In the production of pillar trim substrates and door panel carriers for passenger vehicle interiors, melt from Guangzhou Kingfa Science & Technology ABS Diastal-315 is introduced into a single-screw injection unit with an L/D ratio between
20:1 and
24:1 at barrel set points segmented from
210°C at the feed zone to
235°C at the metering zone. Pre-drying in a closed-loop desiccant dryer at
80°C to
85°C for
3 h to
4 h is mandatory to reduce residual moisture below
0.05% by weight, measured per Karl Fischer titration, because any free water above this threshold hydrolyzes the acrylonitrile-styrene continuous phase during plastication and produces silver streaking on visible Class A surfaces. Mold temperature is held between
60°C and
80°C using a pressurized water thermolator, not an oil unit, to maintain surface gloss replication on grained tool steel without exceeding the Vicat softening onset of the material during ejection. Injection pressure setpoints range from
80 MPa to
120 MPa with holding pressure applied at
50% to
70% of peak injection pressure for a duration tied to gate freeze time, typically
8 s to
15 s for wall thicknesses between
2.0 mm and
3.5 mm. Mold shrinkage is documented at
0.4% to
0.6% in the flow direction and
0.5% to
0.7% transverse per
ASTM D955-08, and toolmakers apply these anisotropy values separately to rib intersections and boss locations to prevent sink marks on visible regions. Regrind addition is capped at
15% by weight for non-visible substrates and excluded entirely from Class A components, because repeated thermal histories reduce the notched Izod impact retention of the polybutadiene rubber phase at sub-zero test temperatures. Volatile organic compound emissions from finished trim are tested according to
VDA 278 thermoplastic desorption analysis, with typical acceptance thresholds requiring total VOC below
100 µg/g and fogging condensate below
250 µg/g for German OEM specifications. Flammability of interior trim components is assessed per
ISO 3795/
FMVSS 302, where a horizontal burn rate of less than
100 mm/min is the maximum permitted for occupant compartment materials. Warpage after asymmetric cooling is corrected by adjusting coolant circuit layout within the mould rather than by altering melt temperature, because processing temperatures above
240°C accelerate thermo-oxidative scission of the butadiene segments and produce visible discoloration on unpainted surfaces. End products produced from this grade in the automotive interior sector include B-pillar lower trim, center console side panels, seat side shields, glove box outer skins, and door panel upper substrates where the balance of dimensional stability and moderate impact ductility matches the mechanical demands of non-airbag load paths.Antenna bracket and dashboard mounting plate production on vertical clamping machines introduces a different mechanical constraint set. Where underhood adjacent or high-solar-load interior positions demand continuous service temperatures approaching
90°C, the heat deflection temperature of ABS Diastal-315 under a
1.8 MPa flexural load is evaluated per
ISO 75-2/A methodology, with grade-specific values to be confirmed against the manufacturer datasheet. Published data for this specific configuration is limited, and tooling decisions should incorporate a safety margin of not less than
15°C between the expected continuous service temperature and the measured HDT. Ultrasonic welding of mounting bosses to polycarbonate counterparts is performed at frequencies of
20 kHz with weld amplitudes between
20 µm and
35 µm, because the ABS surface does not require plasma treatment prior to energy director collapse, unlike semicrystalline polyolefin substrates. Continuous load-bearing plastic fasteners in instrument panel substructures are designed with a creep modulus derived from
ISO 899-2 flexural creep testing, and the permissible long-term deflection is limited to
1.0 mm at a distance of
100 mm from the fixation point after
1000 h at
60°C for passenger-side knee bolster attachment zones.
What Processing Window Sustains Impact Strength in White Goods Components?
