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Jiangsu Xinfuda ABS H1100 H E

    • Product Name: Jiangsu Xinfuda ABS H1100 H E
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 520283
    Density 1.04–1.06 g/cm³
    Melt Flow Rate 3–10 g/10 min (220 °C/10 kg)
    Tensile Strength 40–50 MPa
    Elongation At Break 20–40%
    Flexural Strength 60–75 MPa
    Flexural Modulus 2000–2400 MPa
    Notched Izod Impact Strength 15–25 kJ/m² (23 °C)
    Rockwell Hardness 100–110 R scale
    Vicat Softening Temperature 95–105 °C
    Heat Deflection Temperature 80–90 °C (1.82 MPa)
    Molding Shrinkage 0.4–0.7%
    Flammability HB (UL 94)
    Processing Method Extrusion/Injection molding

    As an accredited Jiangsu Xinfuda ABS H1100 H E factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Jiangsu Xinfuda ABS H1100 H E is supplied in 25 kg moisture-proof woven bags, palletized for bulk industrial handling and storage.
    Container Loading (20′ FCL) 20′ FCL loads about 17 MT of Jiangsu Xinfuda ABS H1100 H E, packed in 25 kg bags.
    Shipping Jiangsu Xinfuda ABS H1100 H E is typically shipped as non-hazardous ABS resin pellets in sealed moisture-barrier bags or lined bulk containers. It is not regulated for transport and has no UN number. Keep dry, avoid heat, sunlight, contamination, and static buildup; use normal industrial hygiene.
    Storage Store Jiangsu Xinfuda ABS H1100 H E in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and flames. Keep original packaging closed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and static buildup. Store on clean pallets, do not overstack, and separate from incompatible chemicals. Follow local regulations and the SDS.
    Shelf Life Shelf life is typically 24 months when stored dry, below 30°C, away from sunlight, in unopened original packaging.
    Application of Jiangsu Xinfuda ABS H1100 H E

    In injection-molded interior automotive pillar trim produced from Jiangsu Xinfuda ABS H1100 H E, the material is pre-dried in a desiccant dryer at 80 °C for 3 h–4 h to a residual moisture content below 0.02 wt%; dryer inlet dew point is held at -30 °C or lower. Injection molding is conducted on a three-zone reciprocating screw with L/D 22:1 and compression ratio 2.2:1, fitted with a positive shutoff nozzle. Barrel temperature profile from rear to front is 200 °C, 215 °C, 225 °C, and 230 °C, with melt temperature measured at 225 °C–240 °C. Mold temperature is controlled at 45 °C–60 °C using pressurized water units. Injection velocity is kept at 50 mm/s–80 mm/s for a flow length of 180 mm–220 mm; hold pressure is 50 MPa–65 MPa for 6 s–8 s. Back pressure is set at 8 bar–12 bar to maintain melt homogeneity without excessive shear heating. These parameters follow the specimen preparation principles of ISO 294-1, with production tolerances adjusted through cavity pressure monitoring. Terminal components are A-pillar covers, B-pillar upper trims, seat side shields, and center console side panels.

    Colorant loading for interior trim is limited to 2 wt%–3 wt% of an ABS-compatible masterbatch to avoid selective reflectance shifts in dark charcoal finishes. The mold surface is textured to Ra 8 µm–12 µm rather than polished; high-gloss variants of this resin can develop flow-direction gloss streaks when the butadiene phase orients under shear. For UV-stabilized pillar trim exposed to sunlight through side glazing, 0.2 wt%–0.5 wt% of a benzotriazole UV absorber masterbatch is added. Emission requirements are evaluated per VDA 278:2011 for volatile and semi-volatile organic compounds, and the compound is screened against REACH Regulation (EC) No 1907/2006, Annex XVII. Process limitations: barrel residence time above 10 min at 230 °C or higher causes oxidation of the butadiene phase, appearing as splay and beige edge streaks. Regrind for visible surfaces is limited to 10 wt%; higher loading reduces impact strength and introduces gloss variability. Published data for this specific configuration is limited, so lot-specific melt flow rate per ISO 1133-1:2022 and capillary viscosity under 1000 s⁻¹ shear should be verified before setting fill velocity.

