| HS Code | 606488 |
| Density | 1.04 g/cm³ |
| Melt Flow Rate | 1.8 g/10 min (200°C/5 kg) |
| Tensile Strength | 44 MPa |
| Elongation At Break | 30 % |
| Flexural Strength | 70 MPa |
| Flexural Modulus | 2.2 GPa |
| Notched Izod Impact Strength | 20 kJ/m² |
| Heat Deflection Temperature | 85 °C (1.82 MPa) |
| Vicat Softening Temperature | 105 °C |
| Rockwell Hardness | R105 |
| Molding Shrinkage | 0.4-0.6 % |
| Ul Flammability Rating | HB |
| Water Absorption | 0.2-0.4 % |
As an accredited CHIMEI (Chi Mei) ABS PA-747S factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | CHIMEI (Chi Mei) ABS PA-747S is packaged in 25 kg moisture-resistant bags, palletized on standard shipping pallets for safe transport. |
| Container Loading (20′ FCL) | A 20′ FCL typically loads about 17–18 metric tons of CHIMEI ABS PA-747S in 25 kg bags, subject to carrier weight limits. |
| Shipping | CHIMEI ABS PA-747S is shipped as non-hazardous polymer pellets, not regulated as dangerous goods. Standard packaging is 25 kg bags or 1,000 kg bulk bags. Keep dry, cool, and away from ignition sources, moisture, and direct sunlight; follow normal industrial hygiene practices. |
| Storage | Store CHIMEI (Chi Mei) ABS PA-747S in a cool, dry, well-ventilated area away from direct sunlight, heat, moisture, and ignition sources. Keep it in original sealed packaging to prevent moisture absorption and contamination. Avoid contact with strong oxidizers and solvents. Maintain stable temperature, use first-in, first-out stock rotation, and follow local regulations and SDS recommendations. |
| Shelf Life | Shelf life is two years when stored cool, dry, in original sealed packaging away from sunlight and moisture. |
Downstream applications for CHIMEI Polylac ABS PA-747S are concentrated in injection-molded structural and housing components where high notched Izod impact, low-temperature ductility, and moderate melt flow are the controlling resin variables. The following scenarios are differentiated by process window, additive package, and terminal part geometry; each is supported by compliance anchors and manufacturing limits observed on production-scale equipment. All process windows remain subordinate to lot-specific certificates of analysis and tool trial data.
In automotive interior trim injection molding, PA-747S is processed as an amorphous high-impact ABS base resin for parts that carry occupant contact loads, seatbelt retractor paths, and thermal cycling from -30°C to 80°C. Compliance anchors include FMVSS 302 and ISO 3795 for horizontal burn rate, EU ELV Directive 2000/53/EC, REACH Regulation (EC) No 1907/2006, and RoHS Directive 2011/65/EU. Incoming melt flow rate is recorded under ISO 1133-1:2022 at 220°C/10 kg, and batch-to-batch variation beyond ±2 g/10 min from the certificate of analysis triggers drying and process adjustment. The molding formulation uses PA-747S at 100 phr as the only resin phase; color masterbatch at 1–2 phr; hindered phenolic antioxidant at 0.1–0.3 phr; zinc stearate internal release at 0.1–0.3 phr; and no phthalate plasticizers or silicone external mold releases. Material is dried in a desiccant dryer at 80°C for 2–4 h to a residual moisture content below 0.05 wt%, measured by Karl Fischer coulometric analysis; moisture above 0.10 wt% produces splay and reduces notched Izod under ASTM D256-10 or ISO 180. Production-scale single-screw reciprocating injection molding machines with screw L/D 20:1–22:1 are operated at melt temperature 230–250°C, mold temperature 40–70°C, back pressure 0.5–1.0 MPa, screw speed 40–70 rpm, injection pressure 80–120 MPa, and clamp force 4–5 kN/cm² of projected area. Barrel residence time above 5 min causes rubber-phase oxidation and a measurable drop in low-temperature impact. Terminal finished parts include lower B-pillar trim covers, center console side covers, seat side shields, glove box outer doors, and instrument panel lower closeouts.
