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EMS-Grivory Grilamid® LV-30H FWA black 9225 PA12-GF30

    • Product Name: EMS-Grivory Grilamid® LV-30H FWA black 9225 PA12-GF30
    • 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 447399
    Material EMS-Grivory Grilamid LV-30H FWA black 9225 PA12-GF30
    Base Polymer PA12
    Reinforcement 30% Glass Fiber
    Density 1.23 g/cm³
    Melting Point 178 °C
    Tensile Modulus 7000 MPa
    Tensile Strength At Break 120 MPa
    Elongation At Break 3%
    Charpy Impact Strength Notched 23 C 15 kJ/m²
    Charpy Impact Strength Unnotched 23 C 60 kJ/m²
    Heat Deflection Temperature A 1 8 Mpa 160 °C
    Vicat Softening Temperature B50 170 °C
    Water Absorption At Saturation 0.7%

    As an accredited EMS-Grivory Grilamid® LV-30H FWA black 9225 PA12-GF30 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Grilamid LV-30H FWA black 9225 PA12-GF30 is supplied as pellets in 25 kg moisture-protective bags.
    Container Loading (20′ FCL) 20′ FCL: Grilamid LV-30H FWA black 9225 PA12-GF30, moisture-protected bags on pallets, securely loaded for safe, efficient transport.
    Shipping Grilamid® LV-30H FWA black 9225 is a PA12-GF30 thermoplastic resin supplied as pellets. Ship in sealed, moisture-proof packaging to prevent humidity absorption. Store in a cool, dry area below 50°C. Not classified as hazardous; avoid dust accumulation and static discharge. Standard freight is acceptable.
    Storage Store in original, unopened packaging in a cool, dry place away from direct sunlight and heat sources. Keep container tightly sealed to prevent moisture absorption, which can degrade the PA12-GF30 resin. Recommended storage temperature is below 30°C. Avoid exposure to UV radiation and humidity, ensuring material is dry before processing to maintain optimal properties.
    Shelf Life Shelf life is typically two years when stored in original, unopened packaging in a cool, dry place.
    Application of EMS-Grivory Grilamid® LV-30H FWA black 9225 PA12-GF30

    In potable water distribution manifolds and valve bodies produced from glass-reinforced polyamide 12, the selection of a 30% glass-fiber loading is driven by the need to maintain creep resistance and dimensional stability in continuous contact with warm water while satisfying drinking-water migration thresholds. The FWA suffix in Grilamid® LV-30H FWA black 9225 indicates a formulation intended for food and water contact, but certification under EU 1935/2004, EU 10/2011, FDA 21 CFR 177.1500, NSF/ANSI 61, BS 6920, and KTW-BWGL must be confirmed for the finished article because insert molding, post-molding assembly, and surface finishing can alter migration behaviour. Pre-drying is the single largest processing risk for water-contact components. A desiccant dryer operating at 80 °C for 4–6 h with an air dew point of ≤−30 °C is used to reach residual moisture ≤0.10%. Hydrolytic degradation begins when molten PA12 is processed above 270 °C in the presence of moisture, causing surface silver streaks and reduced burst strength. Barrel profile from hopper to nozzle is set flat at 250–265 °C, reducing glass-fiber attrition in the compression zone. Mold wall temperature is held at 60–80 °C to create a semicrystalline surface layer that limits extractables. Holding pressure is 50–70 MPa, screw cushion is 3–5 mm, and back pressure is 0.5–1.5 MPa to avoid excessive fiber breakage while still allowing melt homogenisation. Direct gate or valve gate configurations are used for valve bodies; hot runner manifolds must be capable of 270 °C intermittent purge without stagnation. Finished articles include potable water manifolds, flow sensor housings, filter caps, and mixing valve bodies. Long-term contact with chlorine dioxide above 4 mg/L at continuous water temperatures above 60 °C may induce oxidative attack; published data for this specific configuration is limited. Regrind should be limited to 20 wt% when permitted by the application because each regrind pass can reduce notched impact strength, and validation by ISO 179/1eA is required.

