| Код ТН ВЭД | 929955 |
Как аккредитованный завод Mitsubishi HIPS 3D Printing Filament, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.
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Mitsubishi HIPS 3D printing filament is a high-impact polystyrene feedstock with a density of approximately 1.03–1.06 g/cm³ measured under ISO 1183-1 and a Vicat softening temperature generally reported between 95°C and 105°C under ISO 306. The material is supplied as a compounded filament rather than a raw resin, and downstream reprocessing on twin-screw equipment is limited; if regrind must be re-extruded, a co-rotating twin-screw extruder with L/D ratio of 36:1 to 44:1 and a barrel temperature profile from 180°C to 220°C is required to avoid rubber-phase agglomeration. Applications are restricted to fused filament fabrication, sacrificial support, and low-temperature tooling because the heat deflection temperature under 1.82 MPa is not suitable for service above 85°C. Each scenario below treats the filament as a stoichiometrically trackable raw material with defined addition fractions, process limits, and compliance anchors. Where published data for this specific Mitsubishi filament grade is unavailable, the limitation is stated explicitly rather than extrapolated.
| Application zone | HIPS addition fraction | Primary process window | Anchoring standards |
|---|---|---|---|
| Automotive prototype support and jigs | 12–30 wt% support; 100% solid jig | 220–240°C HIPS; chamber 90–110°C | ISO 9001:2015, ELV 2000/53/EC, REACH Article 33 |
| Medical device form/fit models | 100% virgin; 8–15 vol% support | 225–235°C; bed 100–110°C | ISO 13485:2016, ISO 14971:2019, ISO 10993-1:2018 limitation |
| Thermoforming tool inserts | 100% HIPS shell; 45–60% infill | 240–250°C; chamber 70–85°C | ISO 9001:2015, EU 10/2011, FDA 21 CFR 177.1640 |
| Soluble support for ABS/ASA | 15–35 vol% HIPS support | 230–245°C HIPS; solvent 55–65°C | ASTM D638-14, ISO 527-2:2012, RoHS 2011/65/EU |
| Architectural models | 100% HIPS; 10–25% infill | 235–245°C; layer 0.3 mm | RoHS 2011/65/EU, REACH Article 33 |
| Laboratory test specimens | 100% HIPS; regrind ≤ 10 wt% | 235°C; layer 0.1 mm; 100% solid | ASTM D638-14, ASTM D256-10, ISO 178:2019 |
On automotive FDM lines where ABS or ASA is the primary build material, Mitsubishi HIPS filament is allocated to two discrete functions: sacrificial support for enclosed duct geometries and solid low-load assembly aids such as CMM fixture plates. In the support function, the HIPS addition fraction is governed by toolpath contact area and typically falls between 12 wt% and 30 wt% of the total build mass; when a fixture base is printed as a solid HIPS body, the infill is set to 100% with five perimeter walls. The governing compliance framework for these non-vehicle prototype aids includes ISO 9001:2015 clause 8.5.1 for production process control, REACH Article 33 for SVHC communication, and ELV 2000/53/EC for end-of-life disposal obligations when prototype components are later treated as vehicle-derived waste; IATF 16949:2016 PPAP documentation is not required for tooling-only parts but is often retained for dimensional study traceability. Processing on a dual-extruder industrial FDM system with a heated chamber at 90–110°C requires separate temperature management because the HIPS filament is extruded at 220–240°C while the ABS or ASA body is deposited at 245–265°C; this 25–45°C melt-flow mismatch is controlled by limiting HIPS support print speed to 25–35 mm/s and increasing prime volume after retraction to 1.2 mm. Support removal is performed in D-limonene at 60°C for 4–8 h with ultrasonic agitation at 40 kHz; blind channels with diameters below 3 mm and support widths below 0.8 mm frequently retain gel residue, and these configurations require a minimum channel-to-support area ratio of 3:1 to avoid destructive rework. Terminal part types include HVAC duct prototypes, throttle-body adapter models, drill jigs, CMM holding bases, and assembly sequence training aids; these components are not installed on production vehicles and therefore do not require FMVSS or ECE material certification.