    Does ABS H1100 H E Maintain Impact Retention in Electrical Enclosures at Wall Thickness Below 1.5 mm?

    For wall thicknesses below 1.5 mm in electrical enclosure and consumer electronics housing applications, mold-filling pressure increases nonlinearly, and the impact-modified composition of ABS H1100 H E can exhibit reduced notched impact retention if the cavity is underfilled. On a 1200 kN–1800 kN hydraulic injection molding machine, the recommended melt temperature is 220 °C–235 °C, mold temperature 40 °C–60 °C, and injection pressure 90 MPa–120 MPa. Gate cross-section should be 60%–70% of the nominal wall thickness, with a land length not exceeding 1.0 mm. A hot runner with externally heated manifold and valve-gate control is preferred for multi-cavity tools; manifold temperature is held at 230 °C–245 °C. The melt should be injected with an initial velocity of 40 mm/s–60 mm/s and profiled to reduce jetting at the gate. Packing pressure is ramped from 45 MPa to 55 MPa and held for 4 s–6 s. Notched Izod impact values should be assessed according to ISO 180/A on specimens cut from the finished housing; lot-to-lot variation at wall thickness below 1.5 mm is typically wider than at 3.0 mm.

    For electrostatic control, 1.0 wt%–2.0 wt% of an antistatic masterbatch based on ethoxylated alkylamine can be compounded into the base resin. Surface resistivity measured per IEC 61340-2-3:2016 is then verified on the molded part; published data for this specific configuration is limited, therefore the final concentration must be adjusted until the desired dissipative range is achieved. Flame resistance is not provided by the unmodified grade. Enclosures requiring a V-0 rating must either use a flame-retardant ABS compound under a different grade designation or accept an HB rating after verification at the final thickness. Terminal products include router housings, power adapter enclosures, desktop charger shells, intercom faceplates, and small industrial sensor housings.

    Standard / DirectiveDesignationApplication relevance
    UL 94UL 94 HBFlame rating at final wall thickness; unmodified ABS H1100 H E is not a V-0 compound.
    IEC 62368-1 / EN 62368-1IEC 62368-1:2018 / EN 62368-1:2020Fire enclosure and electrical energy hazard compliance for AV/ICT enclosures.
    RoHS Directive2011/65/EU and (EU) 2015/863Heavy metal and phthalate restriction in homogeneous materials.
    REACH RegulationRegulation (EC) No 1907/2006SVHC candidate list and Annex XVII restriction screening.
    IEC 61340IEC 61340-2-3:2016Surface resistance verification of antistatic enclosures.

    The sheet extrusion route for ABS H1100 H E is usually configured on a single-screw extruder with L/D 30:1–34:1 and a three-section barrier screw with compression ratio 2.5:1. Barrel temperatures are set to 190 °C in the feed zone, 205 °C in the compression zone, 215 °C–225 °C in the metering zone, and 215 °C–230 °C at the die adapter. A screen pack of 80/120 mesh is installed to remove contaminants. Pre-drying at 80 °C for 3 h–4 h is mandatory, with moisture content below 0.02 wt%; otherwise, micro-bubbles appear in the sheet surface as pinhole clusters. The melt is fed to a coat-hanger die with adjustable flex lip; die land length is maintained at 15 mm–20 mm to stabilize die swell. The extrudate enters a three-roll calendering stack with roll temperatures of 75 °C–90 °C for the polished top roll, 70 °C–85 °C for the middle roll, and 60 °C–75 °C for the lower roll. Sheet thickness is controlled at 1.5 mm–4.0 mm, and haul-off speed is synchronized with melt pressure at 8 MPa–12 MPa before the breaker plate. Mechanical properties after forming are evaluated according to ISO 527-2 for tensile modulus and ISO 178 for flexural modulus.

