| HS Code | 504307 |
| Density | 1.08 g/cm3 |
| Melt Flow Rate | 3.0 g/10 min (220°C/10 kg) |
| Tensile Strength | 42 MPa |
| Elongation At Break | 30% |
| Flexural Strength | 60 MPa |
| Flexural Modulus | 1900 MPa |
| Notched Izod Impact Strength | 10 kJ/m2 |
| Vicat Softening Temperature | 96°C |
| Heat Deflection Temperature | 78°C at 1.82 MPa |
| Rockwell Hardness | 105 R |
| Light Transmittance | 88% |
| Haze | 3% |
| Molding Shrinkage | 0.4-0.6% |
As an accredited Tianjin Dagu MABS DG-T516HC factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Tianjin Dagu MABS DG-T516HC packaging: 25 kg net per paper-plastic composite bag, supplied palletized in secure industrial packs. |
| Container Loading (20′ FCL) | Tianjin Dagu MABS DG-T516HC loaded into a 20′ FCL, bags palletized, container inspected, sealed, and secured for export. |
| Shipping | Tianjin Dagu MABS DG-T516HC is shipped as non-hazardous polymer resin pellets in moisture-barrier bags or bulk containers. Keep dry, cool, ventilated, away from direct sunlight and ignition sources; avoid moisture and contamination. Not regulated as dangerous goods for transport. |
| Storage | Store Tianjin Dagu MABS DG-T516HC indoors in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, sparks, open flames, and moisture. Keep containers or bags tightly closed, palletized, and protected from puncture, water, and contamination. Avoid static buildup, segregate from incompatible materials, follow the SDS and local regulations, and use first-in, first-out stock rotation. |
| Shelf Life | Typically 24 months from production when stored dry, in original sealed packaging, below 40°C, away from direct sunlight. |
DG-T516HC is a methyl methacrylate-acrylonitrile-butadiene-styrene molding resin supplied as high-clarity granules. The application scenarios below are organized by downstream failure mechanism rather than by generic industry label. All processing windows are starting points that must be confirmed against lot-specific melt flow rate, residual moisture, and optical data because published data for this specific configuration is limited.
Clear rigid housings for diagnostic instruments, lateral-flow analyzers, and fluid-management manifolds molded from DG-T516HC are evaluated first through extractables and residual monomer profiling, not through standard mechanical data alone. The extraction protocol for cytotoxicity screening follows ISO 10993-12:2012 at 6 cm²/mL in serum-containing medium at 37 °C ± 1 °C for 24 h, with eluates then applied to L929 cells under ISO 10993-5:2009. Residual acrylonitrile and methyl methacrylate are quantified by headspace GC-MS with a reporting threshold of 1 µg/g because these low-molecular-weight residuals dominate cell culture outcomes in methyl methacrylate-acrylonitrile-butadiene-styrene copolymers. Lot-to-lot variance in residual monomer is influenced by devolatilization vacuum level and residence time in the polymer finishing step; therefore, a certificate of analysis that lists only melt flow rate and Izod impact is insufficient for medical device use.
Molding these housings requires pre-drying in a desiccant-bed dryer with a dew point ≤ −30 °C and an air temperature of 80 °C ± 5 °C for 4 h, targeting residual moisture ≤ 0.03 wt%. Failure to achieve this moisture level produces silver streaks at the gate and reduces transmission at 450 nm. The recommended melt temperature window is 230 °C to 245 °C, with mold temperature held at 45 °C to 70 °C. High shear at hot-runner valve gates should be limited because the crosslinked polybutadiene phase in MABS can agglomerate under high pressure drop, producing low-angle haze in thick bosses and flow leaders. On a conventional reciprocating screw with L/D 20:1–25:1 and compression ratio 2:1–2.5:1, back pressure should be maintained at 5 bar to 15 bar to keep melt density stable without adding excessive shear work. If an external release agent is necessary, a 0.1 wt% aqueous dilution of a styrenic-compatible release agent should be applied sparingly and checked for haze on the first shot; internal release additives are not recommended because they can reduce clarity and interfere with subsequent bonding or printing.