Washing machine fascia panels, dryer door frames, and refrigerator end-cap assemblies are injection moulded from ABS Diastal-315 on hydraulic or hybrid toggle machines with clamp forces ranging from
500 t to
1600 t depending on the projected part area. The critical processing conflict in white goods applications arises from the competing demands of high melt fluidity for thin-wall filling and minimal residence time to preserve notched Izod impact energy. Melt temperature is maintained between
220°C and
245°C at the nozzle, with a maximum cumulative residence time in the barrel of
5 min at
240°C, beyond which the rubber phase undergoes thermally induced crosslinking and the tensile elongation at break drops by more than
30% relative to virgin material, as measured per
ISO 527-2. A barrel residence time exceeding
8 min at
240°C produces a measurable reduction in notched Izod impact strength from typical injection-grade ABS baseline values in the range of
15 kJ/m² to
25 kJ/m² per
ISO 180/1A, a property cliff-edge that manifests as brittle corner fractures during drop testing of finished appliance housings from
1.0 m height at
-20°C per internal OEM specifications aligned with
IEC 60068-2-75 mechanical shock test methodology. Hot runner manifold temperatures are set
10°C to
20°C above nozzle melt temperature but must not exceed
260°C, because thermal degradation in the hot runner channel produces carbonized deposits that detach periodically and cause black speck contamination in light-colored fascia panels. Pre-drying is executed at
85°C for
3 h to
4 h using a desiccant dryer with a dew point of
-40°C or lower, and the drying hopper inlet air flow rate is sized at
3.7 m³/h per
kg/h of material throughput to maintain homogeneous moisture removal across the bed. Compliance for household appliances requires conformity with
IEC 60335-1 for general safety,
UL 94 HB flammability classification for non-enclosure cosmetic parts, and REACH Annex XVII restrictions for specific phthalate plasticizers and polycyclic aromatic hydrocarbons in accessible components. Gloss consistency across high-visibility control panels is governed by cavity-to-cavity temperature uniformity within
±3°C, achieved through conformal cooling channels in the core insert rather than conventional drilled straight-line circuits. End products in this downstream segment include washing machine top panels, dryer door rings, refrigerator air duct housings, vacuum cleaner motor shrouds, and dishwasher control console surrounds.When post-mould dimensional verification requires a total tolerance window of
±0.15 mm across a
350 mm span, the process window is narrowed further by the interaction between packing pressure decay rate and part mass consistency. Holding pressure is stepped down over
6 s to
12 s in two stages: an initial stage at
60% of peak injection pressure for gate sealing, followed by a reduced stage at
30% to prevent overpacking-induced stress that causes time-dependent warpage after
48 h at
23°C and
50% relative humidity. Screw rotation speed is limited to
40 rpm to
80 rpm for a
50 mm diameter metering section, generating shear heating that supplements barrel conduction without exceeding material degradation limits. Back pressure is set between
5 bar and
15 bar to densify the melt cushion and stabilize shot-to-shot fill variation below
0.3% of total shot weight. Gate dimensions for direct sprue-gated fascia panels are specified with a minimum diameter of
1.5 mm to prevent jetting, while sub-gate diameters below
0.8 mm are avoided because the resulting shear rate exceeds
20,000 s⁻¹ and locally degrades the butadiene phase at the gate land.