    For thermoforming into luggage shells and equipment cases, the sheet is heated to 130 °C–160 °C in a dual-sided quartz or ceramic IR oven. The forming window is narrow; below 125 °C the sheet tears at corners, and above 165 °C the rubber phase begins to degrade, producing orange-peel surface defects. Plug-assisted forming uses a syntactic foam plug temperature of 100 °C–120 °C and mold temperature of 50 °C–65 °C. Regrind from edge trim is incorporated at 15 wt%–20 wt% for non-appearance inner layers; higher proportions reduce draw ratio and cause thickness variation. Colorant masterbatch loading in extrusion is limited to 2 wt%–3 wt%; titanium dioxide-based white formulations at 4 wt% increase melt viscosity and require a die temperature increase of 5 °C. Terminal articles include hard-shell suitcases, protective equipment cases, and thermoformed inner liners for electronic device packaging.

    When EN 71-3 Extraction Limits Constrain Colorant Choice in ABS H1100 H E Toy Molding

    When toy components are injection molded from ABS H1100 H E, the colorant package must be selected so that the finished article complies with the element migration limits of EN 71-3:2019+A1:2021; the standard migration tests are carried out on the final molded part after conditioning, not on the raw pellet. The loading of organic colorants is typically held at 1 wt%–2 wt% for transparent or translucent items and 2 wt%–4 wt% for opaque items; cadmium- and lead-based pigments are excluded under REACH Regulation (EC) No 1907/2006, Annex XVII. The base resin is processed at a melt temperature of 215 °C–230 °C and mold temperature of 40 °C–55 °C. Because thin-wall toy parts often have wall sections of 1.0 mm–1.5 mm, gate diameter is set to 0.8 mm–1.0 mm to promote shear thinning. Packing pressure is 40 MPa–50 MPa with a hold time of 2 s–4 s. Ejector pins must be positioned away from visible surfaces; ABS H1100 H E at high impact-modified content can develop ejector mark whitening when demolded below 35 °C. Terminal articles include toy vehicle bodies, building block components, board game pieces, and non-nipple infant toy structural parts. For articles marketed in the EU, Toy Safety Directive 2009/48/EC requires a technical file that includes the EN 71 series; for the US market, the relevant requirement is ASTM F963-23 for heavy metal migration and mechanical safety. Published data for this specific grade under repeated oven aging tests is limited.

    Pipe Fitting DWV Compliance and Solvent Cement Compatibility

    Pipe-fitting production from ABS H1100 H E targets drainage, waste, and vent fittings in building drainage systems. The relevant product standards are EN 1455-1:2022 for ABS piping systems for soil and waste discharge, or ASTM D2661-21 for ABS Schedule 40 DWV pipe and fittings in North America. Injection molding of fittings with wall sections of 3.0 mm–6.0 mm requires a melt temperature of 215 °C–235 °C and a mold temperature of 45 °C–65 °C. Because thick sections trap heat, cooling time is determined by part thickness squared; for a 5 mm wall, cooling time is typically 18 s–25 s. Packing pressure is 55 MPa–70 MPa, with an initial hold time of 10 s–15 s to suppress sink marks at the hub intersection. Gate design uses a tab or fan gate with thickness 70% of the nominal wall; direct sprue gates into the hub create stress concentration at the intersection and reduce hydrostatic burst retention. Solvent cement compatibility is tested with a mixture of methyl ethyl ketone, cyclohexanone, and tetrahydrofuran in ratios defined by the fitting manufacturer; the cement softens the surface to form a fused joint. The resin must not be blended with PVC or CPVC regrind above 2 wt%, because mixed polymer domains reduce solvent-cement fusion strength and produce leak paths under hydrostatic pressure testing. Terminal articles include P-traps, wyes, elbows, couplings, and vent fittings.