The critical process conflict in clamshell power tool housings is weld-line integrity after melt fronts meet around motor mount bosses, vent slots, and screw bosses. Compliance is assessed against IEC 62841-1:2014 enclosure requirements and UL 94 HB flammability classification, with RoHS Directive 2011/65/EU and REACH Regulation (EC) No 1907/2006 applied to exported assemblies. The downstream molding formula comprises virgin PA-747S pellets at 80–85 wt%, dried first-pass regrind from sprues and rejected shells at 15–20 wt%, color masterbatch at 1–2 wt%, and internal lubricant at 0.2–0.5 phr. Regrind is dried separately at 80°C for 2–4 h and blended in an autoloader; dust fines below 0.5 mm are limited to 2 wt% to prevent gas splay and screw slippage. Processing on hydraulic or servo-hydraulic two-platen injection machines from 1500 kN to 4000 kN clamp force uses barrel zones at 180–200°C feed, 210–230°C compression, 220–240°C metering, and nozzle at 220–235°C. Mold temperature is held at 45–75°C; the upper end is required because cold single-gate filling produces weld-line Izod retention below 45% of the parent value in ribbed boss regions. Sequential valve-gated hot runners, pack pressure 60–80 MPa, and hold time 6–10 s per mm wall thickness reduce sink at screw bosses. Terminal parts include angle grinder motor clamshells, cordless drill body halves, jigsaw housing shells, and orbital sander dust shroud frames.
The controlling parameter is environmental stress cracking under repeated cleaning-agent contact rather than short-term mechanical load. Compliance anchors include IEC 60335-1:2020 for household appliance safety, UL 746C for polymeric enclosures, REACH Regulation (EC) No 1907/2006, and RoHS Directive 2011/65/EU. The direct-injection formulation uses PA-747S at 100 phr, color masterbatch at 1–2.5 phr, hindered phenolic antioxidant at 0.2–0.4 phr, and zinc stearate at 0.1–0.3 phr; ester-based plasticizers are excluded because they reduce chemical resistance and lower deflection temperature under ISO 75-2:2013. Molding is conducted at melt temperature 235–245°C and mold temperature 60–80°C using polished tool steel cavity inserts to avoid flow lines on high-gloss surfaces. Color changeovers use a purging compound with a high-viscosity polyolefin base at 1–2 kg per change; abrasive purges are avoided because they damage polished cavity surfaces. Barrel temperatures must not exceed 250°C; repeated residence above 5 min during color changeovers causes brown streaks in white and light grey shells. Diluted aqueous detergents are tolerated, while ketones, esters, and aromatic solvents induce stress cracking at highly loaded boss areas. The application boundary is external cosmetic shells only; direct food-contact approvals are not claimed for PA-747S unless lot-specific certification is provided. Terminal finished parts include stand mixer outer shells, food processor top covers, vacuum cleaner canister bodies, and handheld vacuum dust cup housings.
Because PA-747S holds flatness within 1.0 mm over 300 mm when cooled in a post-ejection fixture, office equipment enclosures with long flow paths from 250 mm to 500 mm are produced without gas assist. Compliance is evaluated under IEC 62368-1:2018, UL 94 HB, and RoHS Directive 2011/65/EU. The molding formulation contains PA-747S at 100 phr, carbon black or custom masterbatch at 1–2.5 phr, antioxidant at 0.1–0.3 phr, and slip additive at 0.1–0.2 phr. Flame retardant packages are not included because wall thicknesses above 1.5 mm generally require only UL 94 HB; adding brominated flame retardant reduces Izod impact and shifts melt flow. Gate positions are placed on non-visible inner frame ribs with land length 1.0–1.5 mm and edge gate cross section 0.8–1.2 mm. Processing uses melt temperature 220–240°C, mold temperature 40–60°C, injection pressure 80–110 MPa, pack pressure 50–70 MPa, and cooling fixtures that hold the part until surface temperature drops below 60°C. Terminal parts include printer side panels, scanner lower frames, multifunction device front doors, and control panel bezels.
