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EMS-Grivory Grilamid® LVX-65H SST nat PA12-GF65

    • Product Name: EMS-Grivory Grilamid® LVX-65H SST nat PA12-GF65
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 425902
    Density 1.63 g/cm³
    Tensile Modulus 23500 MPa
    Tensile Strength At Break 250 MPa
    Elongation At Break 2.0 %
    Flexural Modulus 22000 MPa
    Charpy Notched Impact Strength 10 kJ/m²
    Heat Deflection Temperature 1 80 Mpa 190 °C
    Melting Point 220 °C
    Mold Shrinkage 0.2 %
    Water Absorption 24 H 0.1 %
    Flammability Rating HB
    Rockwell Hardness M90

    As an accredited EMS-Grivory Grilamid® LVX-65H SST nat PA12-GF65 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 net sealed polyethylene-lined paper bags, moisture-protected, labeled with grade, lot number, and handling instructions.
    Container Loading (20′ FCL) 20′ FCL: palletized Grilamid LVX-65H SST nat PA12-GF65 in sealed bags, weight optimized, securely braced to prevent shifting during transit.
    Shipping EMS-Grivory Grilamid® LVX-65H SST nat PA12-GF65 is shipped as dry, sealed pellets in moisture-barrier bags or drums to prevent water absorption. Keep packaging intact, store in a cool, dry area, and handle carefully to avoid damage. Refer to the SDS for full transport and safety guidelines.
    Storage Store in original, sealed, dry packaging in a cool, well-ventilated area at room temperature. Protect from direct sunlight, heat sources, and moisture to prevent water absorption and property changes. Keep away from incompatible materials and ignition sources. No special storage requirements under normal conditions; ensure containers remain closed when not in use.
    Shelf Life Store in original sealed packaging, cool and dry. Shelf life is 2 years from delivery if kept moisture-free.
    Application of EMS-Grivory Grilamid® LVX-65H SST nat PA12-GF65

    In industrial automation fluid-power assemblies, the substitution of machined aluminium with 65% glass-fibre-reinforced polyamide 12 is governed by pressure cycling, mineral-oil mist exposure, and dimensional stability across humidity fluctuations. The EMS-Grivory Grilamid® LVX-65H SST nat grade is processed as a neat compound at 100 wt% of the shot mass for subplate-mounted pneumatic valve islands, hydraulic accumulator mounting brackets, and manifold adaptor plates. The fixed glass-fibre loading of 65 wt% by weight reduces creep under sustained bolt preload and limits equilibrium moisture uptake relative to PA66, which stabilises port-to-port centre distances across 10–90% RH. In these applications, the governing system standards are ISO 4413:2010 for hydraulic fluid power and ISO 4414:2010 for pneumatic fluid power. Material compatibility is screened by immersion testing under ISO 1817:2015 in mineral oil, ester-based fire-resistant hydraulic fluid, and water-glycol at 70°C for 168 h; the specification normally limits volume change and hardness loss, but published data for this specific compound-fluid pair should be checked before release.The downstream production process for hydraulic and pneumatic manifold components requires an injection-moulding machine with a wear-resistant bimetallic barrel and a three-zone screw with an L/D ratio of 25:1. The melt temperature is maintained at 270–285°C, and the tool surface temperature is held at 80–100°C to promote sufficient crystallinity at the weld-line interfaces. Because the molten compound is highly filled, the gate location is placed at the geometric centre of the port face so that fibrous orientation does not create a weld line across the narrow sealing land. Holding pressure is applied at 60–80 MPa until gate freeze-off to compensate for the anisotropic shrinkage that develops in thick bosses and port walls. Sections thicker than 8 mm present an internal-void risk because displaced air and volatiles cannot escape through the high-viscosity glass-loaded melt; a two-stage injection profile with a slow screw recovery is preferred. The regrind of sprues and runners may be reintroduced at a maximum of 20 wt%, with 80 wt% virgin compound, provided the regrind is re-dried to ≤0.1 wt% moisture and has no more than three processing histories. When storage relative humidity exceeds 60%, predrying in a desiccant dryer at 80°C for 4–6 h is mandatory.The terminal finished-product types are pneumatic valve island baseplates, hydraulic manifold adaptor plates, and accumulator mounting brackets. The operational boundary for these components includes continuous exposure to mineral oil at fluid temperatures up to 120°C, but strong acidic media such as concentrated formic acid or hot concentrated hydrochloric acid are incompatible because the polyamide backbone undergoes acid-catalysed hydrolysis. Dimensional verification is normally performed at 23°C/50% RH after conditioning to ISO 291, and the manufacturer must confirm that the selected hydraulic fluid does not cause post-mould warpage through differential plasticisation of the glass-poor skin layer.