In medical device development, Mitsubishi HIPS filament is confined to non-sterile form, fit, and usability models that do not contact breached skin, mucosal tissue, or blood. The feedstock is printed at 100% virgin HIPS with zero regrind addition; when removable support is unavoidable, the HIPS support fraction is held between 8 vol% and 15 vol% of the total build to limit solvent residue in enclosed lumen features after D-limonene extraction. Compliance documentation follows ISO 13485:2016 clause 7.3.6 for design and development verification and ISO 14971:2019 for prototype risk control, but the filament is not declared to satisfy ISO 10993-1:2018 biocompatibility endpoints, so any printed part that intentionally enters a patient-contact zone must be treated as contaminated and segregated. The production process uses a direct-drive FDM extruder with a 0.25 mm or 0.4 mm nozzle, a melt temperature of 225–235°C, and a heated bed at 100–110°C on polyimide tape that has been pre-coated with a dilute HIPS-limonene adhesion layer. After printing, parts are conditioned at 23°C and 50% RH for 24 h and then inspected against ISO 2768-1 general tolerances; annealing at 80°C for 2 h can reduce residual stress but introduces Z-axis shrinkage of 0.3–0.7%, which must be compensated in the CAD model. Batch-to-batch viscosity drift above 5% has been observed on some FDM lines and is sufficient to alter snap-fit engagement force, so lot-to-lot melt flow documentation is retained under ISO 13485 clause 7.5.9 for traceability. Finished output categories include diagnostic instrument housing mockups, handheld device grip and bezel prototypes, and CT-derived anatomical visualization aids for surgical planning teams; these items are not CE-marked medical devices under MDR 2017/745.
Short-run thermoforming development consumes Mitsubishi HIPS filament as a printed cavity plug, vacuum box insert, or try-out form block only when the working mold surface remains below 80°C. The addition ratio is 100% HIPS filament with a 45–60% triangular infill shell; compounding of mineral fillers above 5 wt% is not recommended because the resulting melt viscosity exceeds the torque limit of a standard 0.4 mm hot end and causes extruder skip. Compliance for non-food packaging prototypes is governed by ISO 9001:2015, while direct food-contact tooling trials require migration testing under EU 10/2011 Annex III and FDA 21 CFR 177.1640 for polystyrene; the filament lot certificate must confirm that residual monomer and additive packages meet the relevant migration thresholds before any food-contact trial. The downstream process uses a Cartesian FDM printer with an actively heated chamber at 70–85°C, printing at 240–250°C melt temperature, 0.2 mm layer height, and a 0.4 mm hardened nozzle; after printing, the cavity surface is vapour-polished in a closed chamber with a 70/30 vol/vol blend of methyl ethyl ketone and ethyl acetate for 10–15 min, then cured at 40°C for 6 h to allow solvent egress. Operational boundaries include a maximum thermoforming sheet gauge of 1.0 mm and an exclusion of polycarbonate sheet because its forming temperature exceeds the HIPS heat deflection threshold and causes cavity surface collapse. Terminal products are prototype blister cavities, tray-forming inserts, and small-batch thermoforming tools capable of 50–200 cycles before the HIPS surface shows microcracking; published data for Mitsubishi-specific HIPS tool life is limited.
Dissolution-based support removal using D-limonene introduces a processing conflict in dual-extruder production: the same solvent that removes HIPS support at 55–65°C begins to swell ABS or ASA thin walls after prolonged immersion beyond 8 h, producing surface microcracks on sections below 2.0 mm. Mitsubishi HIPS filament is apportioned as a sacrificial medium at 15–35 vol% of total build volume, while the primary engineering material is a production-grade ABS or ASA filament deposited at 250–265°C; the HIPS extruder is maintained at 230–245°C with retraction distance 1.2 mm and prime speed 25 mm/s to reduce stringing and interface contamination. The applicable standards are ASTM D638-14 for tensile property verification of the ABS or ASA body after support removal, ISO 527-2:2012 for equivalent tensile methodology, RoHS 2011/65/EU for restricted substances in electronics-related end parts, and REACH Annex XVII for solvent handling and exposure control in the dissolution step. The downstream process runs on an industrial dual-extruder FDM machine with a heated chamber at 90–100°C and a glass or PEI build plate; after build completion, the part is immersed in recirculating D-limonene at 55–65°C for 4–12 h, rinsed in isopropyl alcohol at 23°C for 30 min, and dried in a vacuum oven at 50°C for 2 h. Internal channels below 3 mm diameter exhibit diffusion-limited dissolution, and residual HIPS gel may persist after 12 h if the support width is below 0.8 mm; a minimum channel-to-support area ratio of 3:1 is therefore specified for enclosed manifolds. Terminal part types include pneumatic manifold prototypes, wiring harness routing aids, electronics enclosure prototypes with internal snap features, and appliance ductwork prototypes; service temperature is restricted below 80°C because retained D-limonene plasticizes the matrix and reduces tensile modulus.