Pipe Extrusion Die Swell and Fitting Injection Parameters
ABS drain-waste-vent pipe and injection-moulded fittings manufactured from Diastal-315 are governed by
ASTM D2661 for dimensional and performance requirements and
ASTM D3965 for material cell classification, with supplementary conformance to
ISO 15103-1 where export shipments target European plumbing markets. Pipe extrusion is performed on a single-screw extruder with an L/D ratio between
24:1 and
30:1 and a screw compression ratio of
2.5:1 to
3.0:1, using a barrier flight design to homogenize the melt without excessive shear heating. Barrel temperature profile is set from
180°C at the feed zone rising to
215°C at the metering zone, with the adapter and die head maintained at
190°C to
210°C to control melt viscosity at the die lip. Die swell values for ABS in pipe extrusion typically range from
1.3 to
1.5, requiring a sizing sleeve inside diameter set proportionally smaller than the finished pipe outside diameter, with precise swell compensation determined by inline ultrasonic wall thickness measurement during start-up calibration. Vacuum calibration tank pressure is maintained between
-20 kPa and
-60 kPa relative to atmosphere, and the cooling water temperature is controlled at
15°C to
25°C to achieve a cooling rate that prevents frozen-in orientation from reducing impact resistance at pipe ends. Fitting injection moulding uses the same resin grade on machines with clamp forces from
350 t to
900 t, operating at melt temperatures of
210°C to
240°C and mold temperatures of
40°C to
70°C. Hydrostatic burst testing of pipe and fitting assemblies is performed at
23°C with a short-term failure pressure requirement of not less than
3.5 MPa, and long-term hydrostatic strength is extrapolated per
ISO 9080 to a 50-year design life at
23°C. The material must pass drop-weight impact testing at
-18°C with no visible crack propagation through the full wall thickness. NSF/ANSI 14 certification is required for potable water contact in North American installations, and the formulation must not contain cadmium-based pigments or lead stabilizers to remain compliant with
NSF/ANSI/CAN 61 contaminant leaching limits.
| Processing Variable | Pipe Extrusion | Fitting Injection |
| Melt temperature range | 190°C–215°C | 210°C–240°C |
| Tool/mould temperature | Die 190°C–210°C | Mould 40°C–70°C |
| Screw L/D ratio | 24:1–30:1 | 20:1–24:1 |
| Cooling medium temperature | 15°C–25°C water | 40°C–70°C pressurized water |
| Dimensional tolerance reference | ASTM D2661 Schedule 40 wall | ASTM D2661 socket depth |
Socket fusion joining is not specified for ABS DWV systems; solvent cement welding per
ASTM D2235 is the standard joining method, and the resin surface must be free of mould release agents, moisture, and low-molecular-weight surface exudate to achieve a minimum lap shear strength of
6.9 MPa after
72 h cure at
23°C. The extruded pipe exhibits a density of
1.03 g/cm³ to
1.07 g/cm³ per
ISO 1183-1, and any density deviation beyond this range indicates void formation or incorrect filler loading in the compound. Pipe wall thickness is verified by circumferential ultrasonic measurement at
4 equiangular positions every
100 m of extruded length, with out-of-roundness limited to
1.5% of nominal outside diameter for Schedule 40 dimensional classifications.When high-cavitation tooling for router enclosures and network switch housings demands wall thicknesses between
1.2 mm and
2.5 mm, ABS Diastal-315 is processed with melt temperatures of
225°C to
245°C and mold temperatures of
50°C to
70°C on electric injection moulding machines with clamp forces between
180 t and
650 t. The thin-wall condition raises the effective shear rate in the runner system above
10,000 s⁻¹, requiring gate diameters of at least
1.0 mm for tunnel gates and
1.5 mm for edge gates to prevent premature freeze-off before packing compensation. Pre-drying is performed at
85°C for
3 h in a desiccant dryer with a regeneration air temperature of
180°C or higher, and the drying hopper is purged with
-40°C dew point air at
2.0 m³/h per
kg/h throughput. Flammability classification is assessed per
UL 94 HB for enclosures that do not require V-rated performance, and any formulation change requiring a flame-retardant package must not rely on decabromodiphenyl ether, which is restricted under
EU 2019/1021 persistent organic pollutant regulation. Electrical safety conformity for information technology equipment and audio/video equipment is evaluated under
IEC 62368-1, which superseded
IEC 60950-1 and
IEC 60065, and the enclosure material is subject to glow-wire testing at
550°C per
IEC 60695-2-11 where it serves as a barrier to live components. Surface resistivity measurements are referenced to
IEC 62631-3-2, with antistatic additive packages targeting a value below
10¹² Ω for applications involving exposed data ports. Venting at the parting line is specified at
0.02 mm to
0.04 mm depth to prevent burn marks from adiabatic gas compression at the flow front, while avoiding flash formation that would exceed a
0.05 mm maximum allowed protrusion per customer drawing specifications.Process stability in electronics housing production is monitored through cavity pressure transducers embedded behind the ejector pins in each cavity of a
4-cavity to
16-cavity tool. The cavity pressure at the moment of complete filling is recorded and held within
±5% of the validated setpoint, typically
35 MPa to
55 MPa at the sensor location, because deviations above this band produce flash and deviations below produce sink marks on boss rear surfaces. Cooling time is calculated from part thickness using the relationship that cooling time scales with the square of wall thickness divided by thermal diffusivity, and for a
2.0 mm wall the cooling time is approximately
12 s to
18 s before demolding at a surface temperature below
80°C. Ejection force is controlled by limiting core draft angle to a minimum of
1° for textured surfaces and
0.5° for polished surfaces, because ABS with a high rubber phase content exhibits a higher coefficient of static friction against tool steel than unfilled polystyrene. Batch-to-batch variance in melt flow rate, measured per
ISO 1133-1 at
220°C under
10 kg load, should not exceed
±10% relative to the qualified reference lot, and incoming inspection includes ashing tests per
ISO 3451-1 Method A to confirm filler or glass fiber content where applicable.