Sterilization must be decided before tooling because residual stress from ejection and gate geometry interact with sterilization. Gamma irradiation above 25 kGy can increase yellowness index in unstabilized transparent styrenic copolymers; if gamma is unavoidable, evaluation must include yellowness index shift after 25 kGy and 50 kGy using ASTM E313-20. Ethylene oxide is generally less damaging to optical properties but introduces outgassing control obligations under ISO 10993-7:2008; residual ethylene oxide limits are based on device exposure duration and patient contact, not on a single fixed threshold. Terminal components in this segment include point-of-care analyzer windows, nephelometric cell bodies, transparent fluid header manifolds, blood-collection tube racks with optical fill detection, and covers for coagulation analyzers.
| Test / Standard | Measured Attribute | Application-Specific Requirement | Status for DG-T516HC |
|---|---|---|---|
| ISO 10993-12:2012 | Extraction ratio, eluate preparation | 6 cm²/mL, 37 °C ± 1 °C, 24 h | Protocol selection only; lot verification required |
| ISO 10993-5:2009 | Cytotoxicity | MEM elution, L929 cell viability | Test report on final device required |
| ISO 10993-10:2021 | Sensitization | Single and repeated patch | Final device validation required |
| ISO 10993-23:2021 | Irritation | Intracutaneous or topical exposure | Final device validation required |
| ISO 10993-7:2008 | Ethylene oxide residual | Use-dependent exposure limit | Process validation only |
| ASTM E313-20 | Yellowness index shift post-sterilization | Record ΔYI at 25 kGy, 50 kGy | Comparative lot test |
| ASTM D1003-21 | Haze, luminous transmittance | Post-molding, post-annealing | Lot-specific target |
For thick-walled cosmetic jar bases, domed fragrance caps, and lotion pump collars, the dominant failure mode in service is environmental stress cracking induced by ester-based fragrances and emollients, not impact fracture. Methyl methacrylate-acrylonitrile-butadiene-styrene copolymers show broad resistance to dilute acids and alkaline solutions but can absorb ethyl acetate, benzyl acetate, linalyl acetate, and certain cyclomethicone blends; this uptake lowers the local stress threshold for crazing at machined edges, threads, and ejector pins. A suitable screening protocol is a modified ASTM D543-21 immersion under constant flexural strain: pre-conditioned bars or finished components are wetted with the target formulation, placed in a loaded fixture at a defined outer-fiber strain, and inspected for surface crazing at 8 h, 24 h, and 72 h. Published data for DG-T516HC under specific fragrance concentrates is limited; the test must be repeated with every new perfume oil because low-level impurities can shift the critical stress-crack threshold.
Molding thick transparent parts from MABS requires balancing gate freeze time against sink marks at the thick-to-thin transition. A three-stage hold profile—65% of peak injection pressure for 4 s, 45% for 6 s, and 25% for 8 s—compensates for differential shrinkage between a 3.0 mm base and a 1.5 mm sidewall. Gate diameter should be at least 0.8 times the nominal wall thickness, and the gate should be located on the base or at an interior hub rather than on the visible sidewall to minimize optical flow marks. Mold temperature is held at 55 °C to 70 °C to buffer the temperature drop during slow filling. If a lubricious additive is proposed to reduce cap squeak, silicone-based masterbatches above 0.2 wt% can reduce clarity and alter surface polarity sufficiently to weaken adhesion of hot-foil printing or metallized finishes; any additive addition must be qualified by ASTM D1003-21 haze measurement and crosscut adhesion testing on the decorated part.
Regulatory compliance for cosmetic packaging in the European Union is anchored to Regulation (EC) No 1223/2009 on cosmetic products, which places finished goods safety responsibility on the responsible person rather than on the polymer supplier. The packaging material itself must satisfy REACH Annex XVII restrictions for monomers, heavy metals, and substances of very high concern, and the complete article must meet the heavy metal limits in Directive 94/62/EC on packaging and packaging waste. For some markets, migration of styrene, acrylonitrile, and methyl methacrylate from packaging into cosmetic formulations is evaluated by a 10-day incubation at 40 °C with food simulants under Regulation (EU) No 10/2011; even if the package is not food-contact, this provides a conservative extractable fingerprint. Terminal products in this segment include premium cosmetic jar bases, transparent outer caps, collar rings, pump overcap shells, and thick-walled fragrance caps where high clarity must survive repeated torque loading during opening.
