Products

Polyram PlusTek PD100 Nylon 12, Injection Molding

    • Product Name: Polyram PlusTek PD100 Nylon 12, Injection Molding
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    Specifications
    HS Code 409784
    Density 1.01 g/cm³
    Tensile Strength At Yield 45 MPa
    Elongation At Break 250 %
    Flexural Modulus 1200 MPa
    Izod Impact Notched 23 C 8 kJ/m²
    Heat Deflection Temperature 0 45 Mpa 140 °C
    Heat Deflection Temperature 1 8 Mpa 55 °C
    Melting Point 178 °C
    Water Absorption Saturation 1.5 %
    Mold Shrinkage 1.5 %
    Volume Resistivity 1e14 Ohm·cm
    Dielectric Strength 30 kV/mm

    As an accredited Polyram PlusTek PD100 Nylon 12, Injection Molding factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged in 25 kg sealed, moisture-resistant bags as natural nylon 12 pellets for injection molding use.
    Container Loading (20′ FCL) 20′ FCL of Polyram PlusTek PD100 Nylon 12 pellets, packed in sealed bags on pallets, secured for injection molding shipment.
    Shipping Polyram PlusTek PD100 Nylon 12 is shipped as dry, sealed pellets in moisture-barrier bags or drums. Protect from humidity, direct sunlight, and excessive heat during transport. Handle carefully to prevent bag damage. Non-hazardous, but follow standard industrial hygiene practices and consult the Safety Data Sheet for safe handling and storage.
    Storage Store Polyram PlusTek PD100 Nylon 12 in its original, sealed packaging in a cool, dry, well-ventilated area. Protect from direct sunlight, heat sources, and excessive humidity to prevent moisture absorption. Keep away from strong oxidizers. Recommended storage temperature is below 30°C. Under these conditions, material retains quality for up to one year.
    Shelf Life Shelf life is typically 2 years when stored unopened in a cool, dry place, protected from moisture and sunlight.
    Application of Polyram PlusTek PD100 Nylon 12, Injection Molding

    In fuel vapor management systems for gasoline and flex-fuel passenger vehicles, quick connectors, retainer clips, and mounting brackets are molded from unreinforced nylon 12 where resistance to aromatic hydrocarbons, ethanol blends, and calcium chloride brine outweighs the higher tensile strength of glass-filled polyamides. The Polyram PlusTek PD100 feed is dried in a closed-loop desiccant dryer at 80 °C to a residual moisture of 0.08 wt% or lower; processors operating hot-air hopper dryers observe intermittent surface splay when floor relative humidity exceeds 60 % and dried material remains in open convey lines for more than 4 h. Melt temperature is maintained at 235–250 °C by immersion probe measurement, and hot runner manifold temperature is limited to 5 °C above the screw tip. Mold temperature is held at 40–60 °C; injection velocity is 150–250 mm/s; holding pressure is profiled from 45 MPa to 65 MPa for a 30 mm screw. Carbon black masterbatch is added at 2.0–2.5 wt% for underhood UV and thermal oxidative stabilization; addition above 3.0 wt% produces a measurable drop in notched impact strength under ISO 179-1/1eA because pigment agglomerates concentrate stress at gate vestiges. Regrind from sprues and runners is limited to 15 wt%; higher fractions increase the standard deviation of latch arm pull-out force and reduce melt flow stability at thin crossing points. Components are tested under SAE J2044 for fuel system quick connectors and under ISO 19069-2 for lot traceability and molding material characterization. The primary production line failure mode in this segment is not tensile overload but environmental stress cracking at gate vestiges after exposure to E10 fuel and zinc chloride road salt; this is controlled by polishing gate remnants to 0.05 mm maximum height and eliminating sharp transitions at latch arm roots. Published data for PD100 under CARB LEV III evaporative emission cycles is limited to assembly-level validation rather than raw resin plaques.