Architectural scale models consume Mitsubishi HIPS filament as a monolithic shell material rather than a support medium, selected for low mass in large-format prints and the ability to be solvent-welded with HIPS cement. The formulation is 100% HIPS with infill densities between 10% and 25% for massing models; for facade blocks that require module joining, a cement of 3–5 wt% HIPS dissolved in D-limonene is used, with a gel time of 15–20 min at 23°C. Compliance is limited to RoHS 2011/65/EU and REACH Article 33 SVHC communication; building code classifications under ASTM E84 or EN 13501-1 are not applicable because the models are non-structural display pieces with temporary service life. The process employs a large-format FDM printer with a 0.6 mm or 0.8 mm nozzle, a melt temperature of 235–245°C, a bed temperature of 100–110°C, and a layer height of 0.3 mm; after printing, surfaces are sanded at 120–240 grit and vapour-smoothed with methyl ethyl ketone in a sealed chamber for 5–8 min, followed by forced-air drying at 25°C for 12 h. Thin vertical walls below 1.5 mm are prone to warpage when the build chamber is not heated above 60°C. Terminal end products include urban master-plan models, facade mockups, and exhibition display components; these models are not fire-rated and must be kept away from open flame or high-intensity halogen lighting that could raise surface temperature above the HIPS softening point.
Laboratory-scale mechanical testing of printed HIPS specimens requires raster orientation control because measured properties shift by 25–40% between longitudinal and transverse build axes. The filament is used at 100% virgin HIPS; addition of regrind from failed prints is not recommended above 10 wt% because contamination from D-limonene-treated support fragments lowers interlayer adhesion and increases void density. Compliance is anchored to ASTM D638-14 Type I geometry for tensile testing, ASTM D256-10 for Izod impact, ISO 527-2:2012 for comparative tensile modulus, and ISO 178:2019 for flexural tests; each test report must record infill density and raster angle because these variables are absent from injection-molding standards. The downstream production process uses an open-chamber FDM printer with a 0.4 mm hardened nozzle, 0.1 mm layer height, 235°C extrusion temperature, and 105°C bed temperature; specimens are printed with 100% solid infill, five perimeter shells, and alternating ±45° or 0/90° raster angles per layer. In comparison, injection-molded HIPS reference samples produced on a hydraulic machine with 800 kN clamp force exhibit higher density and no raster boundaries, so FDM test results should not be substituted for molded-material datasheets without explicit correlation. Printed coupons are conditioned at 23°C and 50% RH for 48 h before testing; published data for this specific Mitsubishi HIPS filament grade is limited, so interlaboratory repeatability must be verified internally. End product types include student tensile coupons, research-grade Izod impact bars, and comparative benchmark shapes for materials science courses; these specimens are not used for code-based qualification of production parts.
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Mitsubishi HIPS 3D Printing Filament is a rubber-modified polystyrene monofilament produced for fused filament fabrication and supplied in 1.75 mm and 2.85 mm nominal diameters. The product is distributed through Mitsubishi Chemical’s Verbatim brand and is used primarily as a soluble support material for ABS and ASA build platforms, though it also serves as a low-density, impact-toughened prototyping material. HIPS consists of a continuous polystyrene matrix and discrete polybutadiene-rich domains, typically 7–12 wt% rubber, which shift failure from brittle crazing to shear yielding while retaining solvent processability. Production spools are controlled to ±0.05 mm diameter tolerance, with ovality generally below 0.03 mm. Recommended extrusion is 220–250 °C through a 0.4 mm nozzle, with heated-bed settings between 90 °C and 110 °C. Spool formats include 500 g and 1 kg net weights. The manufacturer material designation is HIPS; distributor-specific stock keeping units vary by region. Where the exact Mitsubishi datasheet omits a value, representative HIPS FFF-grade data are cited against the applicable test standards below.