    High-Gloss Housing Molding Requires Reduced Melt Temperature and Fast Fill

    At melt temperatures exceeding 245 °C, high-gloss ABS H1100 H E household appliance housings develop surface defects including silver streaks, black specks at hot runner dead ends, and color shift in white formulations. The molding process for appliance outer shells, such as air purifier shells, water dispenser front panels, and vacuum cleaner body covers, is therefore set at a melt temperature of 215 °C–230 °C, mold temperature 55 °C–70 °C, and injection speed at 80 mm/s–120 mm/s to freeze gloss before the rubber phase migrates. The mold surface is polished to SPI A-2 or SPI A-3, and venting is increased to 0.02 mm–0.04 mm land depth to prevent burn marks. The colorant is a high-gloss black or pearlescent white masterbatch at 2 wt%–3 wt%; pigment agglomerates above 10 µm are filtered through a 200-mesh screen in the masterbatch carrier. Shrinkage compensation is performed with a mold shrinkage of 0.5%–0.7% per ISO 294-4. Dimensional stability of molded panels is checked after 24 h at 23 °C ± 2 °C and 50% ± 10% RH. Household appliance housings are evaluated for fire classification under IEC 60335-1:2020, Clause 30.2; unmodified ABS H1100 H E requires glow-wire verification for the specific appliance category and is not certified for all enclosure functions. The process limitation is residence time: with hot runner systems, any cavity blocked by a jam can cause material to remain in the manifold at 230 °C for more than 8 min, resulting in yellowing at the next shot.

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    Certification & Compliance
    More Introduction

    Jiangsu Xinfuda ABS H1100 H E is a pelletized acrylonitrile-butadiene-styrene resin. The polymer class consists of a styrene-acrylonitrile copolymer matrix with a dispersed polybutadiene rubber phase; the rubber phase supplies low-temperature impact energy absorption, while the styrene-acrylonitrile matrix contributes rigidity, melt processability and resistance to dilute acids, alkalis and aliphatic hydrocarbons. Published independent data for this specific configuration is limited. The designation H1100 H E is not a standardized ISO 19069-2 classification; unless the producer supplies the data block for melt volume-flow rate, Vicat softening temperature and notched Izod impact, the suffix characters cannot be decoded as confirmed viscosity, elongation or end-use fields. Downstream processing decisions should therefore reference the batch certificate of analysis and the manufacturer’s technical datasheet. Candidate end uses for this polymer class include appliance housings, interior automotive trims, electrical enclosures and consumer electronic parts; the specific grade must be qualified for each use. At minimum, the downstream evaluation should request the following standardized values:

    How Should Moisture Uptake Be Controlled Before Screw Plastication?

    ABS pellets are hygroscopic in the sense that surface and interstitial moisture are retained after shipping and silo storage; equilibrium moisture content at 23 °C and 50 % RH is generally reported between 0.2 wt% and 0.5 wt%. Moisture above approximately 0.1 wt% vaporizes in the compression zone of the screw and produces splay, surface veining and loss of surface gloss on parts. For ABS H1100 H E, desiccant drying at 80 °C to 90 °C with a drying air dew point of −30 °C or lower for 2 h to 4 h is appropriate until residual moisture falls below 0.1 wt%. The hopper should not be heated without dry air circulation. Residence beyond 4 h at 90 °C should be avoided because the polybutadiene phase can undergo oxidative yellowing followed by a measurable reduction in notched Izod impact under ISO 180/A. Moisture before and after drying can be verified by Karl Fischer titration according to ISO 15512:2019 or by the producer’s in-house loss-on-drying method correlated to the ISO method. Dried pellets should not remain in an open machine hopper at ambient humidity above 60 % RH for more than 30 min; if the plant humidity is high, a closed hopper fed with dry air is required. Regrind from sprues and runners can contain additional surface moisture; it should be dried with virgin pellets and limited to 20 wt% unless process capability data support higher levels.