    Why 65% Glass-Fibre PA12 Meets the Structural Load Requirement in Motorcycle Footpeg Brackets

    Because the compound contains 65 wt% discontinuous glass fibre, the tensile modulus of the injection-moulded material typically falls in the range of 15,000–18,000 MPa when measured according to ISO 527-2. In motorcycle footpeg brackets, handlebar clamp bodies, and side-stand pivot brackets, the glass-fibre network dominates the elastic response under bending, while the polyamide 12 matrix contributes low-temperature impact compliance that is not available in more moisture-sensitive semi-crystalline resins. The finished assembly is validated against OEM specifications that reference ISO 527-2, ISO 178 for flexural properties, and ISO 179-1/1eA for notched Charpy impact at −30°C. Where the bracket is not a dedicated crash-energy absorber, multiaxial impact resistance is screened by ISO 6603-2 using a 20 mm striker at −30°C. The addition ratio for load-bearing zones is 100 wt% virgin compound; regrind is limited to non-critical ribs and bosses at a maximum of 20 wt% because repeated high-shear processing shortens glass-fibre length distribution and reduces weld-line impact energy.The downstream moulding process uses sequential valve gating to displace weld lines away from mounting-hole edges and to orient the fibre phase along the primary load path from the footpeg pivot boss to the frame anchor points. The melt temperature is maintained at 260–285°C, the mould steel temperature is kept at 80–110°C, and the tool surface is hardened to HRC 52 to resist abrasive wear during long production runs. A clamp force corresponding to 60–80 MPa of projected area prevents flash at the parting line without overpacking the thin vertical ribs that transfer bending stress. Mould-filling simulation is normally run with a Folgar-Tucker fibre orientation closure, and the resulting orientation tensor is exported to structural finite-element analysis to identify brittle regions where the flow direction is transverse to principal stress. The terminal finished-product types are motorcycle footpeg brackets, handlebar clamp bodies, and side-stand pivot brackets. The operational boundary is defined by low elongation at break measured by ISO 527-2, commonly below 2.5%, which demands that sharp internal corners be replaced by a minimum radius of 1.0 mm and that threaded inserts be installed with ultrasonic insertion rather than press-fitting to avoid microcracking.