Painted two-wheeler exterior panels impose a surface-adhesion boundary because any silicone or PTFE-containing mold release migrates to gate blush zones and produces cross-cut adhesion failure after painting. Compliance is assessed by ISO 2409 cross-cut classification 0–1 on painted substrates, ISO 4892-2 accelerated weathering for UV resistance, REACH Regulation (EC) No 1907/2006, and RoHS Directive 2011/65/EU. The formulation uses PA-747S at 100 phr, UV absorber and hindered amine light stabilizer at 0.3–0.8 phr for dark colors, color masterbatch at 1–2 phr, and no silicone-based external release. Injection molding is performed at melt temperature 230–250°C, mold temperature 45–65°C, and clamp force 3–4 kN/cm² of projected area. After ejection, parts are washed, power-cleaned, and coated with a low-bake two-component polyurethane primer and topcoat at 70–80°C for 30–40 min; powder coating is substituted by liquid coating because cure temperatures above 160°C would distort unfilled ABS. Pre-painting surface tension after aqueous degreasing should be at least 40 mN/m. Terminal finished parts include scooter front fenders, motorcycle side covers, under-seat storage outer shells, and rear lamp body panels.
Tool trunk and modular storage case production with PA-747S is driven by thick-wall dimensional control and low-temperature drop performance rather than high-gloss appearance. Compliance anchors include UL 94 HB, IEC 60068-2-75 mechanical impact testing when specified for industrial enclosures, REACH Regulation (EC) No 1907/2006, and RoHS Directive 2011/65/EU. The molding formulation comprises PA-747S at 100 phr, color masterbatch at 1–3 phr, antioxidant at 0.1–0.3 phr, internal lubricant at 0.2–0.5 phr, and clean first-pass regrind at 10–20 wt% of total shot weight. Processing uses melt temperature 225–240°C, mold temperature 50–70°C, pack pressure 50–70 MPa, and hold time 8–12 s per mm wall thickness for sections from 2.0 mm to 3.5 mm. Cooling fixtures prevent bowing in large flat lids; sink at thick boss areas is controlled by delayed packing and gate placement away from visible top surfaces. Drop-impact testing at -20°C is applied according to customer-specific protocols, with corner wall sections increased by 20–30% to prevent cracking. Terminal parts include power tool carry cases, instrumentation transport housings, modular drawer bodies, and exhibition display case frames.
| Application scenario | Primary standard or regulation | Test method or classification | Operational boundary |
|---|---|---|---|
| Automotive interior trim | FMVSS 302; ELV 2000/53/EC; REACH | ASTM D256-10; ISO 180 | Residual moisture 0.05 wt% max; residence 5 min max |
| Power tool housings | IEC 62841-1:2014; UL 94 HB | UL 94 HB; weld-line Izod retention | Weld-line retention 45% min in ribbed bosses |
| Household appliance shells | IEC 60335-1:2020; UL 746C | ISO 75-2:2013 | Barrel temperature 250°C max; no ester plasticizers |
| Office equipment enclosures | IEC 62368-1:2018; UL 94 HB | UL 94 HB; warpage after cooling fixture | Warpage 1.0 mm/300 mm max |
| Painted two-wheeler panels | ISO 2409; ISO 4892-2 | Cross-cut 0–1 | Silicone-free mold release before painting |
| Modular storage cases | UL 94 HB; IEC 60068-2-75 | IEC 60068-2-75 impact when specified | Hold time 8–12 s/mm for thick walls |
| Scenario | PA-747S loading | Additive package | Excluded additive |
|---|---|---|---|
| Automotive interior trim | 100 phr | Masterbatch 1–2 phr; antioxidant 0.1–0.3 phr; zinc stearate 0.1–0.3 phr | Phthalate plasticizer; silicone release |
| Power tool housings | 80–85 wt% virgin; 15–20 wt% regrind | Masterbatch 1–2 wt%; lubricant 0.2–0.5 phr | Dust fines above 2 wt%; silicone release |
| Household appliance shells | 100 phr | Masterbatch 1–2.5 phr; antioxidant 0.2–0.4 phr; zinc stearate 0.1–0.3 phr | Ester-based plasticizer |
| Office equipment enclosures | 100 phr | Masterbatch 1–2.5 phr; antioxidant 0.1–0.3 phr; slip additive 0.1–0.2 phr | Brominated flame retardant for HB-only walls |
| Painted two-wheeler panels | 100 phr | UV/HALS package 0.3–0.8 phr; masterbatch 1–2 phr | Silicone or PTFE mold release |
| Modular storage cases | 100 phr; regrind 10–20 wt% | Masterbatch 1–3 phr; antioxidant 0.1–0.3 phr; lubricant 0.2–0.5 phr | High-gloss polishing additives |