    Tooling for this segment uses hot sprue bushings and submarine gates into non-sealing surfaces; gate diameters are kept at 60–80 % of the adjoining wall thickness to avoid jetting. Incoming lots are checked for melt volume-flow rate under ISO 1133-1:2022; processors maintain a lot-to-lot MVR control chart, and a shift of more than 10 % triggers gate freeze-time adjustment and retesting of latch arm deflection. On multi-cavity production tools, the runner system is balanced to a fill time variation below 0.2 s, because unbalanced cavities create inconsistent residual stress and change the load-deflection curve of the retaining clip. Mold release agents are prohibited because they migrate to the connector surface and reduce the coefficient of friction required for SAE J2044 retention force; ejection is instead managed by 1 ° to 3 ° draft and textured surfaces only on non-latching regions. Drying audits are performed with a moisture analyzer at 160 °C; material measured above 0.10 wt% is rejected for this application because thin latch arms below 0.8 mm wall thickness show brittle failure when molded with damp resin. These tooling and drying controls are standard on production lines where fuel quick connector insertion force is monitored by an inline load cell with an acceptance band derived from the vehicle manufacturer’s assembly specification.

    What Limits Regrind Content in Pneumatic Push-In Fittings?

    Pneumatic push-in fittings, distribution blocks, and flow control valve bodies require thread-root radii, collet retention windows, and internal bore tolerances that are extremely sensitive to melt viscosity drift. The governing compliance framework is ISO 14743 for push-in fittings and ISO 4414 for safety of pneumatic systems; REACH Article 33 candidate list disclosure is applied for imported assembled fittings. Internal lubricant masterbatch is compounded at 0.5–1.0 wt% to reduce tube insertion force during assembly; higher levels reduce collet grip because lubricant migration to the contact surface lowers friction beyond the specified assembly envelope. Regrind content is capped at 20 wt% in manifold bodies but set to 0 wt% in clamping collets and release sleeves because knit-line fatigue at the collet hinge triggers after repeated push-pull cycling when recycled material enters the melt stream. The injection molding line uses accumulator-assisted hydraulic machines with clamp force from 80 to 150 tonnes, general-purpose screws with L/D 20–22, and compression ratio 2.0:1. Melt temperature is set at 240–260 °C, mold temperature at 60–80 °C, and injection velocity at 180–300 mm/s to prevent flow hesitation at the sealing lip. Cavity-to-cavity hot runner temperature variation must remain below ±4 °C because thread minor diameter variation above 0.03 mm causes inconsistent O-ring compression. Screw recovery is set to finish 0.5–1.5 s before the cooling timer ends to avoid melt residence at the check ring. End products in this segment include G-thread and R-thread push-in fittings, modular manifold blocks, throttle valves, and silencer bodies. Published data for PD100 under ISO 14743 full temperature and pressure endurance tests is limited to part-specific validation because assembled fitting performance is determined by thread seating and collet geometry as much as by resin properties.

    For rail and EV cable management clips, the application boundary is not simple tensile load but low-temperature impact after moisture conditioning and fire performance inside enclosed electrical compartments. Cable tie heads, clamp bodies, corrugated conduit connectors, and high-voltage cable spacers are molded in 8–32 cavity multi-plate tools with tunnel gates into non-appearance edges. Melt temperature is set at 230–245 °C, screw rotational speed at 120–180 min⁻¹, back pressure at 3–7 MPa, and mold temperature at 50–70 °C. UV-stabilized masterbatch is added at 2.0–3.0 wt%; carbon black at 0.2–0.5 wt% is used only where laser marking contrast must remain legible after EN 45545-2:2020 R22/R23 interior fire testing. The low equilibrium moisture uptake of PA12—below 0.7 wt% at 23 °C and 50 % RH—keeps snap-fit retention force stable after humidity aging; this is verified by insertion-removal cycling under the vehicle maker’s harness retention specification. Cavity fill imbalance above 2 % of shot weight is a known cause of dimensional scatter in live hinge clamps; hot runner tip temperatures are logged and corrected to a ±3 °C band. Ejection is a production bottleneck because flexible latch and hinge features adhere to textured tool steel; draft angles of 3 °, air poppets at 0.5–0.8 MPa, and edge gates no smaller than 60 % of the nominal wall are standard countermeasures. Published data for PD100 under full EN 45545-2:2020 hazard-level classifications is limited to specific wall thickness brackets; flame-retardant package selection must be tested on the final component at its worst-case section rather than on laboratory plaques.