    Table 1. Compliance verification matrix for water-contact PA12-GF30 FWA articles
    Standard or regulationRelevant test or boundaryApplication scope
    FDA 21 CFR 177.1500Extractables under food-contact conditionsNylon food-contact components
    EU 10/2011Overall migration limit < 10 mg/dm²Plastic articles in contact with food
    NSF/ANSI 61Extraction and toxicological reviewDrinking water system components
    BS 6920Odour, flavour, metals, and microbial growthUK water-contact fittings
    KTW-BWGLDrinking-water hygiene testingGerman-market plastics in water contact

    How Does Weld-Line Strength in Air Brake Valve Housings Survive High-Cycle Pressure Pulsation?

    Compressed air brake systems for heavy-duty commercial vehicles use 30% glass-reinforced PA12 valve bodies because the material’s low equilibrium moisture uptake limits swelling in humid air reservoirs and because PA12 retains mechanical response after exposure to zinc chloride road salt. Component-level validation is governed by assembly-specific OEM tests rather than a single global material standard; SAE J2494 addresses air brake performance requirements at the assembly level, and ISO 7628-1 covers thermoplastic tubing but not injection-moulded valve housings. The critical failure mode in these housings is not creep but weld-line cracking under pressure pulsation. At 30% glass loading, weld-line tensile strength can fall by more than 40% relative to surrounding material because glass fibers orient parallel to the melt front and do not interpenetrate across the knit plane. Gate sequencing is therefore used to move weld lines away from sealing faces; if a weld line cannot be eliminated, melt temperature is raised to 270–275 °C and mold wall temperature to 80 °C to improve interfacial fusion. Residence time must remain below 5 minutes at the upper melt temperature. Injection speed should be set in the upper third of the machine range to reduce melt-front cooling, but excessive shear above 10,000 s⁻¹ can damage glass fibers and lower impact strength. Back pressure is held at 1.0–2.0 MPa and screw recovery is slowed to avoid fiber breakage. The screw should have a compression ratio of 1.5–2.0:1 and a non-return valve with hardened ring; abrasive glass fiber causes clearance growth in standard nitrided barrels after 10,000–15,000 cycles if wear-resistant coatings are not used. Dilution with unfilled PA12 regrind is not advised for pressure-bearing walls because the 30% glass loading is required for burst strength; regrind content is limited to 10 wt%. Finished articles include ABS modulator housings, solenoid valve bodies, pressure protection valve covers, and trailer gladhand mounting plates. Avoid post-mold machining of sealing surfaces because exposing glass fibers creates a rough surface with poor lip-seal retention.

    When chemical process equipment must resist dilute acids, aliphatic hydrocarbons, and hot water without the dimensional growth seen in PA6-based components, PA12-GF30 is specified for pump volutes, filter heads, and dosing pump housings. The polymer matrix shows low water regain; at 23 °C/50% RH, equilibrium moisture uptake is typically 0.5–0.7% by ISO 62, whereas PA6-GF30 can absorb 2.5–3.0%. This lower moisture uptake translates into more stable pump housing dimensions and lower risk of shaft bore closure in humid environments. Chemical resistance screening follows ISO 175 and, where stress-cracking is suspected, ISO 22088-3 bent-strip tests at 1% strain. PA12-GF30 is generally resistant to diesel, aliphatic solvents, weak acids, and warm water up to 80 °C; it is attacked by concentrated mineral acids, phenols, cresols, and benzyl alcohol. No grade-specific resistance data for the black 9225 formulation should be assumed without testing; immersion work should be performed on as-moulded plaques with correct skin orientation. Residual mold-in stress accelerates environmental stress cracking in chemical service. Thick sections should be annealed at 80–90 °C for 4 h in circulating air, followed by slow cooling at ≤1 °C/min. The specific residual stress threshold for this grade is not published; moulder validation is required. Melt temperature is kept at 245–260 °C, mold temperature 70–80 °C, and gate size is enlarged by 20–30% relative to unfilled PA to prevent jetting and fiber-rich surface defects. Finished components include diaphragm pump housings, metering valve bodies, filter heads, and flue-gas condensate drains. Continuous service with aqueous glycol above 50% at 80 °C may reduce service life; published data for this specific configuration is limited.