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Refrigerator liners are typically formed from extruded sheet of 2.0 mm to 4.5 mm thickness, heated to sheet surface temperatures of 165 °C to 190 °C and formed with areal draw ratios up to 2.5:1. PA-747S is used in this application because its lower melt mass-flow rate corresponds to higher melt strength and higher graft-rubber molecular weight retention after sheet extrusion. However, published data for the retained impact after deep-draw thermoforming of this specific grade are limited; therefore, finished liner impact values must be measured on formed samples in accordance with ISO 180/1A or ASTM D256. Production evidence on single-screw sheet lines with 90 mm or 120 mm barrier screws and L/D ratios of 32:1 to 40:1 indicates that melt temperatures of 200 °C to 230 °C at the die lip, with chill-roll temperatures of 60 °C to 85 °C, suppress surface whiting and minimize frozen-in orientation that later releases as liner bowing. Deep-draw corners require the sheet to be heated uniformly to a core temperature no more than 12 °C below the surface; otherwise, corner thinning may fall below 40 % of original sheet thickness and the liner can fail internal cavity pressure testing. When regrind content exceeds 20 wt%, pre-drying at 80 °C for 3–4 h in a desiccant dryer with a dew point not higher than -30 °C is required to bring moisture below 0.02 %, and the regrind fraction should be limited to 30 wt% to avoid a measurable loss in notched impact. The material is not compatible with brominated flame-retardant ABS residuals if the production line is not purged; cross-contamination changes the UL 94 classification and may create corrosive decomposition products at die temperatures above 240 °C.
Sheet conversion of PA-747S requires close control of screw speed, back pressure, and melt filtration because the lower flow state raises melt pressure at the screen changer. With a melt mass-flow rate of 0.8 g/10 min at 200 °C/5 kg, the resin generates higher screw torque than PA-756 at the same throughput; therefore, screw speed is typically limited to 60–80 rpm on 90 mm extruders to keep barrel pressure below 300 bar. Melt pumps are recommended for thickness uniformity; a gear pump upstream of the sheet die reduces surging and allows die lip gauge variation within ±0.05 mm on 3.0 mm sheet. The cooling-roll stack is operated with a roll gap of 2.0 mm to 3.5 mm and differential roll temperatures: the middle roll is held 10 °C to 15 °C above the first roll to minimize stress curl. If the melt exceeds 235 °C, the polybutadiene phase undergoes oxidative scission, visible as yellowing and a drop in notched Izod impact from 31 kJ/m² to below 24 kJ/m². If the sheet is stored at ambient relative humidity above 60 % prior to thermoforming, reheating causes surface blisters; sheets should be either wrapped in low-moisture-transmission film or re-dried at 80 °C for 2 h. Knife trimming of cold sheet is not recommended below 10 °C because the sheet becomes notch-sensitive and edge cracks can initiate during later trimming. Published data for this specific line configuration is limited, and processing boundaries should be confirmed on the target equipment.
For freezer door panels formed from PA-747S, the primary performance criterion is not single-notch Izod but multiaxial impact at -25 °C. Instrumented impact tests under ISO 6603-2 on formed panels of 3.0 mm thickness show that ductile puncture energy is higher than for PA-717C and PA-756, but published data for this exact lot is limited. The rubber phase in PA-747S maintains a secondary loss peak below -40 °C, which allows crack arrest under rapid loading. In practice, freezer liner corners should be formed to radii no smaller than 2.0 mm; tighter radii concentrate frozen stress and reduce puncture energy by more than 20 %. When the liner is exposed to polyurethane foam blowing agents, resistance to environmental stress cracking can be assessed under ISO 4600 ball/ring stress-cracking specimens. PA-747S performs better after annealing at 70 °C for 1 h because annealing lowers residual tensile stress below 8 MPa. Excessive annealing near 90 °C can promote polybutadiene crosslinking and reduce ductility, so thermal conditions must be tightly controlled.
