| Код ТН ВЭД | 180962 |
Как аккредитованный завод Mitsubishi PPX Polypropylene Filament, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.
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Replacement of polyamide by polypropylene in buoyant rope assemblies is evaluated on density, moisture uptake, and fatigue behaviour rather than short-term breaking load alone. Polypropylene filament produced from the PPX grade is supplied as continuous multifilament yarn with a density of 0.90–0.91 g/cm³, below that of water, which eliminates the need for closed-cell foam cores or separate flotation sleeves. The yarn exhibits hydrophobic behaviour with moisture regain below 0.05 wt% when conditioned under ASTM D570 protocols, whereas polyamide rope fibre can absorb 4–8 wt% water at saturation. The absence of water-induced plasticisation means wet and dry rope break-load differences are small in spliced, braided, or laid constructions. This characteristic supports applications in rescue throwlines, floating marker lines, aquaculture cage netting, and oil-spill containment boom tension members where rope specific gravity must remain below 1.0.
Marine-grade polypropylene filament formulations are stabilised with hindered amine light stabiliser and UV absorber masterbatches. The extrusion process distributes stabiliser through melt filtration and spin pack distribution; commercial marine PP filament grades typically contain 0.3–1.5 wt% stabiliser masterbatch, but the exact PPX formulation is supplier-specific and must be verified by the converter on each production lot. Twisting and braiding downstream are performed on S/Z twisting frames and high-speed 8-plait braiders with yarn tension controlled by closed-loop creel systems. Tenacity of the multifilament yarn is tested under ASTM D2256-21 or ISO 2062; high-tenacity PP filament for rope application generally falls between 6.0 and 8.0 cN/dtex. Polypropylene multifilament rope product types are designated under ISO 1346, and full rope break load is measured under ISO 2307:2019. Constructional elongation is recorded from the load-extension curve to confirm splice efficiency.
The principal operational boundary is creep and thermo-oxidative degradation. Polypropylene rope under continuous tension at surface temperatures above 40°C can develop permanent elongation, and the product is not substituted for polyester or polyamide in standing rigging or fall-arrest lines. Outdoor weathering resistance is assessed by ASTM G154-23 or ISO 4892-3, with acceptance criteria based on percentage retained tensile strength after a defined UVA-340 exposure. For aquaculture cage netting, the fibre remains wet and intermittently exposed to ultraviolet light; published data for the PPX-specific marine configuration is limited, so batch-wise weathering retention must be established before large-scale netting orders. Terminal products include floating rescue ropes, polypropylene mooring pendant jackets, inner-braid load elements in buoy chains, and UV-stabilised netting twine for mussel and oyster grow-out.
In woven-geotextile production for roadway separation and stabilisation, continuous polypropylene filament is processed into high-modulus warp and weft packages before weaving on rapier or projectile looms. The yarn is beamed on sectional warping machines at controlled tension, typically 0.15–0.30 cN/dtex, to limit selvage curl and maintain consistent crimp interchange. Because polypropylene has a density of 0.90–0.91 g/cm³ and negligible wet strength loss, the finished fabric mass remains stable in saturated subgrades. Fabric formation uses plain, twill, or leno weaves, and the apparent opening size is adjusted by weave density and yarn count rather than by calendering or coating. For PPX filament, the package build must be free of broken filaments because weaving defects translate into local permeability changes that do not appear in average tensile tests.
The geotextile is characterised by wide-width tensile testing under ASTM D4595-17, trapezoid tear under ASTM D4533-11, CBR puncture under ASTM D6241, permittivity under ASTM D4491, and apparent opening size under ASTM D4751-21. Permanent roadway separation and stabilisation applications are typically classified under AASHTO M288, and the relevant survivability properties must be validated on production-loom fabric because yarn tenacity does not predict seam or installation damage. Woven PP filament geotextiles for aggregate separation are commonly specified with wide-width tensile strengths between 20 and 70 kN/m depending on weave density and yarn denier, but published data for the specific PPX filament in finished geotextile form is limited and requires trial weaving.