    When Mold Temperature Drops Below 40 °C in Cosmetic Buckle Tools

    Quick-release buckles, ski boot closure components, and trekking pole clamps impose contradictory mold-temperature requirements because high-gloss surfaces demand a cold tool while low-temperature impact toughness demands a warm tool. If the cavity surface is held below 40 °C, gate blush and sink marks are reduced, but frozen-in orientation near the gate lowers notched impact strength when measured under ISO 179-1/1eA at -30 °C. A two-stage thermolator profile is used on production tools: the first 8–10 s of holding time run at 35 °C to set the skin layer, then the tool is switched to 80 °C for the remainder of packing and cooling. Melt temperature is kept at 240–250 °C; injection velocity is 200–350 mm/s to fill thin snap arms before the skin freezes. Color masterbatch is added at 1.0–2.0 wt%, and no regrind is permitted in high-gloss cosmetic surfaces because pigment splitting and black specks produce visible flow lines. For load-bearing ski boot closure components, post-molding annealing at 90 °C for 2 h is applied only where the design cannot meet the required -30 °C notched impact with as-molded parts; this anneal also increases shrinkage by 0.1–0.2 %, so the cavity must be adjusted accordingly. End products include quick-release buckles, strap adjusters, pole locking clamps, and boot instep covers. The limiting process conflict is that longer holding time improves pressure transmission to thick sections but over-packs thin gate areas; cavity pressure sensors are therefore placed at the last point to fill and at the gate to set switchover at 95–98 % cavity fill.

    In potable and process water filter housings, impeller cages, and valve bodies, unreinforced PA12 is specified only when lower water absorption than PA6 or PA66 is required: at 23 °C water saturation, unreinforced PA12 absorbs approximately 1.5 wt% water, while PA6 absorbs approximately 9 wt%, and the continuous wetted wall temperature remains below the grade’s mechanical derating limit. The material meets FDA 21 CFR 177.1500 for nylon resins; finished devices in drinking-water service may additionally need NSF/ANSI/CAN 61 extraction testing. For potable-contact surfaces, regrind content is 0 wt%; for non-contact structural sections, internally generated runner regrind is limited to 15 wt% after documenting stable melt flow. Melt temperature is controlled at 235–250 °C, and barrel residence time above 240 °C is limited to 5 min to avoid hydrolysis and yellowing. Sequential valve gating is used in filter bowl tools to reduce weld-line porosity; packing pressure is maintained at 50–70 MPa. Cooling time is governed by wall thickness squared, not part weight: a 3 mm wall section requires approximately 18–25 s mold closed time with canal cooling channels of 10 mm diameter located 1.5 channel diameters from the cavity. Hydrostatic burst testing of the complete filter bowl is the release criterion, not tensile plaques. Published data for PD100 in hot chlorinated water above 60 °C is limited, so the filter manufacturer must validate service life using its own derating curve. End products include filter bowls, filter unions, pump impeller cages, valve bodies, and air release valve bodies.

    Medical Enclosure Compliance and Sterilization Tolerance

    Reusable medical handpiece housings, monitor enclosures, and fluid trap bodies made from PA12 are evaluated under ISO 10993-1:2018 biological risk assessment, with USP Class VI testing or device-specific extractables work required depending on the patient-contact classification. Cleanroom injection molding is performed in an ISO 14644-1 Class 8 environment as a minimum; process validation follows ISO 13485. For tissue- or fluid-contact components, regrind content is 0 wt%; for non-contact monitor enclosures, a validated internally generated regrind fraction not exceeding 10 wt% may be permitted only when the risk file demonstrates equivalent extractables and mechanical properties. Melt temperature is set at 240–255 °C, mold temperature at 50–70 °C, and screw speed at 80–120 min⁻¹ to limit shear heating. Hot runner temperature is kept at or below 255 °C to prevent brown discoloration from thermal degradation; cavity-to-cavity cooling water variation is maintained below 1 °C to control shrinkage at sealing faces. The main limitation in this segment is steam sterilization: repeated exposure to 134 °C gravity steam can shift crystallinity and produce dimensional growth at O-ring interfaces, so autoclave stability must be tested on the final enclosure rather than predicted from resin datasheets. End products are primarily replacement rather than load-bearing devices; load-bearing or clamping components require additional cyclic fatigue evaluation under the device’s ISO 10993-guided risk assessment. No inference of biocompatibility for PD100 is made without grade-specific master file documentation and statement from the supplier.