For light guide plates and display lenses made from DG-T516HC, the critical optical variables are spectral transmission in the blue band where photodiode response begins to roll off, not only total luminous transmittance. The optical path through a 2.0 mm flat plaque should be evaluated with ASTM D1003-21 for total luminous transmittance and haze, and with a diode-array spectrophotometer for transmission at 450 nm, 525 nm, and 630 nm. Loss in the 450–500 nm region is particularly visible because the human eye perceives yellowing against a white light source. MABS has a refractive index near 1.51 due to the methyl methacrylate fraction, but exact index for a production lot must be taken from the certificate of analysis or measured by an Abbe refractometer; even a 0.005 shift changes ray tracing in edge-lit light guide plates. Diffuse haze from the polybutadiene phase can be managed by high-gloss tooling, low-shear filling, and adequate mold temperature.
Production of light guide plates uses injection molding with a melt temperature of 235 °C to 245 °C and a mold temperature of 60 °C to 75 °C. Flow-induced birefringence is minimized by filling through a side gate on the longest edge and avoiding a center hot drop, which can create a visible radial stress pattern in cross-polarized light. Cooling time for a 2.0 mm plaque may exceed screw recovery time, making cycle time cooling-limited; reducing mold temperature to shorten cycle time is not acceptable because it increases birefringence and lowers surface replication. If a color masterbatch is required, it should be limited to 0.5–1.0 wt% and must use a MABS or styrene-methyl methacrylate carrier rather than a standard ABS carrier, because a higher-rubber ABS carrier can increase diffuse haze and reduce light guide efficiency. Post-molding, the parts can be coated with a UV-cured acrylate hard coat to raise pencil hardness from the uncoated HB–2H range to 3H–4H, but adhesion must be tested per ASTM D3359-17 after 48 h at 85 °C/85 % RH. Terminal products include router light pipes, set-top box front windows, LED indicator lenses, touch sensor windows, and transparent display covers where polycarbonate is not required for heat resistance.
Regulatory compliance for electronic components is driven by RoHS Directive 2011/65/EU Annex II restricted substances such as lead, mercury, cadmium, hexavalent chromium, polybrominated biphenyls, and polybrominated diphenyl ethers. If the customer requires flame-retardant transparency, the resin should not be compounded with brominated flame retardants because those additives often destroy clarity; instead, the piece part must be evaluated on a UL 94 yellow card with the specific wall thickness and color. Published data for DG-T516HC with halogen-free flame-retardant systems is limited, so flammability claims must be based on a third-party test report rather than a generic MABS rating.
Control panel lenses for washing machines, tumble dryers, dishwasher consoles, and HVAC wall controls are a separate application zone because the surface must survive repeated contact with household cleaners, disinfecting wipes, and skin oils at elevated temperatures. DG-T516HC is selected when the part does not need the heat distortion temperature of polycarbonate but must maintain transparency after exposure to benzyl ammonium chloride disinfectants, 0.5% active chlorine bleach solution, and 70% isopropanol. Resistance is screened by 24 h immersion at 23 °C ± 2 °C per ASTM D543-21; the pass criterion is absence of visual crazing, not tensile strength retention, because cosmetic integrity is the first customer-visible failure. The critical molding variable is gate placement: side-gated panels often show a distinct weld line at the distal end of the lens, and the rib-to-surface transition can retain residual stress that is later activated by disinfectant exposure. A post-molding anneal at 70 °C for 1 h reduces this stress enough to improve chemical resistance but increases total cycle time.
Hard coat adhesion on MABS requires surface activation before coating because the low surface polarity of styrenic acrylic copolymers can lead to premature delamination under humidity. Coating thickness is typically maintained at 5 µm to 15 µm; thicker films are prone to cracking at sharp lens edges, while thinner films do not provide sufficient scratch resistance. Adhesion is tested per ASTM D3359-17 crosshatch after 48 h at 85 °C/85 % RH and after 5 cycles of 24 h water immersion at 65 °C; a minimum of 4B classification is considered suitable for decorative lenses, while 5B is required for direct-touch keypad windows. Terminal products include HVAC display lenses, rotary knob inserts, capacitive touch sensor windows, iron soleplate inspection windows, and induction cooker display screens where local temperatures do not exceed the Vicat softening temperature of the specific lot.