    Analytical Instrument Deck Plates and the Anisotropic Shrinkage Boundary

    The first operational constraint in precision analytical instrument deck plates and optical bench brackets is anisotropic mould shrinkage. For a 65 wt% glass-fibre-reinforced polyamide 12, flow-direction shrinkage measured in accordance with ISO 294-4 can remain below 0.2%, while cross-flow shrinkage can be three to five times larger, creating a measurable out-of-plane bow in flat deck plates. The natural grade of Grilamid® LVX-65H SST is processed at 100 wt% without carbon black or antistatic masterbatch unless the specified analytical environment demands conductivity control. Regrind is restricted to 10 wt% in alignment-critical base frames because particle contamination from multiple heat histories can alter the coefficient of linear thermal expansion and disturb interferometric flatness. Compliance for the assembled instrument includes IEC 61010-1:2010 for laboratory equipment, RoHS 2011/65/EU, and REACH 1907/2006; if the deck plate is installed in a cleanroom, outgassing requirements must be tested separately because published data for this specific natural PA12-GF65 configuration in high-vacuum service is limited.The downstream production method for warpage-critical deck plates is injection-compression moulding rather than conventional injection moulding. A compression stroke of 0.1–0.3 mm is applied after fill to equalise pressure across the part and reduce differential fibre orientation between the edge and centre regions. The melt temperature is set at 260–280°C, and the mould surface is maintained at 90–110°C to achieve adequate crystallinity before ejection. Hot-runner sequential valve gates balance fill rates among multiple flow fronts, and the gate layout is arranged so that the warpage-sensitive flatness datum is not intersected by a weld line. After ejection, the deck plates are held in cooling fixtures for 20 min under light constraint to prevent post-demoulding curl. The terminal finished-product types are mass spectrometer chassis plates, optical table mounting brackets, and laboratory diagnostic instrument base frames. The operational boundary includes continuous exposure at 23°C/50% RH, but natural unfilled and glass-filled PA12 surfaces are not intrinsically UV-stable; outdoor or UV-rich environments require a UV-absorbing coating or a black pigmented co-moulded layer.

    At sub-zero alpine service temperatures, the glass-fibre network in a 65 wt% GF PA12 compound dominates tensile modulus and restricts creep of the polyamide 12 matrix. In ski touring binding frames and crampon bracket assemblies, load is transferred through heel pins and toe inserts, and brittle fracture at −30°C must be excluded by material-level testing before product-level release testing. The load-bearing zones are injection-moulded from 100 wt% virgin compound; regrind is not permitted in release-relevant zones because impact consistency is degraded by fibre-length reduction and by accumulated thermal oxidation. The product safety framework is ISO 13992:2019 for alpine ski bindings, and the material qualification matrix includes ISO 527-2 for tensile modulus, ISO 179-1/1eA for notched Charpy impact at −30°C, and ISO 8256 Type 2 for tension impact at −40°C. The finished component must maintain dimensional stability after thermal cycling between −40°C and 60°C, because release-setting accuracy depends on the positional repeatability of the housing bores.The downstream process for these low-temperature structural housings uses a tool temperature of 60–70°C to limit post-mould shrinkage in the thick toe-piece boss, while accepting a slightly lower crystallinity than would be obtained at higher mould temperatures. The melt temperature is held at 260–275°C to avoid excessive residence time in the high-shear gate region, and the injection speed is staged to prevent jetting in the pin-insert cavity. After ejection, the housings are annealed at 120°C for 2 h in a support fixture to relieve moulded-in stress and to stabilise the bore geometry before insert staking. The terminal finished-product types are ski touring binding toe-piece housings, crampon frame brackets, and release-lever bases. The boundary condition for this application is outdoor weathering: natural PA12 grades do not contain carbon black and therefore require a UV-stable overmoulding layer or a painted surface when multi-season alpine exposure is expected.

    When Cyclic Loading in Pneumatic Actuator End Caps Demands Controlled Fibre Orientation