| Standard/Regulation | Test Method or Clause Reference | Application Scope |
| IEC 62368-1 | Clause 6.4 fire enclosure requirements | ICT/AV equipment housings |
| UL 94 HB | Horizontal burn, 3.0 mm specimen | Non-structural enclosures |
| IEC 60695-2-11 | Glow-wire at 550°C | Live component barriers |
| IEC 62631-3-2 | Surface resistivity measurement | ESD-sensitive housing area |
| REACH Annex XVII | Entry 51 phthalate restrictions | Accessible plasticized parts |
| RoHS 2011/65/EU + (EU) 2015/863 | Annex II restricted substances | Electronic equipment assemblies |
When Medical Device Housings Require Biocompatibility Screening Without Animal-Derived Processing Aids
Diagnostic equipment enclosures, laboratory analyser front panels, and ultrasound cart shells are injection moulded from ABS Diastal-315 in facilities where material handling and processing documentation conform to
ISO 13485 quality management system requirements for medical device manufacturing. Cytotoxicity is evaluated per
ISO 10993-5 using the MEM elution method, where L929 mouse fibroblast cells are exposed to an extract of the finished moulding and a viability result of
≥70% of the negative control is required for acceptance. Intracutaneous irritation and skin sensitization data are referenced to
ISO 10993-10 and
USP <88> biological reactivity testing where the device is classified as surface-contacting with intact skin for a cumulative duration exceeding
30 days. The formulation must be free of processing aids, slip agents, and mould release additives derived from bovine, ovine, or caprine sources, with a supplier declaration of TSE/BSE absence prepared per
EMA/410/01 Rev. 3 and
ISO 22442 where materials of animal origin are concerned. Cleanroom moulding is executed under
ISO 14644-1 Class 7 conditions for components supplied non-sterile but intended for use in clinical environments, with airborne particulate concentration limited to
352,000 particles ≥0.5 µm per cubic metre. Mould release agents based on silicone emulsions are prohibited when the finished component will undergo subsequent adhesive bonding, pad printing, or ultrasonic welding, because residual silicone at the surface reduces lap shear bond strength by more than
40% compared to solvent-wiped surfaces when tested per
ISO 4587. Sterilization compatibility is verified for ethylene oxide cycles at
55°C to
60°C with relative humidity between
40% and
70%, using gas concentrations of
600 mg/L to
800 mg/L ethylene oxide for exposure durations of
4 h to
6 h, followed by aeration at
50°C for
12 h or longer to reduce residual ethylene oxide below
4 mg/device per
ISO 10993-7 acceptance criteria. Gamma irradiation at doses of
25 kGy to
50 kGy produces measurable discoloration in ABS due to conjugated double bond formation in the polybutadiene phase, and gamma sterilization is generally specified only when other modalities are incompatible with the device design.During validation of injection moulding parameters for medical housings, the process capability index Cpk for critical dimensions is required to exceed
1.33, and any dimension with a specification tolerance narrower than
±0.10 mm triggers 100% automated vision inspection at the machine side. Pre-drying is performed at
82°C for
4 h in a desiccant dryer equipped with a ceramic heater and closed-loop regeneration, and the material feed system is purged with medical-grade compressed air filtered to
0.01 µm particulate size and
-40°C pressure dew point. Screw and barrel surfaces in contact with the melt are specified as nitrided or bimetallic to eliminate iron contamination, and any abrasive wear of the screw flights resulting in iron levels above
50 ppm in the melt is cause for screw replacement before further production. The end products in this segment include bench-top analyser housings, centrifuge covers, patient monitor bezels, and laboratory automation equipment panels where cleanability, dimensional stability at repeated disinfection exposure, and documented material traceability from resin lot to finished device are the primary engineering requirements.