    Dairy Filling Valve Bodies and Alkaline CIP Fluid Compatibility

    Food processing equipment uses PA12-GF30 for structural components that require resistance to hot water, dairy fats, and alkaline cleaning-in-place solutions. The material is not a replacement for stainless steel in shear-throttle valves or homogeniser parts, but it is used in valve bodies, guide bushes, and product-contact housings where lower thermal mass and corrosion resistance are required. For dairy contact, EU 10/2011 overall migration and FDA 21 CFR 177.1500 extractive limits apply; the final article also must meet Regulation (EC) No 1935/2004 traceability and good manufacturing practice provisions. CIP solutions containing 1–2% sodium hydroxide at 75–85 °C are the dominant chemical exposure. PA12-GF30 tolerates short alkaline exposure, but repeated 30–60 minute cycles can remove surface finish and expose glass fibers if the mold surface is not sufficiently polymer-rich. High mold temperatures of 80–85 °C are used to create a resin-rich skin and reduce exposed fiber ends. Processing window: melt temperature 250–265 °C, holding pressure 60–80 MPa, and gate freeze time 3–5 s; hot runner tips with 1.0–1.5 mm gate diameter help maintain uniform packing without leaving brittle knit lines. Do not blend with external color masterbatch; the black 9225 is pre-compounded, and additional masterbatch above 1 wt% can shift viscosity and change gate freeze time. Finished products include dairy filling valve bodies, CIP spray-ball mounts, and level-sensor flanges. Not recommended for continuous contact with steam above 121 °C or with peracetic acid above 500 ppm at elevated temperature; published data for this specific grade is limited.

    Electrical and electronic housings made from 30% glass-reinforced PA12 are specified where lower moisture regain preserves surface resistivity after high-humidity exposure, such as outdoor industrial terminal boxes, sensor enclosures, and power-tool structural frames. The material’s lower moisture absorption compared with PA66 reduces electrolytic corrosion at insert-moulded brass terminals and maintains dimensional fit for sealing interfaces under IEC 60529 ingress protection tests. Electrically relevant properties include comparative tracking index tested per IEC 60112, dielectric strength per IEC 60243-1 at 1.0 mm thickness, and volume resistivity per IEC 62631-3-1. Typical PA12 grades can show CTI values above 500 V, but the grade-specific UL Yellow Card for black 9225 must be consulted for the official value. Insert molding of brass or steel terminals requires preheating inserts to 120–140 °C to prevent cold fracture at the interface; insert surface roughness should be Ra 3.2–6.3 µm to ensure mechanical anchoring. Molding uses a melt temperature of 250–260 °C, mold temperature 60–80 °C, and venting gaps of 0.01–0.02 mm to prevent burn marks at end-of-fill. The material is supplied in black 9225, so no color masterbatch is required; addition of external regrind above 15 wt% may shift dielectric strength and should be qualified separately. Finished articles include industrial connector bodies, terminal blocks, sensor housings, and motor brush-holder frames. Compliance with RoHS 2011/65/EU and REACH 1907/2006 is expected for the base polymer but must be confirmed through final supplier declarations. Outdoor applications exposed to UV require additional carbon-black stabilisation; black 9225 provides some protection, but prolonged wet and UV cycling may still reduce gloss and surface electrical properties.