    Free Quote

    Competitive Polyram PlusTek PD100 Nylon 12, Injection Molding prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8615365186327 or mail to admin@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8615365186327

    Email: admin@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    Polyram PlusTek PD100 is an unfilled polyamide 12 injection-molding compound supplied as natural and black pellets. It is intended for components that require low equilibrium moisture uptake, high impact retention at subzero temperatures, and resistance to aliphatic hydrocarbon media. The material can be processed on a conventional single-screw reciprocating injection-molding machine equipped with a 3-zone screw having an L/D ratio of 20:1 to 24:1 and a compression ratio of 2.0:1 to 2.5:1. Within the PlusTek portfolio, PD100 is distinguished from glass-fibre-reinforced PA12 grades by retaining high elongation at break, typically above 200% under ISO 527-2, which makes it suitable for snap-fits, cable ties, clips, and fluid connectors. When lot-specific PD100 certificate values are not available, the following typical values for unfilled PA12 injection-molding compounds are used for preliminary tool design only; final tool compensation must be based on lot-specific certificate data and mold-flow analysis.

    Representative unfilled PA12 injection-molding data for preliminary tool design
    PropertyTest methodValue
    DensityISO 1183-11.01 g/cm³
    Water absorption at 23 °C, 50% RHISO 620.7 wt%
    Water absorption, saturation in water at 23 °CISO 621.5 wt%
    Melting temperature, DSCISO 11357-3176 °C
    Vicat softening temperature, A50ISO 306140 °C
    Heat deflection temperature, 0.45 MPaISO 75-2/B130 °C
    Tensile modulusISO 527-21,500 MPa
    Tensile stress at yieldISO 527-245 MPa
    Nominal strain at breakISO 527-2>200%
    Flexural modulusISO 1781,200 MPa
    Charpy notched impact at 23 °CISO 179-1/1eA10 kJ/m²
    Charpy notched impact at –30 °CISO 179-1/1eA6 kJ/m²
    Mold shrinkage, flow directionISO 294-41.2–1.6%
    Mold shrinkage, transverse directionISO 294-41.3–1.8%

    Melt volume-flow rate for PD100 should be obtained from the lot certificate; unfilled PA12 grades are commonly characterised at 230 °C under 2.16 kg load according to ISO 1133-1. The value is not used for tool design alone because injection velocity and holding-pressure control dominate cavity filling in thin-wall sections.

    What separates long-chain PA12 from PA6 and PA66 in humid service?

    The amide-group concentration in PA12 is lower than that of PA6 and PA66. Under ISO 62 at 23 °C and 50% RH, equilibrium moisture uptake is typically 0.7 wt% for unfilled PA12, compared with 2.8 wt% for PA6 and 2.5 wt% for PA66. The lower polarity of the C12 backbone reduces hydrogen bonding and limits moisture-induced plasticization. Consequently, flexural modulus and yield stress are more stable across humid and dry service envelopes, but the absolute stiffness remains below that of unfilled PA66. For PD100, the property difference translates into lower post-mold dimensional growth in moist environments and better retention of dielectric insulation; however, electrical properties should be tested under IEC 62631-3-1 because absorbed moisture influences volume resistivity.

    Equilibrium moisture uptake and density comparison for unfilled polyamide injection-molding grades
    Resin typeDensity (ISO 1183-1)Water absorption at 23 °C, 50% RH (ISO 62)Saturation in water, 23 °C (ISO 62)
    PA121.01 g/cm³0.7 wt%1.5 wt%
    PA111.04 g/cm³1.2 wt%2.0 wt%
    PA61.13 g/cm³2.8 wt%9.5 wt%
    PA661.14 g/cm³2.5 wt%8.5 wt%

    Compared with PA11, PD100's PA12 backbone has a lower melting temperature, typically 176 °C versus 189 °C for PA11 under ISO 11357-3. That lowers the melt-processing window but does not reduce low-temperature impact significantly; Charpy notched impact at –30 °C remains above 6 kJ/m² for high-quality unfilled PA12. The choice between PA12 and PA11 is often driven by supply source—petroleum-derived for PA12 versus castor-oil-derived for PA11—and by specific fuel-swell resistance requirements.