Under conditions of solvent bonding, lateral flow cartridges and microfluidic inserts impose a different constraint: the part must survive a 45 °C annealing cycle followed by 24 h immersion in 70/30 v/v ethanol/water without opacification at the bond line. MABS can be solvent welded with cyclohexanone, methyl ethyl ketone, or a mixture of cyclohexanone and butyl acetate, but the capillary gap must be maintained between 0.05 mm and 0.15 mm to form a uniform weld; larger gaps produce bubble haze, while a zero gap can cause stress cracking when the solvent swelling pressure exceeds the craze threshold. A solvent blend of 80/20 v/v cyclohexanone/butyl acetate is often used as a starting point, but the ratio must be adjusted for local dew point and air velocity because evaporation rate changes the effective dwell time. Solvent dwell time must be validated from 0.5 s to 3 s on the actual production line. When methyl ethyl ketone is used in automated lines, explosion-proof ventilation is required, and leachate testing of the finished part must confirm that solvent residuals are below the reporting threshold of 1 µg/g for methanol extractables. Under Regulation (EU) 2017/746 on in vitro diagnostic medical devices, polymer-related extractables are part of analytical performance and stability testing; therefore, a solvent-bonded device is not acceptable without a process-specific extractables study. Terminal products include lateral flow assay cassette bodies, sample transfer reservoirs, transparent microfluidic manifolds, and PCR plate sealing frames.
Transparent filter bowls, pump head covers, and water-level sight tubes in small appliances can be considered for MABS, but the service window narrows when water temperature exceeds 60 °C or oxidative disinfectants are present. Hypochlorous acid and chlorine dioxide attack the residual unsaturation in the polybutadiene phase, leading to a measurable transmission loss in the 400–500 nm region that precedes mechanical embrittlement. Continuous exposure to 1.0 ppm free chlorine at 25 °C may be acceptable for many high-clarity MABS grades, but published data for DG-T516HC under sustained chlorinated water exposure is limited; the material must be tested by recirculating exposure with the actual water chemistry, including pH, hardness, and scale inhibitors. For potable water components, NSF/ANSI 61 certification cannot be assumed for a generic molding grade; confirmation from the resin manufacturer or a certified test laboratory is mandatory before tooling is committed.
Processing these thick-walled bowls uses hot-runner valve gating to hide the gate vestige at the bottom of the bowl. The risk is shear heating across the valve pin; local melt temperature must not exceed 250 °C because yellowing accelerates above this threshold. Mold temperature is set at 60 °C to 80 °C, and hold pressure is profiled to compensate for a wall thickness transition from 2.0 mm bowl sidewall to 4.0 mm threaded neck. Threads must be molded with generous radii and restrained gate-induced orientation because thread-root residual stress is the most common initiation point for chlorine-driven crazing. If a UV stabilizer masterbatch is added for outdoor lift-up covers, let-down should not exceed 2 wt% because excess additive can depress Vicat softening and increase haze. Terminal products include espresso machine water reservoir sight tubes, transparent condensate inspection windows, non-potable filter bowls, and pump head covers where water contact occurs at a controlled temperature below 60 °C.
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Tianjin Dagu MABS DG-T516HC is a pelletized methyl methacrylate-acrylonitrile-butadiene-styrene terpolymer supplied by Tianjin Dagu Chemical Industry Co., Ltd. The grade falls within the MABS moulding and extrusion material family designated under ISO 19066-1. It combines a methyl methacrylate-containing rigid phase with a grafted polybutadiene rubber phase; refractive-index matching between the matrix and the rubber modifier is the primary mechanism responsible for optical transparency. Published data for this specific configuration is limited in independent public data sheets, so the following processing boundaries and property comparisons are drawn from class-level MABS reference data and the manufacturer’s application guidance. Grade-specific first-article validation remains mandatory before tooling release.
Drying is normally carried out in a desiccant dryer with a return-air dew point at or below -30 °C. A class-level MABS starting point is 80 °C for 3 h to 4 h, with a residual pellet moisture target below 0.05 wt%. Hopper residence times beyond 4 h should be avoided because stagnant heated pellets can develop yellowing at the hopper walls. Surface splay in moulded parts is frequently a downstream signal of moisture breakthrough, even when the dryer setpoint appears correct. The drying system should be audited using a dew-point meter at the return-air line, not only at the desiccant tower outlet.