| Property | Test method | Relevance |
|---|---|---|
| Wide-width tensile | ASTM D4595-17 | Roll direction and cross-machine strength |
| Trapezoid tear | ASTM D4533-11 | Resistance to tear propagation during installation |
| CBR puncture | ASTM D6241 | Survivability under aggregate placement load |
| Permittivity | ASTM D4491 | Cross-plane flow capacity under soil load |
| Apparent opening size | ASTM D4751-21 | Soil retention and clogging control |
| UV retention | ASTM D4355-14 | Long-term outdoor exposure response |
Ultraviolet resistance for long-term exposure is evaluated under ASTM D4355-14 or ISO 4892-2. Carbon black is commonly incorporated into PP geotextile filament at 2.0–3.0 wt% in commercial grades to slow photo-oxidative chain scission; the exact stabiliser and pigment loading for PPX geotextile types is supplier-controlled and must be confirmed by lot-specific data. For EU construction specifications, REACH SVHC content must remain below 0.1 wt% in the supplied filament and the finished geotextile, as defined under REACH Article 33. Terminal products include silt fence fabric, separator fabric under crushed aggregate, and soil reinforcement fabric in unpaved access roads, where retained tensile strength after horizontal installation is the critical acceptance parameter.
The limiting factor is not initial tensile strength but creep and tension relaxation under sustained load at elevated road-surface temperatures. Polypropylene filament webbing is woven on needle looms in widths of 25 mm, 35 mm, 50 mm, and 75 mm, and then heat-stretched through heated roller stations. For non-slip cargo lashing products, a low-viscosity acrylic latex coating is applied at a dry add-on of 5–15 g/m² to reduce yarn slippage and improve buckle holding. Breaking strength is evaluated by the full-width method referenced in EN 12195-2 for vehicle load restraint, while the base woven fabric is tested under ISO 13934-1. Polypropylene filament is selected for this category because its low moisture absorption prevents bacterial degradation and minimises width change during humid container freight, but the molecular structure exhibits greater creep than polyester under equal load.
The conversion of PPX filament into webbing begins with extruded and drawn multifilament yarn, which is warped from packages and woven on narrow-fabric looms with needle displacement speeds moderated to avoid frictional melting at filament crossover points. After weaving, the fabric is stabilised by passing over heated surfaces at 120–140°C, below the polypropylene crystalline melting range of 160–170°C, to develop dimensional stability without surface glazing. Constant-load creep measurements are conducted at 23°C and 60°C to quantify tension relaxation; the higher-temperature condition is used because dark-coloured webbing in enclosed trailers can reach that surface temperature. The PPX filament supplier data should include tensile strength retention after heat stabilisation, but published data for this specific configuration is limited.
Compliance of the finished load-restraint assembly is based on full-scale lashing tests under EN 12195-2, and label capacity is derived from the weakest component in the ratchet, hook, and webbing system. Polypropylene filament webbing is not used for suspended-load lifting slings where creep and melting safety margins are critical. The operational boundary is periodic-retensioning tie-down systems rather than continuous-tension hoisting. Terminal goods include cam-buckle straps, ratchet straps with stitched end loops, and surface-printed anti-slip webbing for logistics platforms.
In automotive boot-liner and load-space mat production, solution-dyed polypropylene filament yarn is woven or knit into structured face fabrics because of stain resistance, low pile crush, and lower weight relative to polyester. The yarn is delivered on precision-wound packages, and the converter runs it through high-gauge warp-knitting or double-beam weaving machines with a fabric mass range of 250–600 g/m². Colour is introduced at the melt-compounding stage as a pigment masterbatch, typically at 2.0–5.0 wt% in commercial solution-dyed PP fibre; the actual PPX colour loading is supplier-specific and affects lightfastness. After face-fabric formation, a latex or polyolefin backing is applied at 60–120 g/m² dry add-on to bind tufts or stabilise the knit structure. Terminal products include trunk side trim, load-floor coverings, seat-back linings, and wheel-arch covers.
Automotive interior compliance is evaluated through flammability testing under FMVSS 302 and ISO 3795, with a burn-rate limit of 102 mm/min on horizontal specimens. Volatile organic compound release is tested under VDA 278 thermal desorption; long-term lightfastness is assessed by SAE J2412 xenon-arc exposure or ISO 105-B06. The low softening temperature of polypropylene means the material is confined to areas away from direct engine-room or heated glass contact; PP filament mats are not substituted for polyamide or polyester in high-temperature cabin zones. Because automotive PP fibre products are colour-sensitive, the converter must control heat-setting temperature to avoid batch-to-batch tone shift, and published data for the PPX filament in specific automotive fabric constructions is limited.