Within the CHIMEI POLYLAC ABS range, PA-747S occupies a low-flow, high-impact position that is distinct from PA-747 and PA-756. The difference from PA-747 is primarily observed in notched impact and melt-flow balance: PA-747S typically provides a lower melt mass-flow rate and a higher rubber content, which improves deep-draw corner integrity but requires more care in screw recovery during injection molding. PA-756, in contrast, is designed for high-speed injection molding of thin-wall structural parts and has a significantly higher melt mass-flow rate; it cannot be substituted into sheet applications where sagging during preheat and uneven draw cause wall-thickness variation above 15 %. Direct grade-to-grade comparison requires matching test specimens and conditioning under ISO 291 at 23 °C/50 % RH. The typical property profile for PA-747S is summarized below.
| Property | Test method | Representative value |
|---|---|---|
| Density | ISO 1183-1 | 1.04 g/cm³ |
| Melt mass-flow rate | ISO 1133-1 at 200 °C/5 kg | 0.8 g/10 min |
| Tensile yield stress | ISO 527-2 | 46 MPa |
| Flexural modulus | ISO 178 | 2300 MPa |
| Notched Izod impact | ISO 180/1A at 23 °C | 31 kJ/m² |
| Heat deflection temperature | ISO 75-2 at 1.8 MPa | 95 °C |
| Vicat softening temperature | ISO 306 B50 | 102 °C |
| Mold shrinkage | ISO 294-4 | 0.4–0.7 % |
The lower flow of PA-747S increases shear viscosity at typical sheet extrusion shear rates compared with PA-756. This means die pressure in a 1500 mm sheet die can be 25–40 % higher than with PA-756. The selection of PA-747S therefore depends on whether the end-use requires low-temperature impact below -20 °C or higher melt strength. Injection molders seeking cycle-time reduction should not select PA-747S for wall sections below 1.5 mm without mold-flow simulation and gate redesign.
In injection molding, PA-747S is generally reserved for thick-walled covers, housings, and interior components where toughness outweighs cycle time. If a specification initially written for PA-756 is changed to PA-747S, melt temperature should be raised from 200–220 °C to 210–235 °C, and mold temperature should be raised from 30–40 °C to 40–60 °C to improve weld-line strength and reduce internal stress. Because the melt mass-flow rate is 0.8 g/10 min at 200 °C/5 kg, cavity filling is slower; therefore, injection velocity profiles should be adjusted to avoid jetting at the gate. On hot-runner systems, gate diameters below 1.0 mm produce excessive shear heating and gate blush; valve gates with 1.5 mm or larger bores are preferred. Hydraulic machines with clamp force from 250 t to 450 t and screw diameter 60–80 mm can process PA-747S if plasticizing capacity is derated by 15–20 % relative to PA-756. Back pressure should be set at 5–10 bar to prevent air entrapment without over-shear of the polybutadiene phase. Mold shrinkage of 0.4 % to 0.7 % is close to general-purpose ABS, but rib sinking is more pronounced because the lower flow requires higher packing pressure; pack pressure of 40–60 bar post-gate is typical for 2.0 mm wall sections. Weld lines in deep ribs should be tested under ISO 527-2 tensile specimens cut from molded plaques because notch-sensitive crack paths follow weld-line boundaries. If the mold has texture depths below 25 µm, the lower flow may not reproduce the texture unless mold temperature is raised to 70 °C. These adjustments prevent brittleness and surface delamination that occur when high-flow ABS parameters are retained without revalidation.
With respect to chemical resistance, PA-747S shares the general ABS limitations: it is not recommended for continuous contact with ketones, esters, chlorinated solvents, or concentrated oxidizing acids; it performs acceptably in dilute aqueous acids, alkalis, and many aliphatic hydrocarbons under ambient conditions. The material is typically supplied with a RoHS Recast 2011/65/EU statement and REACH SVHC declaration for articles; however, food-contact status is application-specific and must be verified under EU 10/2011 or FDA 21 CFR 181.32 for the final part, because regrind, colorants, and processing aids can change migration behavior. Ultraviolet weathering resistance is low in unpigmented form; long-term outdoor use requires UV-stabilized black or white grades and testing under ISO 4892-2 for the intended service period. Parts processed from PA-747S can be bonded with solvents such as methyl ethyl ketone only under controlled ventilation and after compatibility testing, because solvent stress cracking can occur at molded-in stress concentrations above 10 MPa. The material should not be dried in hoppers with residual PVC or polyamide, as off-gassing at 200 °C can contaminate the polymer and produce surface defects. These limitations are not exhaustive and do not replace end-use validation.