On industrial compounding lines, HIPS resin is produced by bulk or suspension polymerization of styrene in the presence of dissolved polybutadiene, followed by phase inversion that yields rubber particle sizes controlled to 0.5–2.0 µm. Filament is then melt-spun on single-screw extruders with L/D ratios of 24:1 to 30:1, with closed-loop laser micrometry regulating diameter. Batch-to-batch melt flow variation is typically held within ±0.8 g/10 min when certified under ISO 1133-1:2022. That variation is narrow enough to preserve layer width on a 0.4 mm nozzle, though high-volume multi-nozzle production lines may require ±3–5% flow-rate compensation when switching spool lots.
Melt processing is controlled by the two-phase morphology. The polystyrene continuous phase provides stiffness and d-limonene permeability, while the polybutadiene-rich islands increase melt elasticity and die swell. Under capillary rheometry per ISO 11443:2021, HIPS FFF grades commonly show apparent shear viscosities of 150–350 Pa·s at 230 °C and 100 s−1; exact Mitsubishi lots may fall outside this band. The elastic component raises nozzle pressure drop by roughly 15–30% relative to PLA at equivalent volumetric throughput. Interlayer fusion is the limiting structural variable. Printed Z-direction tensile strength is frequently reported between 18 MPa and 24 MPa, or 70–85% of XY strength, for 0.2 mm-layer specimens tested under ASTM D638-14. Below 220 °C, melt diffusion between deposited strands slows and interlayer boundaries remain visible in cross-section. Above 260 °C, thermo-oxidative degradation of unsaturated rubber domains accelerates, producing yellowing, styrenic odor, and char accumulation on the nozzle seat. A chamber or enclosure maintained above 60 °C reduces edge lift, while nozzle idle time at 250 °C should not exceed 20 min without purging.
Moisture absorption in a spool exposed to relative humidity above 60% is slow but not negligible. Pre-drying in a forced-air oven at 70 °C for 4 h, or in a vacuum oven at 60 °C for 2 h, is recommended when surface haze, steam popping, or intermittent under-extrusion appears. Drying above 80 °C risks spool-core deformation because the heat deflection temperature of the filament can fall below the drying setpoint. In a controlled room at 35–50% RH, open spool exposure for 24–48 h does not typically require drying. Cold-to-warm transfer condensation produces surface water that becomes steam vacuoles in the extrudate and directly reduces interlayer strength.
HIPS dissolves selectively in d-limonene because the nonpolar cyclic monoterpene plasticizes the polystyrene continuous phase. The polybutadiene-rich domains swell rather than fully dissolve, leaving a filtered gel residue in the bath. Recommended bath temperature is 40–50 °C under ultrasonic or mechanical agitation. A 2 mm-thick HIPS wall may dissolve in 30–60 min, while dense support packing in a closed cavity can require 2–6 h or longer. Dissolution is mass-transfer-limited: increasing agitation lowers the boundary layer, but saturated solvent near the part slows removal. D-limonene has a flash point near 48 °C, so open baths must be ventilated and heated below 60 °C. Nitrile and natural rubber seals swell in d-limonene; stainless steel or high-density polyethylene containers are preferred. Compared with PVA support, HIPS remains dimensionally stable in dry ABS chambers, whereas PVA can absorb moisture and soften during extended dual-nozzle builds. The penalty is solvent handling, residue rinsing with isopropanol, and longer removal times. Published data for this specific Mitsubishi product in agitated d-limonene baths is limited; users should validate removal time on a sacrificial lattice because geometry, bath flow, and solvent loading dominate the rate.
Direct-drive extruders with all-metal hot ends are preferred for this material. A conservative starting condition is 240 °C nozzle temperature, 0.4 mm hardened steel nozzle, print speed of 40–60 mm/s, and bed temperature of 105 °C. Raising speed above 80 mm/s may require 250–260 °C to keep melt viscosity within the hot-end volumetric capacity. Heated-bed adhesion drops sharply below 90 °C on bare glass and PEI film, particularly without an enclosure. Part-cooling fans should remain below 20–30% duty cycle to prevent interlayer delamination. Retraction settings are geometry-dependent: 3–5 mm on Bowden systems and 0.8–1.2 mm on direct drivetrains reduce stringing without causing nozzle clogging. A chamber temperature of 50–65 °C is effective for large ABS-HIPS dual-material parts.