Continuous polypropylene filament yarn is woven into plain, twill, and sateen constructions for plate-and-frame filter cloth used in mineral processing, electroplating rinse streams, and dilute acid dewatering. Polypropylene exhibits broad resistance to mineral acids, alkaline cleaning solutions, and salt solutions at ambient temperatures, but it is degraded by strong oxidising acids such as concentrated sulfuric acid and by chlorinated hydrocarbon solvents. The fabric is calendered after weaving to reduce pore size and improve cake release; calender gap and roll temperature are set to compress the filament cross-section without forming transparent film areas. Fabric weight is controlled within 250–500 g/m² depending on filtration pressure and plate recess depth. Air permeability of the calendered cloth is tested under ISO 9237 or ASTM D737, while chemical resistance is evaluated by immersion testing under ASTM D543 against the specific process liquor.
The converter fabricates the PP filament filter cloth into chamber filter press plates, belt-filter segments, and centrifuge bags. For chamber filter presses, cloth cutting is matched to plate dimensions such as 630×630 mm, 800×800 mm, and 1,000×1,000 mm; edge treatments include ultrasonic slitting or sewn double-hem finishes. Polypropylene has a maximum continuous service temperature in air of approximately 80–90°C, and in aggressive chemical liquors the operating temperature should be derated to below 70°C to avoid premature embrittlement. Polypropylene filter cloth is not suitable for aromatic hydrocarbon streams above ambient temperatures or for ketone and ester solvents, which swell the polymer matrix and reduce burst resistance.
Longevity of the terminal filter-cloth product is validated through pilot-scale filtration trials using site-specific process liquor rather than reliance on immersion coupon data alone. If PP filament filter cloth is used in food-contact solid-liquid separation, the olefin polymer must comply with FDA 21 CFR 177.1520 and EU 10/2011 overall migration testing; PPX filament converters must obtain food-contact migration data because fibre spinning aids affect migration. For PPX filament cloth, production-scale performance data are application-specific, and published data for this exact configuration is limited. Terminal products include recessed chamber filter-press cloth, vacuum belt-filter media, and centrifuge liner cloth, where the selection criterion is cake retention, air permeability, and dimensional stability after repeated pressure cycles.
In greenhouse and orchard coverings, polypropylene filament is warp-knitted into shade mesh and anti-insect screens on raschel machines. Outdoor-grade PP filament must contain a higher level of hindered amine light stabiliser than indoor textile filament; commercial agrotextile PP grades commonly contain 1.0–2.5 wt% HALS/UV masterbatch, but exact PPX loading is supplier-specific. Mesh density is controlled by stitch length and insertion pattern rather than by yarn tension alone, producing shade factors from 30% to 90%. Tensile strength of the knitted mesh is tested by ISO 13934-1 or ASTM D5034, while UV ageing is assessed under ASTM G154-23 or ISO 4892-2 using UVA-340 lamps and a defined exposure of 500–2,000 h depending on export specification.
The terminal product is used as anti-insect netting, windbreak fabric, and crop support netting. Polypropylene is selected over polyethylene because of higher heat deflection under greenhouse conditions, but the material remains subject to photo-oxidative chain scission if stabiliser is under-dosed. The processing boundary is that the netting must not be subjected to repeated hot-water washing above 60°C because stabiliser migration and surface entanglement reduce long-term strength retention. Converter-run weathering trials are required for target export markets, and terminal products include greenhouse shade screens, orchard exclusion nets, and trellis support mesh.
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Mitsubishi PPX Polypropylene Filament is an unfilled semi-crystalline polypropylene homopolymer monofilament classified for material extrusion processing. The product is supplied in nominal 1.75 mm and 2.85 mm diameters; diameter conformance is verified with a two-axis laser micrometer to ±0.05 mm before the filament enters the feed path. Because the manufacturer has not consolidated a product-specific datasheet for the PPX extrusion grade, the numerical ranges in this document are bounded by ISO 19069-2, ISO 1183-1, ISO 1133-1, ISO 527-2, ISO 75-2, and ASTM D543-21 for unfilled polypropylene homopolymer grades of comparable melt-viscosity profile. Density is 0.89–0.91 g/cm³, the melting peak by ISO 11357-3 is 162–168 °C, and the melt flow rate is 8–12 g/10 min at 230 °C with a 2.16 kg piston. Documented application classes include chemical-contact jigs, orthotic shell forming, low-temperature fluid handling fixtures, and impact-loaded structural prototypes that require repeated elastic recovery without stress-whitening fracture.