    For melt processing of medium-viscosity ABS grades, a general-purpose three-zone screw with an L/D of 20:1 to 24:1 and a compression ratio of 2.0:1 to 2.5:1 is commonly employed. Melt temperature measured by air shot should remain between 220 °C and 250 °C; mould wall temperature should be controlled from 40 °C to 80 °C to balance gloss, cycle time and dimensional stability. Injection velocity should be set to maintain continuous melt-front progression without hesitation; a fill time of 1 s to 4 s for wall thicknesses of 1.5 mm to 3.0 mm is typical. If the producer’s certificate of analysis confirms a melt volume-flow rate in the medium-viscosity range—approximately 5 cm³/10 min to 15 cm³/10 min at 220 °C/10 kg under ISO 1133-1—then standard cold-runner tools can be used; for lower MVR, gate and runner diameters may require an increase of 10 % to 20 % to prevent short shots. Masterbatch color concentrates should be tumble-mixed for 15 min at 20 rpm if no liquid binder is used; if liquid binders are present, mixing time is reduced to 5 min. Thermal degradation in ABS is autocatalytic once initiated; the butadiene phase oxidizes first, generating carbonyl species that appear as yellowing and reduce elongation at break. Residence time at melt temperature should therefore be limited to 10 min to 15 min; shutdown purges should use SAN or acrylic purging compound at the purging compound manufacturer’s recommended temperature. The producer may report physical properties on specimens prepared according to ISO 294-1 moulding conditions.

    When High-Elongation Grades Are Used in Cold-Impact Components

    If the H suffix in H1100 H E indicates a high-impact or high-elongation ABS, the differentiation from general-purpose ABS is achieved primarily through an increase in the volume fraction and particle-size distribution of the polybutadiene phase. Representative published ranges place general-purpose ABS rubber phase volume fraction near 5 % to 12 %, while high-impact grades commonly extend from 12 % to 20 %. This morphological shift increases notched Izod impact under ISO 180/A at 23 °C from a general-purpose range near 10 kJ/m² to 18 kJ/m² to a high-impact range of 20 kJ/m² to 35 kJ/m², but reduces tensile modulus under ISO 527-2 from roughly 2.2 GPa to 2.7 GPa to 1.8 GPa to 2.3 GPa. Elongation at break may shift from below 10 % to above 15 %, although published data for this specific configuration is limited. Density for high-impact ABS is usually between 1.03 g/cm³ and 1.07 g/cm³ under ISO 1183-1. Higher rubber content increases die swell in sheet extrusion, an effect quantified by extrudate swell ratio on a capillary rheometer, reduces melt flow, and can produce a slightly higher coefficient of linear thermal expansion. A high-impact grade may not be interchangeable with high-flow ABS used for thin-wall parts; high-flow grades typically exceed 20 cm³/10 min MVR under ISO 1133-1 at 220 °C/10 kg, but they sacrifice low-temperature impact resistance. Cold-impact applications include interior door panels, lower B-pillar trim, luggage compartment covers and battery housing covers. At −30 °C, high-impact ABS generally exhibits ductile failure only in unnotched tests; notched tests may still show brittle failure depending on rubber particle size and graft morphology.

    Representative ABS family differentiation ranges reported in published polymer datasheets. Values are not a substitute for a producer certificate of analysis for Jiangsu Xinfuda ABS H1100 H E.
    ABS family Rubber phase volume fraction (%) MVR (ISO 1133-1, 220 °C/10 kg, cm³/10 min) Notched Izod (ISO 180/A, 23 °C, kJ/m²) Tensile modulus (ISO 527-2, GPa)
    General-purpose 5–12 10–20 10–18 2.2–2.7
    High-impact / high-elongation 12–20 8–15 20–35 1.8–2.3
    High-flow 5–10 25–40 8–15 2.1–2.5
    Heat-resistant 8–15 5–15 15–25 2.0–2.5

    Compared with high-impact polystyrene, an ABS high-impact grade provides better resistance to aliphatic oils and increased surface hardness. Compared with ASA, ABS H1100 H E is not expected to offer prolonged ultraviolet weathering stability unless UV stabilizer packages are specified. Replacement of butadiene rubber with saturated acrylic rubber in ASA eliminates the allylic hydrogens that are susceptible to photo-oxidation. If outdoor exposure is part of the end-use, the producer should supply a weathering program conducted under ISO 4892-2 or ISO 4892-3 with color and impact retention data.