    When cyclic loading in pneumatic actuator end caps demands controlled fibre orientation, the moulding strategy differs from static bracketry because weld lines migrate in relation to core pins, port threads, and cushion-seal bores. The compound's weld-line tensile strength under ISO 527-2 is typically reduced to 40–50% of the fully fused bulk value in a 65 wt% glass-loaded polyamide 12, so gate placement must place the weld line outside the pressure-retaining wall and into a non-structural flange. The pressure-retaining section is moulded from 100 wt% virgin compound, while regrind at up to 20 wt% is permitted only in external ribs and mounting flanges that do not see cyclic pressure load. The regulatory framework is ISO 4414:2010 for pneumatic systems, and dimensional interchangeability follows ISO 21287:2012 for compact pneumatic cylinder end caps. Material compatibility with compressor oils and synthetic ester lubricants is screened under ISO 1817:2015 at 70°C for 168 h, with hardness change and tensile modulus retention recorded after immersion.The injection-moulding process uses a melt temperature of 270–290°C and a tool temperature of 85–95°C. Fill speed is profiled from slow to fast to avoid jetting at the port core, and gas-venting pins are positioned at the weld-line extremities to reduce burn marks and local porosity. Holding pressure is maintained until the gate freezes, and the tool is polished to Ra 0.1 µm in the seal-groove cavities because exposed glass fibres at the surface produce micro-grooves that compromise lip-seal contact. The terminal finished-product types are pneumatic actuator end caps, rotary actuator housings, and valve cover plates. The operational boundary includes continuous pneumatic pressure cycling at 10 bar and temperature excursions to 80°C; the design must avoid sharp root radii in the port thread bosses because notch-sensitive fatigue crack initiation can occur at thread run-out points.

    Evaluating Compressor Valve Housing Mouldings Under Hot Synthetic Ester Oil Exposure

    Compressor valve housing mouldings and high-temperature oil exposure test the polyamide 12 matrix differently from dry mechanical loading because hot synthetic ester oils can plasticise the polymer phase and lower the modulus. The material is processed at 100 wt% for oil-exposed sealing faces and pressure-adjacent walls; regrind is not used in these zones because multiple heat cycles create oxidative species that accelerate surface microcracking under thermal-oil cycling. The relevant system standard is ISO 4414:2010, and material-fluid compatibility is assessed by ISO 1817:2015 immersion in the specific ester compressor oil at 100°C for 168 h. Published data for this specific PA12-GF65 compound in hot synthetic ester oil is limited, so the end-user must validate weight change, volume change, and tensile strength retention for the exact oil formulation. The terminal component class includes small pneumatic compressor cylinder head shrouds, valve plate housings, and oil-separator cover plates.The downstream moulding process for oil-exposed compressor housings uses a tool temperature of 95–110°C to maximise crystallinity before demoulding, a melt temperature of 275–285°C, and a screw with a low-shear geometry to limit fibre breakage. After ejection, the parts are annealed at 150°C for 4 h in conforming support fixtures to stabilise dimensions and relieve internal stress before exposure to hot oil. The housing design incorporates radiused boss roots and a minimum wall thickness of 3 mm to avoid sink-induced voiding at the valve cover sealing face. The operational boundary is continuous service at 100°C in synthetic ester oil; exposure above 150°C is not recommended because oxidative aging of the heat-stabilised polyamide matrix can reduce tensile elongation and promote surface embrittlement at sharp corners.

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    Certification & Compliance
    More Introduction

    EMS-Grivory Grilamid® LVX-65H SST nat is a natural-coloured, heat-stabilised polyamide 12 injection moulding compound reinforced with 65% by mass glass fibre. Under ISO 1043-1 the material is designated PA12-GF65. The nat suffix denotes natural, unpigmented material, and the SST designation identifies the specific stabiliser and processing package. The compound is supplied as cylindrical pellets for conventional injection moulding, and the uncoloured natural grade is intended for applications where colouring is performed at the processing stage or where a neutral natural surface is acceptable. Typical density under ISO 1183-1 is 1.68 g/cm³; water absorption after 24 h immersion in 23 °C water is ≤ 0.6% under ISO 62, and equilibrium water absorption at 23 °C is approximately 1.5%. Because PA12 has lower intrinsic water affinity than PA6 or PA66, the conditioned mechanical properties are less affected by humidity than equivalently reinforced short-chain aliphatic polyamides. The high glass-fibre fraction also reduces the total moisture uptake relative to unfilled PA12 because the glass fibres do not absorb water; however, dimensional movement is anisotropic due to fibre orientation. This anisotropy is a key difference from unreinforced PA12 and from lower-fibre PA12 grades.