Comparison should be made on measured optical and mechanical values rather than resin family labels. In transparent ABS, clarity is achieved through reduced rubber content, finer rubber morphology, or refractive-index tuning; MABS replaces part of the styrene with methyl methacrylate, producing a lower-haze, higher-transmission window while retaining notched impact resistance. PMMA offers higher tensile modulus and surface hardness but lower notched impact strength. The table below presents typical published reference windows for MABS, transparent ABS, and PMMA. These are not DG-T516HC certified lot values; they are class-level data for comparative screening.
| Property | Test Standard | MABS Reference Window | Transparent ABS | PMMA |
|---|---|---|---|---|
| Light transmittance | ASTM D1003 | 88–91% | 85–88% | 92–93% |
| Haze | ASTM D1003 | 0.8–2.5% | 2.0–5.0% | <1.0% |
| Tensile yield strength | ISO 527-2 | 37–50 MPa | 35–45 MPa | 60–75 MPa |
| Flexural modulus | ISO 178 | 1800–2400 MPa | 1700–2200 MPa | 2800–3300 MPa |
| Notched Izod impact at 23 °C | ISO 180/1A | 5–12 kJ/m² | 8–20 kJ/m² | 1.5–2.5 kJ/m² |
| Density | ISO 1183-1 | 1.08–1.10 g/cm³ | 1.06–1.10 g/cm³ | 1.17–1.20 g/cm³ |
| Vicat softening temperature B50 | ISO 306 | 85–105 °C | 85–98 °C | 95–108 °C |
| Melt volume-flow rate | ISO 1133-1 | 8–25 cm³/10 min | 5–20 cm³/10 min | 2–10 cm³/10 min |
These comparisons illustrate that DG-T516HC should not be selected solely on transmittance. PMMA remains the preferred material when surface hardness and UV resistance dominate; transparent ABS remains preferred when room-temperature impact and lower melt temperature are critical; MABS occupies the intermediate position when a balance of optical clarity, impact strength, and melt flow is required. Grade-specific lot data for DG-T516HC may shift within these reference windows due to rubber content, graft morphology, and stabiliser package; substitution of PMMA or transparent ABS should not occur without re-executing dimensional, optical, and impact validation.
Tooling for transparent MABS requires venting placements that are often more extensive than for opaque ABS. Parting-line vents should be spaced along the flow front convergence points and should not exceed 0.03 mm depth for unfilled low-viscosity grades. Vacuum-assisted venting is used on large flat optical faces to prevent diesel gas marks at knit lines. Draft angles below 0.5° can produce ejection stress whitening at undercuts; textured surfaces typically require 1° draft per 0.025 mm of texture depth. Gate blush is controlled by reducing first-stage injection velocity and increasing melt temperature within the supplier’s upper limit. A thermal gate diameter below 1.2 mm may impose excessive shear heating in thin-wall parts.
For lenses and light guides, wall thickness should be designed with a flow-length-to-thickness ratio below 150:1 for unfilled MABS. Beyond this ratio, packing pressure decays before the cavity is fully packed, creating sink marks at the gate side and haze at the flow front. A constant wall thickness of 2.0 mm to 3.0 mm is often used for optically functional housings; changes in wall section above 25% generate visible knit lines. If the part includes a clear window and an opaque frame, two-shot moulding or laser welding may be used, but material compatibility must be confirmed.
Thin-wall housings below 1.5 mm nominal wall thickness rely on high melt-volume-flow rate grades, but flow length is not governed by MVR alone. Cavity filling pressure, gate design, and melt temperature interact. A general-purpose transparent ABS may reach equivalent spiral flow but exhibit higher haze because the rubber particle size distribution is not tuned for thin-wall birefringence. For DG-T516HC, the manufacturer’s technical data should be consulted for spiral-flow length at 240 °C and 80 MPa injection pressure. If the certified value is unavailable, published data for this specific configuration is limited; start-up mould trials should use a valve-gated hot runner with a gate diameter at least 60% of local wall thickness or a cold full-round runner of 4 mm to 6 mm for walls above 2 mm. Gate shear rates above 50 000 s⁻¹ can produce melt fracture and flow marks in clear styrenics, making direct hot-tip gates unsuitable for cosmetic surfaces.
Medical and diagnostic housings produced from DG-T516HC should be evaluated for the intended sterilisation modality. Gamma sterilisation under ISO 11137-1 and ISO 11137-2 can induce measurable yellowing in non-stabilized MABS at a reference dose of 25 kGy; the full maximum dose plus process margin must be tested. EtO sterilisation under ISO 11135 normally requires aeration time to reduce residual gas below limits established through ISO 10993-7. MABS can retain impact properties after EtO better than lower-rubber clear styrenics, but each device geometry must be validated. Steam autoclaving is generally outside the recommended use unless the supplier confirms that the grade survives repeated cycles without gate-area distortion, because class-level MABS Vicat softening temperatures may fall below 105 °C.