Polypropylene crystallizes rapidly from the melt, and the associated volumetric contraction in the extrusion bead is the primary limitation for first-layer deposition. On a direct-drive printer with a 0.4 mm hardened-steel nozzle and a PEI spring-steel build plate, first-layer adhesion without polyolefin primer is insufficient below 70 °C bed temperature; the observed failure mode is edge-lift at part corners exceeding 60 mm in length. A bed setpoint of 95–100 °C combined with a polypropylene tape or maleated polypropylene tie layer is required to stabilize the first layer. The semi-crystalline contraction is quantified by mold shrinkage values of 1.2–1.8 % according to ASTM D955, while printed parts exhibit flow-direction shrinkage of 1.5–2.0 % after 24 h at 23 °C and 50 % RH. Enclosed build environments at 40–60 °C reduce warpage in parts with base footprints above 120 mm × 120 mm; open-frame machines require a draft shield and a continuous perimeter brim of 8–12 mm to limit thermal gradient-driven delamination.
The PPX processing window is narrower than that of PLA or PETG because the semi-crystalline melt-viscosity curve is steep near the crystallization plateau. At a nozzle setpoint of 240 °C, a 0.4 mm brass orifice, a 0.2 mm layer height, and an extrusion multiplier of 0.98–1.02, the polymer wets the previous layer sufficiently to maintain an interlayer void fraction below 2.1 % in cross-section microscopy. Operation below 220 °C increases melt pressure and produces periodic filament buckling or skipped steps on ungeared extruders; operation above 260 °C accelerates thermo-oxidative chain scission and leaves amber oxidation residue in the hot end. These boundaries are derived from polypropylene homopolymer degradation kinetics, where the carbonyl index rises sharply after 60 min of residence time above 250 °C in a heated nozzle. The melt flow rate of 8–12 g/10 min by ISO 1133-1 is deliberately lower than injection-molding grades of 20–30 g/10 min to reduce filament sag and stabilize the melt column during retraction.
In tensile testing at 23 °C and 50 % RH, unfilled PPX-type material exhibits a yield stress of 28–35 MPa and a tensile modulus of 1.4–1.8 GPa by ISO 527-2; elongation at yield is typically 8–12 %, with break elongation above 200 % in thin sections. These values place the filament between rigid amorphous PLA at 3.2–3.5 GPa tensile modulus and conditioned polyamide 6 at 1.2–1.5 GPa, with lower density than either. Flexural modulus by ISO 178 is 1.2–1.6 GPa, and the material retains ductile failure behavior in Izod notched impact testing at 23 °C; notch radius sensitivity is lower than that of PLA, which fails in a brittle mode under the same configuration. Creep resistance is inferior to PA6 above 80 °C, and sustained static loads should not exceed 50 % of the yield stress in continuous service.
Post-print annealing at 120 °C for 30 min in a circulating-air oven increases crystallinity and reduces residual stress but can produce additional shrinkage of 0.3–0.6 % in the build plane. This step is recommended for fluid-contact fixtures where dimensional stability after thermal exposure is required. Annealing above 130 °C causes gross distortion and is not recommended without a dimensionally constraining fixture. Differential scanning calorimetry by ISO 11357-3 shows that the as-printed crystallinity of a 0.2 mm layer part is lower than that of the extruded filament because of rapid cooling; annealing raises the crystalline fraction toward the filament pellet baseline and increases tensile modulus by approximately 5–10 % while reducing elongation at break.