    What Mechanical Property Shifts Occur When Glass Fibre Content Reaches 65% in PA12?

    The primary difference from PA12-GF30 and PA12-GF50 is a higher tensile modulus and tensile strength combined with lower elongation at break. Dry tensile modulus at 1 mm/min under ISO 527-1/-2 is approximately 20,000 MPa; tensile stress at break is approximately 230 MPa; elongation at break is approximately 2.5%. Conditioned modulus at 23 °C and 50% relative humidity remains higher than that of many PA6 or PA66 glass-fibre compounds with comparable loading because PA12 absorbs less moisture. Charpy unnotched impact strength at 23 °C is approximately 90 kJ/m² under ISO 179/1eU; notched Charpy impact strength is approximately 35 kJ/m² under ISO 179/1eA.

    Typical dry mechanical and thermal property profile for EMS-Grivory Grilamid® LVX-65H SST nat
    PropertyTest methodTypical value
    DensityISO 1183-11.68 g/cm³
    Tensile modulus, dryISO 527-1/-220,000 MPa
    Tensile stress at break, dryISO 527-1/-2230 MPa
    Elongation at break, dryISO 527-1/-22.5%
    Charpy unnotched impact, 23°CISO 179/1eU90 kJ/m²
    Charpy notched impact, 23°CISO 179/1eA35 kJ/m²
    Melting peakISO 11357-3178 °C
    HDT at 1.8 MPaISO 75-1/-2165 °C
    HDT at 0.45 MPaISO 75-1/-2175 °C
    Water absorption, 24 hISO 620.6%

    The high glass-fibre volume fraction creates a skin-core morphology in injection-moulded parts. In the skin layer, fibres orient predominantly parallel to flow; in the core, orientation is more random because of slower cooling and reduced shear. This structural gradient explains the measured difference between flow-direction and transverse tensile modulus. In ribs, bosses, and weld lines, fibre orientation is disturbed, which reduces local stiffness and creates sinks, warpage, and strength loss. Weld lines and gate regions can show tensile strength reductions of 30% to 50% compared with flow-oriented regions. Mould shrinkage under ISO 294-4 is anisotropic, with published values near 0.1% in the flow direction and near 0.4% transverse to flow. These differences require revised gate placement and part geometry when upgrading from PA12-GF50 or PA12-GF30.

    Thermal response in short-duration tests is controlled mainly by the glass-fibre network. The melting peak measured under ISO 11357-3 is approximately 178 °C. Heat deflection temperature under 1.8 MPa load is approximately 165 °C, and under 0.45 MPa it is approximately 175 °C, both under ISO 75-1/-2. These HDT values exceed those of unreinforced PA12 by a wide margin, but continuous service above 120 °C is not generally recommended without long-term heat-ageing validation, because the oxidative stability of the PA12 matrix limits property retention. In moisture-rich environments, PA12 absorbs less water than PA6 or PA66, so dry-state modulus is better retained; however, the grade is not intended for continuous hot-water immersion above 80 °C under high tensile loads. The coefficient of linear thermal expansion is anisotropic; published values for injection-moulded PA12-GF65 are approximately 0.15 × 10-4 K-1 in the flow direction and 0.8 × 10-4 K-1 transverse under ISO 11359-2. Published multi-point creep and fatigue data for this specific formulation are limited, so load-bearing designs should use component-level testing or finite-element analysis with measured anisotropic data.

    The polyamide 12 matrix contains a repeating long-chain amide backbone with lower amide-group density than PA6 or PA66. This molecular structure reduces equilibrium water uptake of the matrix and contributes to lower fuel permeation in direct fuel-contact applications. In LVX-65H SST nat, the glass fibre dominates short-term modulus, but the matrix controls long-term creep, chemical resistance, and low-temperature impact. At temperatures below the PA12 glass transition, the compound retains relatively high stiffness; above the glass transition, modulus decreases even though HDT remains high due to fibre reinforcement. Creep and load-deflection behaviour under sustained service near 80–100 °C should therefore be evaluated with conditioned specimens rather than dry short-term data.