    Electroplating and Weld-Line Limitations in Production Tooling

    Electroplating on ABS relies on the selective etching of the polybutadiene phase by chromic acid; the resulting surface micro-porosity anchors electroless nickel or copper before electrodeposition. A high-impact grade with dispersed rubber particles below approximately 1 µm and uniform distribution can support adhesion measured by peel strength in accordance with ASTM B533. If the rubber phase is excessively coarse or agglomerated, etched surfaces may show pits or non-uniform deposition, causing local adhesion loss after thermal cycling. The processor should verify that the moulded stress state is low; high residual stress from fast filling or low melt temperature can cause local over-etching at gates and weld lines. In injection tooling, weld lines are unavoidable when flow fronts recombine around cored openings. For high-impact ABS, weld-line notched Izod strength can drop to 40 % to 60 % of the un-welded value under ISO 180/A. Gate placement and sequential valve-gate control are therefore more critical than with general-purpose ABS. Surface defects at weld lines cannot be corrected by raising melt temperature alone; increasing melt temperature above 250 °C accelerates butadiene degradation and increases yellowing. Acrylonitrile content also influences chemical resistance; ABS generally resists dilute acids, alkalis and aliphatic hydrocarbons, but is attacked by ketones, esters and chlorinated solvents.

    Assessing Regulatory Data for Electrical and Automotive Submissions

    Unmodified ABS that does not contain brominated flame retardants or heavy-metal pigments can generally meet the restriction on lead, mercury, hexavalent chromium, polybrominated biphenyls and polybrominated diphenyl ethers under EU RoHS Directive 2011/65/EU Annex II, but the producer must issue a material declaration. The cadmium limit is 0.01 wt%; the other restricted substances are limited to 0.1 wt%. Under REACH EC 1907/2006, the supplier should confirm the absence of candidate list SVHCs at above 0.1 wt% in the article, or provide safe-use information. For automotive interior applications, emissions and odour performance should be defined by the OEM against VDA 270, VDA 277 or ISO 12219-1; the grade cannot be assumed to meet low-emission interior specifications without test data. Flammability of unmodified ABS in thin sections is typically UL 94 HB; a V-0 classification at 1.5 mm requires flame-retardant additives or a different polymer system. Food-contact use requires a specific compliance statement; 21 CFR 181.32 addresses acrylonitrile copolymer resins, and EU food-contact migration would require evaluation under Commission Regulation (EU) No 10/2011, with acrylonitrile monomer migration below the applicable specific migration limit.

    Compliance checkpoints for downstream submissions involving unmodified ABS.
    Area Standard or regulation Required material data Document type
    Hazardous substances in electrical equipment 2011/65/EU Annex II Pb, Hg, Cd, Cr(VI), PBB, PBDE by XRF or wet chemistry Supplier RoHS declaration
    SVHC communication EC 1907/2006 REACH Candidate list SVHC content by substance REACH statement
    Flammability UL 94 HB/V tests Thickness, color, minimum ranking UL yellow card or laboratory test report
    Automotive interior emissions VDA 270, VDA 277, ISO 12219-1 Odour grade, total VOC and semi-volatile organic compound values Test report
    Food-contact polymer resin 21 CFR 181.32, EU 10/2011 Monomer migration data and polymer identity Food-contact conformity statement

    For sheet extrusion and thermoforming of ABS H1100 H E, the extruder should be a single-screw machine with a barrier mixing section and L/D of at least 30:1; the flat die temperature should be profiled within 220 °C to 240 °C to maintain melt strength. Polishing rolls are run from 80 °C to 110 °C depending on sheet thickness and gloss. If the grade is pre-dried to below 0.1 wt%, sheet can be thermoformed at surface temperatures of 140 °C to 190 °C; lower temperatures produce excessive drawing stress and post-mould shrinkage, while higher temperatures may cause sagging. The thermoforming mould should be temperature-controlled at 80 °C to 120 °C to achieve consistent wall thickness; unheated moulds promote premature freezing and non-uniform thinning. Because high-impact ABS retains more melt elasticity than general-purpose ABS, die-lip opening and draw ratio should be adjusted through sheet thickness mapping rather than by raising melt temperature alone. Published data for this specific configuration is limited, so the producer’s processing guide remains the controlling document.

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