    When pellet surface moisture exceeds 0.15 wt% before hopper entry

    Even though PA12 absorbs less moisture than PA6 and PA66, storage in ambient conditions above 60% RH can raise pellet surface moisture to approximately 0.15–0.20 wt%. Pre-drying is then required to avoid splay, melt-pressure variation, and surface defects. A desiccant dryer with a dew point of –30 °C or lower at 80 °C for 4–6 h is standard; vacuum dryers operated at 70–80 °C for 2–4 h may be used where low-throughput drying is acceptable. Residual moisture measured by Karl Fischer titration should be below 0.10 wt% before processing. Drying should not exceed 100 °C for unfilled PA12 to avoid pellet sticking and oxidation-induced yellowing in natural grades.

    Barrel temperatures should be profiled from feed to nozzle: 190–210 °C in the feed zone, 210–230 °C in compression, 230–250 °C in metering, and 220–240 °C at the nozzle. Melt temperature measured at the purged shot should remain between 220 °C and 250 °C. Mold temperature should be maintained between 40 °C and 80 °C. For parts thicker than 3 mm, mold temperatures below 40 °C drive rapid skin solidification and anisotropic core growth; this produces post-mold warpage and sink marks. Injection velocity of 100–200 mm/s is suitable for nominal wall thicknesses from 1.5 mm to 3.0 mm. Holding pressure is typically 50–70% of injection pressure. Back pressure can be set between 0.5 MPa and 2.0 MPa, and screw surface speed should be limited to 0.2–0.5 m/s to avoid excessive shear heating and degradation. Melt residence time should not exceed 10 minutes at 250 °C to limit thermo-oxidative yellowing; screw speeds above 150 rpm on small machines can generate shear heating beyond the melt-temperature set point.

    Gate design, shrinkage compensation, and hot-runner limitations

    Unfilled PA12 has a high coefficient of linear thermal expansion and semi-crystalline shrinkage; tooling should apply 1.2–1.6% flow-direction and 1.3–1.8% transverse-direction compensation under ISO 294-4 cavity-pressure conditions. If a mold is cut to lower shrinkage, the risk of overpacking and warpage increases.

    Gate size and location should account for long-chain melt relaxation. Circular gate diameter should be at least 60% of the local wall thickness. Tab gates should have land length 0.5–1.0 mm. Runner diameters below 4 mm in cold-runner tools can increase pressure loss and gate freeze-off before complete pack. Hot-runner systems should maintain manifold temperatures at 230–245 °C; tip temperatures above 260 °C can produce black specks and surface gel formation. Needle-shutoff nozzles with small tip orifices are less tolerable to unreinforced PA12 than to reinforced grades because the melt can string from the gate.

    On production-scale machines with clamp forces between 60 t and 120 t, short-shot instability is observed when nozzle temperature drops below 220 °C or when hold-pressure is released too early. Process monitoring through cavity-pressure sensors is recommended to hold peak cavity pressure above 35 MPa for parts with a wall thickness up to 2 mm; for thicker sections, peak cavity pressure can be lower, 25–30 MPa, but should remain above zero until gate seal. In multi-cavity tools, runner balancing is critical because unfilled PA12 has lower thermal conductivity and may show asymmetric gate freeze if runner lengths vary by more than 10%. Cavity pressure sensors should verify that peak cavity pressures across cavities do not deviate by more than 5–10%.

    In fluid-contact applications, PA12 is selected for resistance to diesel fuel, lubricating oil, grease, alkaline cleaning media, and aliphatic hydrocarbons. It is not resistant to strong mineral acids at elevated temperature, phenol, concentrated formic acid, or polar chlorinated solvents. Published data for PD100-specific extended chemical exposure is limited; qualification should include immersion testing under ISO 527-2 tensile property retention or ISO 22088-2 stress-cracking after exposure to the specific process fluid. The grade's low moisture uptake also supports dimensional stability in pneumatic and fuel-system connectors; however, all fuel-contact approvals must be confirmed against the relevant OEM specifications and not inferred from PA12 generic performance.

    Regulatory status should be obtained from the manufacturer's certificate. Statements for EU RoHS 2011/65/EU, REACH SVHC, and FDA 21 CFR food-contact compliance depend on the specific pigment and additive package selected. When natural grade is used in food-contact applications, extraction testing under Regulation (EU) No 10/2011 may be required for the finished article.

    Top