Environmental stress cracking resistance in MABS is controlled by rubber content, rubber particle size, and graft adhesion. DG-T516HC is not intended for aggressive solvent contact. Dilute aqueous cleaning agents and dilute acids may be tolerated at room temperature, but ketones, esters, aromatic hydrocarbons, and concentrated oxidising acids attack the methacrylate and styrene matrix. Alcohol-based disinfectants containing 70% ethanol or isopropanol are used on transparent housings, but repeated exposure under residual moulded-in stress can induce crazing at gates and weld lines. For cleaning-agent compatibility, moulded bars should be tested under constant strain, and the critical strain for visible crazing should be reported for the exact cleaner. Published data for DG-T516HC in this chemical configuration is limited; no field claim should be made without test data.
Twin-screw compounding is not required at the moulding plant because DG-T516HC is supplied as a ready-to-mould formulation. If masterbatch colouring is necessary, the carrier should be MABS or transparent ABS with a melt-volume-flow rate within 10 cm³/10 min of the base resin to prevent visible flow-line separation. Screws with an L/D ratio of 20:1 to 24:1 and a compression ratio of 2.0:1 to 2.5:1 are suitable for pre-compounded MABS. Excessive shear heating above 260 °C should be avoided because methyl methacrylate segments can depolymerise, releasing volatiles and reducing optical clarity. Machines originally configured for polycarbonate frequently generate longer residence time; purging with a heat-sensitive indicator compound is required before transparent production.
Clear MABS components are joined by ultrasonic welding, solvent bonding, or UV-curable adhesives. Ultrasonic welding requires a near-field joint because the butadiene phase attenuates high-frequency vibration. A shear joint with controlled interference of 0.05 mm to 0.15 mm per side is preferred for structural clear parts. Welding pressure and amplitude should be reduced relative to unfilled amorphous ABS; excessive amplitude produces melt smearing and white marks at the joint. Post-mould machining should avoid dull tools and low feed rates because frictional heat above the glass transition can create stress whitening. Dry machining with carbide tooling at a surface speed below 200 m/min is a conservative starting point, but the supplier-specific guidance for DG-T516HC should be followed.
Outdoor glazing is not a nominal application for unstabilized MABS. Ultraviolet exposure yellows the butadiene phase, and photo-oxidation reduces impact properties. For DG-T516HC, accelerated weathering should be run under ISO 4892-2 using a xenon-arc source with a borosilicate filter. The difference from PMMA is significant: PMMA is inherently UV-stable, while MABS requires light stabiliser selection and copolymer composition control to approach similar outdoor performance. If the application is indoor lighting or short-term outdoor use, a UV-stabilized formulation or a protective topcoat should be qualified.
Compliance documentation required for DG-T516HC before commercial release includes:
| Regulatory Area | Selected Standard or Test Method | Evidence Required |
|---|---|---|
| RoHS substance restrictions | IEC 62321 series under Directive 2011/65/EU | Supplier declaration, XRF screening, batch-level lot data |
| REACH SVHC obligations | Regulation (EC) No 1907/2006 Article 33 | SDS and SVHC declaration for each supplied lot |
| Medical device biocompatibility | ISO 10993-1, ISO 10993-5, ISO 10993-10 | Finished-device biocompatibility evaluation |
| Radiation sterilisation validation | ISO 11137-1, ISO 11137-2 | Maximum dose verification and yellowness shift data |
| EtO sterilisation residuals | ISO 11135, ISO 10993-7 | Residual ethylene oxide limits on finished device |
| Accelerated weathering | ISO 4892-2, ASTM D1003 | Delta yellowness index and delta haze after xenon-arc exposure |
| Flammability classification | UL 94 | Supplier Yellow Card at target wall thickness |
Batch-level incoming inspection for DG-T516HC should include melt volume-flow rate per ISO 1133-1, notched Izod impact per ISO 180/1A, transmittance and haze per ASTM D1003, and yellowness index per ASTM E313. Retention of these data against the supplier’s control limits is necessary for maintaining optical and mechanical reproducibility in high-volume moulding. If regrind is used, virgin-to-regrind ratio should not exceed 20% for optical parts unless the moulder demonstrates no shift in haze, yellowness index, or notched impact across 5 consecutive production lots. Regrind exposed to multiple heat histories above 240 °C can exhibit higher haze at the gate due to rubber particle agglomeration, so purge and residence-time control is more critical than for opaque ABS.