidizers. Keep it in original sealed packaging on pallets, avoiding moisture, contamination, UV exposure, and excessive stacking. Maintain moderate temperature and humidity, practice first-in/first-out rotation, and follow the SDS and local storage regulations. |
| Shelf Life | Typically 24 months when stored in original sealed packaging under dry, cool, well-ventilated conditions away from direct sunlight. |
Competitive Lotte Chemical ABS HR-5300 prices that fit your budget—flexible terms and customized quotes for every order.
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Lotte Chemical ABS HR-5300 is a high-heat acrylonitrile-butadiene-styrene terpolymer supplied as pelletized feed for injection molding and, with adequate screw design, selected profile extrusion. The grade is positioned in the high-heat ABS subset rather than the high-impact or electroplating subset: the continuous styrene-acrylonitrile matrix is formulated to shift the glass transition and heat deflection response upward, while the dispersed polybutadiene phase is retained at a level that provides ambient notch resistance but not low-temperature ductility. Table 1 lists representative production-control typicals compiled from supplier technical literature using ISO specimen preparation and conditioning under ISO 291:2008. These values should be confirmed against lot-specific certificates of analysis because production site adjustments can move individual lots within the supplier’s specification window.
| Property | Value | Test method | Condition |
|---|---|---|---|
| Density | 1.05 g/cm³ | ISO 1183-1:2019 | 23 °C |
| Melt mass-flow rate | 4.5 g/10 min | ISO 1133-1:2022 | 220 °C, 10 kg |
| Tensile yield strength | 45 MPa | ISO 527-2:2012 | 50 mm/min |
| Elongation at break | 10% | ISO 527-2:2012 | 50 mm/min |
| Flexural modulus | 2,300 MPa | ISO 178:2019 | 2 mm/min |
| Flexural strength | 68 MPa | ISO 178:2019 | 2 mm/min |
| Notched Izod impact strength | 24 kJ/m² | ISO 180/1A:2019 | 23 °C |
| Notched Izod impact strength | 8 kJ/m² | ISO 180/1A:2019 | -30 °C |
| Vicat softening temperature | 111 °C | ISO 306:2013 | B50, 50 N |
| Heat deflection temperature | 104 °C | ISO 75-2:2013 | 1.80 MPa, annealed |
Because the grade is designed for elevated-temperature dimensional stability rather than maximum flow length, its melt mass-flow rate is lower than that of high-flow ABS. This places HR-5300 in a processing envelope where barrel temperature, screw recovery, and mold temperature must be managed as a single thermomechanical system. Pre-drying in a desiccant dryer at 80 °C to 90 °C for 3–4 h is required before processing when the resin has been exposed to ambient relative humidity above 60% RH; target residual moisture is below 0.02 wt% when determined by ISO 15512:2019. Failure to maintain this moisture threshold produces silver streaking at the gate and reduces tensile yield strength under ISO 527-2:2012 because hydrolytic chain scission of the SAN continuous phase occurs during melt residence.
The injection molding cycle is rate-limited by cooling time in thick sections and by screw recovery in multicavity tools. On a reciprocating-screw machine with a general-purpose 18:1 to 22:1 L/D screw and a compression ratio of 2.2:1 to 2.6:1, barrel set points from rear to nozzle are typically 210 °C, 230 °C, 240 °C, 245 °C, and 245 °C, yielding an air-shot melt temperature of 235–250 °C. Back pressure is maintained at 5–10 bar hydraulic, and screw speed is held between 60 rpm and 120 rpm for a 45 mm diameter screw. Higher screw speeds increase shear heating and may produce local degradation at the non-return valve if wear has opened a clear back-leakage path.
Mold temperature should be held at 60–80 °C for appearance components. The higher end of this range improves surface gloss and reduces flow-line visibility, but it increases cooling time by 3–5 s for a 2.0 mm wall section. For a full-round cold runner in a 2.0 mm wall part, runner diameters below 6.0 mm are not recommended when the flow length exceeds 80 mm because pressure loss through the runner can exceed 25 MPa before the gate. In hot-runner systems, manifold temperature should be limited to 230–240 °C; hot-runner drops may be set 10–15 °C warmer than the nozzle to compensate for heat loss without exposing the melt to prolonged temperatures above 250 °C.
Residence time above 5 min at melt temperature degrades the polybutadiene phase and shifts natural color toward yellow. On a 1,200 kN clamp injection molding machine with a valve-gated hot-runner tool, production-scale troubleshooting has identified gas-generated black specks after 4–6 h of continuous cycling when a shut-off valve seat leaked and allowed polymer to stagnate at the stem base. In such cases, the corrective action is to reduce the manifold set point to the lower end of the processing window and verify valve stroke before increasing back pressure.
Because the high-heat SAN continuous phase increases melt viscosity relative to medium-flow ABS, pressure loss in thin-wall tools becomes coupled to screw recovery and gate freeze. Components with wall sections below 1.2 mm are generally outside the recommended flow-length window unless flow simulation using the supplier’s viscosity model confirms that screw-tip pressure remains below the available machine specific injection pressure. For a 1.5 mm wall electronic enclosure, screw-tip injection pressure is commonly 80–120 MPa, depending on gate geometry and hot-runner balance. Hot-runner manifolds should be set to 230–240 °C, with valve-gate drops set 10–15 °C warmer than the machine nozzle.