Thermoforming Luggage Shells from ABS Sheet Stock
Extruded ABS sheet produced from Diastal-315 resin is thermoformed into luggage shell halves at sheet thicknesses from
1.5 mm to
4.0 mm, using single-station shuttle thermoforming machines with quartz or ceramic infrared heating elements. Sheet surface temperature is conditioned to
160°C to
180°C on both faces before vacuum or plug-assist forming, because temperatures below
150°C produce localised stress whitening at deep draw corners and temperatures above
190°C cause sheet sag sufficient to compromise material distribution uniformity. A plug assist made from syntactic foam or PTFE-coated aluminium is engaged at
60% to
80% of the final draw depth for draw ratios exceeding
1:1, with plug temperature maintained at
90°C to
110°C to prevent premature sheet cooling on contact. Vacuum is applied at
-0.08 MPa to
-0.095 MPa gauge pressure within
0.5 s of sheet contact with the female mould, and the mould itself is temperature-controlled at
50°C to
80°C to set surface gloss and reduce post-forming sink at rib intersections. Post-mould shrinkage of formed ABS sheet is documented at
0.3% to
0.5% after
24 h conditioning at
23°C and
50% relative humidity per
ISO 11501 or internal dimensional stability protocols, and shell dimension verification is deferred until this conditioning period elapses to avoid false pass readings. Impact performance of finished luggage shells is evaluated through the
ATA 300 or equivalent internal drop test sequence, which imposes repeated impacts from
0.9 m height onto a concrete substrate at
-20°C,
23°C, and
60°C, and the shell must not exhibit through-panel fracture or hardware detachment after the prescribed cycle count. Environmental stress cracking resistance is screened against common service fluids including isopropanol, dilute detergent, and sunscreen formulations containing octinoxate, using a constant-strain jig method referenced to
ISO 4599 with an applied strain of
0.5% and an exposure duration of
72 h at
23°C. Any visible crazing at the loaded region constitutes failure and triggers a formulation review.Sheet extrusion for thermoforming grade feedstock is performed on a single-screw extruder with L/D of
30:1 to
36:1 and a barrier screw profile, feeding a flat die with internal deckle adjustment to maintain sheet thickness tolerance at
±0.05 mm across a
1200 mm die width. The extrudate is polished between a three-roll stack with the middle roll temperature set at
80°C to
100°C, and the cast film is edge-trimmed before winding. The sheet is conditioned at
23°C for
48 h prior to thermoforming to relax frozen-in orientation that would otherwise cause anisotropic shrinkage during heating. In hybrid luggage construction, injection-moulded frame components using the same resin grade are produced at melt temperatures of
220°C to
240°C and mould temperatures of
50°C to
70°C, then joined to thermoformed shells using structural adhesive cured at
23°C for
24 h to achieve lap shear strength exceeding
5.0 MPa per
ISO 4587. Published data for the specific thermoforming response of this grade is limited, and sheet processors are advised to characterise the lower and upper sheet temperature limits using a sag test fixture before committing to production tooling. The end products in this segment include hardside luggage shells, musical instrument cases, protective equipment housings, and industrial transport cases where the combination of thermoformability, surface hardness, and moderate impact resistance at cold temperature conditions is functionally matched to the application.