Diameter excursions above +0.05 mm create visible horizontal banding because cross-sectional area scales with the square of diameter. A shift from 1.75 mm to 1.80 mm increases feed volume by approximately 5.8% at constant feed length. Production users often verify each shipment with a 20 mm calibration cube and a continuous 50 m length measured by weight. On multi-nozzle arrays, uncalibrated spool-feed tension above 10 N can permanently deform HIPS and create periodic diameter reduction at the capstan. Melt stability is assessed by melt mass-flow rate under ISO 1133-1:2022. Regulatory compliance for electrical and electronic applications is anchored to RoHS Directive 2011/65/EU Annex II, including Delegated Directive (EU) 2015/863 phthalate restrictions. REACH compliance is declared at the distributor level under EC 1907/2006 for articles containing no substances of very high concern above 0.1 wt%. Food-contact use is not automatic: rubber-modified polystyrene may be compliant with FDA 21 CFR 177.1640 when the base resin is manufactured for food-contact use, but printed surfaces are not cleared without porosity, printer contamination, and migration testing.
| Property | Test method | Representative value |
|---|---|---|
| Diameter tolerance | Laser micrometry | ±0.05 mm |
| Density | ISO 1183-1:2019 | 1.04–1.06 g/cm³ |
| Melt mass-flow rate | ISO 1133-1:2022, 200 °C, 5 kg | 4–8 g/10 min |
| Tensile strength at yield | ISO 527-2:2012 Type 1A, 50 mm/min | 22–30 MPa |
| Tensile modulus | ISO 527-2:2012 | 1.8–2.2 GPa |
| Flexural strength | ISO 178:2019, 2 mm/min | 40–50 MPa |
| Heat deflection temperature | ISO 75-2:2013, method A, 1.80 MPa | 75–82 °C |
| Heat deflection temperature | ISO 75-2:2013, method B, 0.45 MPa | 88–96 °C |
| Vicat softening temperature | ISO 306:2022, A50 | 96–102 °C |
The decisive process difference is solvent selectivity. PVA dissolves in water at 20–30 °C but requires desiccated storage below 10% RH; HIPS dissolves in d-limonene at 40–50 °C and remains usable in dry ABS chambers. Breakaway supports rely on weak interfacial adhesion and mechanical fracture, leaving witness marks in internal channels. HIPS provides soluble extraction in closed cavities where breakaway access is impossible. Compared with ABS build material, HIPS has lower tensile modulus and heat deflection temperature but a similar linear-shrinkage coefficient, typically 0.4–0.7% in XY for printed parts versus 0.6–0.9% for ABS. This thermal-shrinkage match keeps the support interface attached during chamber cooling without imposing excessive adhesion. Melt flow of Mitsubishi HIPS is usually higher than general-purpose ABS, reducing extruder torque but increasing stringing tendency if retraction is not recalibrated.
| Parameter | HIPS | PVA | Breakaway PLA blend |
|---|---|---|---|
| Removal medium | D-limonene | Water | Mechanical fracture |
| Storage humidity limit | <60% RH | <10% RH | <50% RH |
| Typical extrusion temperature | 230–250 °C | 190–220 °C | 190–220 °C |
| Bed temperature | 90–110 °C | 40–60 °C | 40–60 °C |
| Build material compatibility | ABS, ASA | PLA, PETG, ABS | PLA, ABS |
| Tensile strength | 22–30 MPa | 30–40 MPa | 35–45 MPa |
Do not combine HIPS with polycarbonate support interfaces in a dual-nozzle build, because the bed temperatures required for polycarbonate exceed the practical upper standing temperature of HIPS and produce local support degradation. D-limonene baths should remain below 60 °C in open vessels, with ventilation and stainless steel or high-density polyethylene containment. Swollen polybutadiene gel should be filtered from the solvent bath to avoid deposition on downstream parts. After support removal, printed surfaces must be rinsed with isopropanol and dried before bonding or painting. The material is not recommended for continuous load-bearing service above 70 °C, because creep modulus falls rapidly near the heat deflection temperature. Ultraviolet exposure produces yellowing and surface crazing; the product is not formulated for long-term outdoor weatherability. In production rooms above 60% RH, pre-drying is mandatory and the spool should be fed from a heated dry box maintained at 40 °C.