Gate freeze occurs earlier than in high-flow ABS because the solidification front advances rapidly once the wall temperature drops below the heat deflection temperature. For a rectangular edge gate of 1.0 mm depth, the effective packing window can be shortened by 15–25% relative to a medium-flow ABS with a Vicat softening temperature below 95 °C; hold-pressure time should therefore be established by weight stabilization rather than by analogy to unfilled general-purpose ABS. Melt-front velocities above 150–200 mm/s may induce jetting in multi-gate housings and reduce weld-line strength. Published data for the specific configuration of a sequential valve-gate system delivering hot-runner melt to a thin-wall automotive trim carrier is limited, so mold trials are required.
Thermal stability in the barrel is governed by temperature and residence time, not by shear alone. Capillary rheometry at 240 °C shows the pseudoplastic response typical of ABS: apparent viscosity decreases from approximately 1,000 Pa·s at 100 s⁻¹ to below 200 Pa·s at 1,000 s⁻¹. This shear-thinning characteristic permits filling of moderate flow-length sections at acceptable pressure, but it does not cancel the requirement for a stable cushion. A cushion variation of ±2 mm during production indicates inconsistent plastication or non-return valve wear and should be corrected before dimensional variation is transferred to the part.
Thermogravimetric analysis of high-heat ABS under nitrogen typically shows decomposition onset above 280 °C; yellowing, however, begins earlier because the polybutadiene phase is oxidatively sensitive. Therefore the nozzle melt temperature should not exceed 250 °C, and any barrel residence distribution that retains 15% of material beyond 5 min is sufficient to create visible color shift. Amine-based mold release agents and certain amine-containing purging compounds are incompatible with this chemistry because they accelerate thermo-oxidative degradation at processing temperature; purging with an unpigmented ABS or a dedicated ABS purging compound is preferred.
The coefficient of linear thermal expansion for high-heat ABS is commonly 70–80 × 10⁻⁶ K⁻¹ per ISO 11359-2:1999. A mold-temperature variation of ±10 °C across a cavity can therefore shift a 150 mm critical dimension by 0.05–0.10 mm through differential post-mold shrinkage. If the component is to be painted or plated, the tool surface temperature should be held in a narrower band because the primary surface defect in this amorphous ABS is shrinkage-induced gloss variation rather than crystalline spherulite growth.
Compared with lower-heat ABS grades, HR-5300 is selected for components exposed to intermittent heat such as automotive interior trim near HVAC outlets, microwave oven door frames, electric rice cooker lids, and heater housings. The governing property in these applications is retention of modulus and dimensions when the part reaches surface temperatures of 85–95 °C under low external load. The Vicat softening temperature of the grade, measured by ISO 306:2013 method B50, is approximately 10–15 K above that of general-purpose ABS at equivalent rubber content, reducing deformation under contact with hot air and heating elements. This advantage comes at the cost of lower flow; for thin-wall parts with flow-length-to-thickness ratios above 120:1, high-flow grades may be required despite lower heat resistance.
Notched Izod impact at 23 °C is adequate for components not subjected to sub-ambient abuse; however, at -30 °C the value drops by more than half. This restricts use in exterior automotive parts exposed to winter impact. Where low-temperature ductility is the governing failure mode, high-impact ABS or an ABS-polycarbonate alloy should be selected. HR-5300 is not formulated as an electroplating grade; an etch line must be validated before plating because polybutadiene particle size and distribution control adhesion in the etched surface layer. Applications requiring a UL 94 V-0 listing at 1.5 mm should use a flame-retardant ABS grade rather than this product, which is not positioned as a flame-retardant system.
Production lots that incorporate regrind above 20 wt% should be restricted to non-appearance structural components unless optical inspection and melt flow testing confirm that the blend remains within the supplier’s original melt mass-flow rate control window. Repeated heat histories reduce notched Izod impact by 5–15% per heat cycle, with the larger effect at -30 °C than at 23 °C. Regrind that contains fines below 0.5 mm particle size can also separate in the hopper and produce non-uniform feeding; a gravimetric blender is preferred over volumetric blending when regrind content exceeds 10 wt%.
For a component weighing 250 g, injection speed should be profiled to hold velocity-controlled filling until 90–95% of shot volume is reached, then switch to pressure-controlled packing at 60–80% of the filling pressure. Hold pressure time is set by gate freeze rather than part weight; gate freeze can be identified by part-weight stabilization after 0.3–0.5 s increments in hold time. Average cavity pressure during packing in this grade is typically 35–45 MPa. A tool with a projected area of 500 cm² therefore requires a clamp force of 175–225 metric tons. Exceeding this cavity pressure range does not improve sink-mark resistance but can flash the parting line on presses with low clamp-force margins.
Residual polypropylene purging compound is incompatible with the ABS matrix and can cause delamination in post-mold painting. If a previous material was run on the machine, the barrel should be purged with an ABS-compatible compound and the nozzle tip inspected before resuming production with HR-5300.