Guangzhou Kingfa Science & Technology Co., Ltd. supplies ABS Diastal-315 as a pelletized acrylonitrile-butadiene-styrene feedstock within the Diastal series. The grade is positioned for medium-flow injection-molding applications in which a balance of flow length, impact resistance, and surface quality is required. Publicly available datasheet values for the specific Diastal-315 subdesignation are limited; therefore the processing envelope, property ranges, and comparative distinctions presented here are drawn from industrial baseline data for unfilled ABS injection-molding grades with a comparable flow classification. Lot-specific design verification must be performed using the supplier certificate of analysis and the relevant ISO 2580-1 designation block.
What drying and residence-time boundary conditions apply before melt processing?
Moisture control is the first critical boundary condition. ABS pellets absorb atmospheric moisture, and when surface moisture reaches approximately 0.1 wt% or higher, degradation of process stabilizers and vaporization during plastication can produce splay, silver streaking, and reduced impact retention. Diastal-315 should be dried in a desiccant dryer with a supply-air dew point no higher than -20 °C. A drying temperature of 80±5 °C for 2–4 h is the standard starting condition. The target residual moisture before melt processing is below 0.02 wt%, as determined by Karl Fischer titration or a calibrated moisture analyzer. If the material has been stored in ambient warehouses at relative humidity above 60 %, the drying time should be extended to the upper end of the range or until the moisture target is confirmed. Hopper temperatures should not exceed 90 °C during extended idling because prolonged exposure can result in pellet surface oxidation and yellowing of the styrene-acrylonitrile phase.
Residence-time control is equally important. The butadiene-rubber phase in ABS undergoes thermo-oxidative cross-linking and chain scission when retained at melt temperatures for excessive periods. At barrel temperatures above 230 °C, total residence time in the plasticating unit should be limited to 8–10 min. During stoppages, the screw should be jogged and the barrel temperature reduced to 120–150 °C. Purging should use a styrenic purging compound rather than PVC or acetal purge materials; PVC contamination releases hydrogen chloride at processing temperatures and corrodes the screw, check ring, and nozzle. In twin-screw compounding operations with L/D ratios of 32:1 or higher, barrel vent ports are used to remove residual moisture and volatiles, but the supplier’s pellet stabilizer package is not designed for extended recompounding; downstream addition of recycled ABS should be constrained to the percentage stated on the lot certificate and validated by impact testing per ISO 179-1/1eA.
Barrel temperature profiling for unfilled ABS Diastal-315 typically begins with rear-zone settings of 190–210 °C, center-zone settings of 210–230 °C, front-zone settings of 220–240 °C, and a nozzle setting of 230–250 °C. These are initial set points, not universal values; the actual melt temperature measured by a needle pyrometer should be 220–245 °C for thin-wall filling and 210–230 °C for thick-section parts. Mold temperature should be maintained at 40–80 °C using water or oil thermolators with a control band no wider than ±5 °C. Lower mold temperatures reduce cycle time but increase molded-in stress and can reduce weld-line strength. Higher mold temperatures improve surface gloss, flow-marking uniformity, and weld-line coalescence but extend cooling time and may increase mold shrinkage variation.
Injection speed is set to achieve a stable melt-front velocity through the gate and cavity rather than the maximum machine velocity. Overly fast filling of ribbed or bossed geometries creates jetting and surface frothing. Injection specific pressure for unfilled ABS is commonly 60–120 MPa; packing pressure is typically 50–70 % of peak injection pressure and must be held long enough to prevent sink marks at the base of ribs and screw bosses. Back pressure should be maintained at 0.3–0.7 MPa to allow gentle homogenization without excessive shear heating. Screw rotation speed should be limited to 30–60 rpm for an injection screw with compression ratio 2.0:1–2.5:1 and L/D 20:1–24:1. If the shot size is below 30 % of barrel capacity, residence-time risk increases; if it is above 70 %, plastication consistency may decrease. The ideal shot weight is therefore 40–65 % of the rated barrel volume for this material class.