    Processing, Moisture Control, and Fibre Attrition on the Production Floor

    Processing on production-scale injection moulding machines requires predrying in a desiccant dryer at 80 °C for 4–8 h to a residual moisture level of ≤ 0.10%. The drying air dew point should be ≤ -30 °C. Melt temperatures from 250 °C to 280 °C and mould temperatures from 80 °C to 100 °C are used as starting points; higher mould temperatures improve surface appearance and weld-line strength at the cost of longer cycle time. The 65% glass fibre loading is abrasive; screws with hardened check rings, bimetallic barrels, and hardened nozzle tips are specified. Moderate screw speed and back pressure limit fibre attrition; injection speeds of 80–150 mm/s are typical for wall sections from 2 mm to 4 mm. Residence time at melt temperature should not exceed 10 minutes, and the barrel should be purged with a suitable PA12 or PA6/66 purge compound during interruptions. Exposure to ambient air with relative humidity above 60% can raise pellet moisture above the recommended limit within 1–2 h in warm conditions; hopper drying should remain active during production. Regrind use above 30% is not recommended because fibre length reduction and heat history may lower impact strength and increase melt viscosity variation. Batch-to-batch variation in fibre length distribution can occur if regrind or improperly dried material is used; process monitoring should therefore include melt pressure and part mass rather than melt temperature alone.

    For components with wall thickness below 1 mm, filling is difficult because of the high glass-fibre content and elevated melt viscosity. Gate and runner sizing should be more generous than for unfilled PA12; pin gates below 0.8 mm can cause fibre blocking and surface defects. Venting depth should be kept below 0.02 mm to avoid flash while allowing gas escape from the highly reinforced melt. Published process data for such thin-wall configurations are limited, and prototype tooling is recommended before production release.

    When the grade is used to replace PA12-GF30, PA12-GF50, PA6-GF60, or PA66-GF60, the higher modulus and lower elongation require redesigned ribs, corner radii, and gating to avoid stress concentration. Compared with PA12-GF50, the 65% glass fibre loading raises tensile modulus and HDT but lowers Charpy impact and elongation; processing requires higher packing pressure because shrinkage anisotropy is more severe. Compared with PA6 or PA66 glass-fibre compounds, the PA12 matrix provides lower equilibrium moisture uptake and better retention of tensile modulus after conditioning; however, PA6/PA66 may offer lower raw material cost and higher dry-state HDT. Compared with PPA-GF65 or PPS-GF65, LVX-65H SST nat processes at lower melt temperatures and generally has higher elongation at break, but it is not a direct substitute in continuous high-temperature service above 180 °C. Typical applications include injection-moulded housings, pump bodies, flanges, brackets, gear casings, and structural inserts for automotive and industrial equipment. The PA12 matrix provides resistance to oils, greases, fuels, and many solvents; the grade is selected over PA6 or PA66 glass-fibre compounds when lower moisture uptake and better dimensional stability in humid air are needed. It is selected over die-cast aluminium or zinc when part mass reduction and corrosion resistance are priorities, but absolute tensile modulus is lower by roughly an order of magnitude; ribbing, metal inserts, and fibre-orientation modelling are required to compensate. The material is not generally supplied as a food-contact grade; specific migration testing under EU Regulation (EC) 10/2011 would be required for food-contact use. Chemical resistance of the PA12 matrix extends to aliphatic hydrocarbons, diesel fuel, lubricating oils, and many industrial solvents. However, strong acids, oxidising media, and some phenolic compounds can degrade polyamide; compatibility testing under ISO 22088-3 or ASTM D543 is recommended for chemical service. The grade is not recommended for continuous use in concentrated acids or strong alkalis.

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