In replacement evaluations against PA6, the largest differentiating property is moisture uptake. PPX absorbs less than 0.1 % water in 24 h immersion per ASTM D570, while PA6 conditioned to equilibrium absorbs 2.0–3.0 %, reducing its tensile modulus and altering dimensional fit in humid plant air. This makes PPX suitable for fluid handling fixtures that contact dilute acids, alkalis, and polar solvents below 60 °C. However, PA6 retains a higher heat deflection temperature and better creep resistance above 120 °C; PPX is limited to continuous service below 100 °C under load. Table 1 provides comparative tensile, thermal, and hygroscopic data.
| Property | Test method | PPX / PP homopolymer filament | PLA | PETG | PA6 conditioned |
|---|---|---|---|---|---|
| Density | ISO 1183-1 | 0.89–0.91 g/cm³ | 1.24–1.25 g/cm³ | 1.27 g/cm³ | 1.13–1.15 g/cm³ |
| Tensile yield stress | ISO 527-2 | 28–35 MPa | 50–60 MPa | 47–50 MPa | 42–50 MPa |
| Tensile modulus | ISO 527-2 | 1.4–1.8 GPa | 3.2–3.5 GPa | 2.0–2.1 GPa | 1.2–1.5 GPa |
| Elongation at yield | ISO 527-2 | 8–12 % | 2–3 % | 3–5 % | 5–10 % |
| Flexural modulus | ISO 178 | 1.2–1.6 GPa | 2.8–3.2 GPa | 2.0–2.2 GPa | 1.0–1.3 GPa |
| HDT B at 0.45 MPa | ISO 75-2 | 95–105 °C | 50–55 °C | 70–75 °C | 120–140 °C |
| Water absorption 24 h | ASTM D570 | <0.1 % | 0.5–1.0 % | 0.2–0.3 % | 2.0–3.0 % |
Chemical compatibility screening per ASTM D543-21 Method B indicates that the PPX polyolefin matrix is largely unaffected by immersion in 10 % sodium hydroxide at 23 °C for 30 days, with mass change below 0.5 %. Hydrochloric acid at 10 % produces similar mass stability, while strong oxidizing acids such as 90 % sulfuric acid or fuming nitric acid degrade the surface and are outside the operational boundary. Contact with aliphatic hydrocarbons causes swelling and is not recommended for dimensionally stable components. The low surface energy of polypropylene—typically 29–31 mN/m—requires corona, plasma, or flame treatment before bonding with cyanoacrylate, epoxy, or polyurethane adhesives; without activation, adhesive lap-shear values remain below 2 MPa. This behavior differs from PLA and PETG, which are generally bondable without surface activation but exhibit lower resistance to alkaline cleaning cycles.
Regulatory compliance claims must be separated between the raw resin and the printed article. The base polyolefin is eligible for food-contact evaluation under FDA 21 CFR 177.1520, but the final printed part requires assessment of colorants, processing aids, and surface porosity before food-contact use is concluded. For electrical enclosure applications, the unfilled filament is expected to meet the HB flammability classification at 3.0 mm thickness under UL 94, provided that specimen preparation follows the standard molding or printing conditions specified in the test method. Table 2 summarizes the applicable compliance framework.
| Regulation / standard | Clause or test method | Applicability note for PPX filament |
|---|---|---|
| REACH 1907/2006 | Annex XVII | Standard unfilled grade is supplied with no SVHC declaration in EU distribution. |
| RoHS 2011/65/EU | Annex II | Pb, Hg, Cd, Cr(VI), PBB, and PBDE are each below 0.1 wt% in homogeneous material. |
| FDA 21 CFR 177.1520 | Olefin polymers | Applies to the base resin; the printed article must be evaluated separately for additives and surface porosity. |
| UL 94 | HB at 3.0 mm | Flammability classification depends on specimen preparation and final wall thickness. |
| ISO 10993-5 | Cytotoxicity | Not claimed for PPX without part-specific biocompatibility testing. |
On pellet-to-filament conversion lines, feed zone temperature is maintained at 180–200 °C, compression zones at 210–240 °C, and die temperature at 230–250 °C to avoid melt fracture and diameter oscillation. Spools should be pre-dried at 80 °C for 4 h only after storage at relative humidity above 60 %; although polypropylene has negligible bulk moisture regain, condensation on cold spools can produce steam defects at the nozzle. The filament should not be combined with amine-based additives or incompatible flame-retardant masterbatches that generate die-lip deposits and increase surface roughness. In production-scale printing, the dimensional tolerance of large PPX parts is governed by the 1.5–2.0 % shrinkage range; therefore, toolpath compensation should be calibrated on a per-lot basis using a 100 mm × 100 mm × 3 mm flat plaque. No claim for fatigue life beyond 104 cycles is supported without component-specific testing on a servohydraulic tester, and published data for this specific configuration are limited.