Mechanical and thermal design data for part validation
For preliminary part design, the following physical and mechanical envelope is representative of unfilled medium-impact ABS feedstocks in the same segment as Diastal-315; lot-specific certificates of analysis must replace these values for production release. Density is typically 1.04–1.07 g/cm³ when measured by ISO 1183-1. Tensile stress at yield is generally 35–50 MPa and tensile strain at break 5–25 % under ISO 527-2 at 23 °C. Flexural modulus is normally 2000–2500 MPa under ISO 178. Notched Charpy impact strength at 23 °C is commonly 10–30 kJ/m² with a 1eA notch under ISO 179-1. The heat deflection temperature under 1.8 MPa load is generally 90–105 °C under ISO 75-2, and Vicat softening temperature is typically 95–110 °C under 50 N load per ISO 306. Mold shrinkage is commonly 0.4–0.7 %, depending on wall thickness, gate geometry, and mold temperature, and should be measured on a plaque or article under ISO 294-4.
Those values define the application envelope. If the load-bearing service temperature exceeds 80 °C or the part must survive a 1.8 MPa load at temperatures above the measured HDT, high-heat ABS or another polymer is required. If the impact specification at -30 °C exceeds 20 kJ/m² or the part is a safety-related automotive component, low-temperature multi-axial impact data under ISO 6603-2 must be generated; published data for this specific grade are limited.
Usage is limited to interior or non-load-bearing exterior parts where the continuous service temperature remains below the HDT margin. Typical injection-molded articles include appliance fascia, housing shells, cable-management components, and trim panels. Outdoor exposure is not recommended unless UV-stabilized concentrates are validated by xenon-arc testing under ISO 4892-3; unpigmented and non-UV-stabilized ABS will yellow and lose impact after prolonged sunlight.
Comparative property envelopes for unfilled ABS injection-molding grades are shown below. The Diastal-315 column represents the general medium-flow category into which the grade is positioned; these values are not certified lot data.
| Property | Test method | Diastal-315 medium-flow ABS range | High-heat ABS range | Electroplating ABS range |
| Density | ISO 1183-1 | 1.04–1.07 g/cm³ | 1.05–1.07 g/cm³ | 1.05–1.08 g/cm³ |
| Melt volume-flow rate at 220 °C/10 kg | ISO 1133-1:2022 | 15–30 cm³/10 min | 5–15 cm³/10 min | 10–25 cm³/10 min |
| Tensile stress at yield | ISO 527-2 | 35–50 MPa | 38–52 MPa | 35–48 MPa |
| Flexural modulus | ISO 178 | 2000–2500 MPa | 2200–2600 MPa | 2000–2500 MPa |
| Notched Charpy impact, 23 °C, 1eA | ISO 179-1 | 10–30 kJ/m² | 8–20 kJ/m² | 15–30 kJ/m² |
| Heat deflection temperature, 1.8 MPa | ISO 75-2 | 90–105 °C | 100–115 °C | 90–105 °C |
| Vicat softening temperature, 50 N | ISO 306 | 95–110 °C | 105–120 °C | 95–110 °C |
When a high-heat, flame-retardant, or electroplating ABS is specified instead
Diastal-315 differs from high-heat ABS primarily in thermal resistance. High-heat ABS grades are modified with additional comonomer or heat-stabilizer systems and typically show HDT values 10–25 °C higher than general-purpose ABS. Where the application contains metal inserts, heat-generating electrical contacts, or paint-bake ovens above 85 °C, a high-heat grade should be specified. The mechanical property balance of Diastal-315 is otherwise closer to general-purpose ABS, and its higher flow length can reduce injection pressure in thin-wall parts compared with low-flow high-heat grades.
Compared with electroplating ABS, Diastal-315 is not formulated to produce the controlled butadiene-particle size distribution and low internal strain required for uniform chromic acid etching and electroless metal adhesion. If decorative chrome plating is required, an electroplating grade should be selected, and plating adhesion should be tested under ISO 4527 or the corresponding customer standard. In comparison with halogenated flame-retardant ABS, Diastal-315 should not be used where a V-0 rating at 1.5 mm under IEC 60695-11-10 is required unless an independent test report demonstrates otherwise; the addition of flame retardants at the molding machine is not recommended because it can reduce impact strength and alter melt viscosity.
In comparison with low-flow flat-sheet extrusion ABS, Diastal-315 is optimized for injection molding and is not recommended for sheet extrusion at thicknesses above 3 mm unless melt strength is confirmed. Its medium-flow melt viscosity is too low for large-diameter pipe or sheet extrusion without sheet sag. In comparison with very high-flow ABS grades with melt volume-flow rates above 35 cm³/10 min, Diastal-315 retains better weld-line strength and lower tendency for fingered edge flow, but it may be less suitable for long flow-path components with wall thickness below 0.8 mm.
Production-scale injection molding of unfilled ABS grades in the Diastal-315 classification commonly observes specific failure modes. Splay is most often caused by residual moisture or by gas entrapment in hot-runner manifold zones above 250 °C. Gate blush appears as a low-gloss halo around edge gates and is controlled by profiling injection speed through the gate, increasing mold temperature above 50 °C, and relocating gates to hidden surfaces. Weld-line fracture in impact tests occurs when the flow fronts cool below their fusion temperature before merging; the notched impact retention at a weld line is frequently lower than the base value, but published data for this specific configuration are limited. If weld-line strength is critical, the weld line should be moved to a non-loaded region, or local mold heating should be applied and validated by ISO 179-1/1eA or ISO 6603-2.
Chemical incompatibility boundaries are relevant in service. Styrenic resins are sensitive to environmental stress cracking induced by ketones, esters, aromatic hydrocarbons, and chlorinated solvents. Cleaning of ABS parts should use water, mild detergent, or isopropyl alcohol only after verifying the compatibility of printing or adhesive layers. Aggressive solvents may not dissolve the polymer but can cause crazing and reduced impact resistance. If adhesive bonding or painting is required, surface treatment and primer selection should be validated by cross-cut adhesion per ISO 2409 or peel testing; silicone-based mold release agents should be avoided because they lower surface energy and reduce paint adhesion.
Why is mold temperature control decisive for cosmetic ABS surfaces?
Cosmetic defects in ABS are strongly influenced by mold temperature uniformity. When wall thickness is below 2 mm, the melt front freezes rapidly, and variations in mold surface temperature of more than ±5 °C create visible flow lines, gloss differences, and matte bands across the part. A thermolator with turbulent water flow should be used rather than a heated mold alone; cooling channel spacing and circuit design must be checked for pressure drop and Reynolds number above 10,000 to ensure heat transfer. Surface gloss measured by ISO 2813 with a 60 ° specular geometry typically increases with mold temperature, but gloss consistency is more important than the absolute value. Gate blush, splay, and drag marks are reduced by lowering the mold-temperature differential between the stationary and moving halves to less than 5 °C.
Regulatory compliance documentation should be requested for the exact lot and shipment. The supplier’s analysis certificate is required to confirm that the material meets RoHS 2011/65/EU Annex II restrictions for lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE, and to confirm REACH SVHC registration status under EC 1907/2006. Food-contact status, electrical-grade tracking resistance, and UL color-specific flammability listings are not transferred automatically from a generic ABS resin; they must be certified for the finished part and the specific color concentrate used at the molding machine. If the material is colored by dry pigment blending, dispersion quality should be verified by optical microscopy and tensile impact retention because uneven pigment dispersion can reduce notched impact strength and create visible streaks.