    When Industrial Actuator Gear Housings Require Moisture-Cycled Dimensional Stability

    Industrial motion-control assemblies use PA12-GF30 for gear housings, coupling sleeves, cam wheels, and linear actuator covers because the grade retains dimensional stability under variable humidity better than short-chain aliphatic polyamides. In a 2 mm section, moisture uptake at 23 °C/50% RH approaches 0.5–0.7% by ISO 62, which is substantially below PA6-GF30. This difference reduces hygroscopic expansion and allows gear centre distances to remain within 0.05–0.15% tolerance over seasonal humidity changes. Anisotropic mold shrinkage must be accounted for in gear housings with thin bearing webs. For a 2 mm wall, flow-direction shrinkage is typically 0.2–0.4%, transverse shrinkage 0.5–0.8%; these values shift with gate location, fiber orientation, and effective packing pressure. To stabilise dimensions, parts are annealed at 80 °C for 4 h immediately after molding, and dimensional audits are conducted after 24 h at 23 °C/50% RH. The molding window uses melt temperature 250–265 °C, mold 70–80 °C, holding pressure 50–70 MPa, and injection speed set to minimise jetting; if jeting occurs at the gate with a flow-length-to-thickness ratio above 3:1, the gate land is widened by 25%. Finished products include gear housing shells, cam followers, conveyor coupling rings, and positioner brackets. Machining after molding is not recommended for bearing bores because cutting through the resin-rich surface exposes glass fibers and accelerates wear; if machining is unavoidable, sharp tungsten carbide tools with 0.05–0.10 mm/tooth feed are used. The ranges below are drawn from published typical data for 30% glass-reinforced PA12 grades; they are not a supplier certificate for this specific batch of black 9225.

    Table 2. Moisture and mechanical response ranges for 30% glass-reinforced PA12 at 23 °C
    PropertyDry as mouldedConditioned 23 °C/50% RHTest method
    Tensile modulus7800–8500 MPa5800–6500 MPaISO 527-1/-2
    Tensile strength at break125–140 MPa100–115 MPaISO 527-1/-2
    Elongation at break2.5–4.5%4.0–6.0%ISO 527-1/-2
    Charpy notched impact12–16 kJ/m²13–18 kJ/m²ISO 179/1eA
    Density1.25–1.30 g/cm³ISO 1183
    Equilibrium water absorption0.5–0.7%ISO 62

    Hydrogen fuel handling components made from PA12-GF30 are being evaluated for structural housings, manifold supports, and low-pressure valve mounting brackets, not for high-pressure storage liners. The glass-fiber reinforcement embrittles the material, which is undesirable for liner expansion; PA12 liners typically use unmodified or lightly filled grades. Qualification under UN ECE R134 and ISO 19880-3 is system-specific, and material compatibility must be proven through rapid gas decompression and permeation testing. Published data for this specific configuration is limited. Processing for hydrogen-adjacent components prioritises low volatile residue and dimensional stability. Melt temperature is held at 245–260 °C, mold 60–80 °C, and no external mold release is used because silicone contamination interferes with downstream seal bonding. Parts are vacuum-dried at 80 °C for 6–8 h after molding to reduce water content before closed-system assembly. Glass-fiber orientation at sealing faces is managed with edge gates placed away from the seal land. Finished products include hydrogen dispenser valve housings, fuel cell manifold brackets, and thermal management component frames. Avoid use in contact with high-pressure hydrogen above 20 bar unless validated for rapid decompression; environmental stress-cracking data under hydrogen is not publicly available for this grade.

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    Certification & Compliance
    More Introduction

    EMS-Grivory Grilamid LV-30H FWA black 9225 is a heat-stabilised, 30% glass-fibre-reinforced polyamide 12 compound supplied as black pellets for injection moulding. Its resin designation under ISO 1043 is PA12-GF30, and the numeric suffix in the trade name identifies the nominal glass-fibre loading by mass. The density is typically 1.24–1.26 g/cm³ when measured to ISO 1183-1, which is lower than a comparable 30% glass-fibre-reinforced polyamide 66 because the PA12 matrix is less dense. The FWA identifier refers to a specific stabiliser and colour package, while black 9225 is the colour code used in traceability and batch release documentation. Those codes are not generic commercial descriptors; the exact regulatory scope must be confirmed against the current EMS certificate because FWA-based approvals are grade-, colour-, and region-specific.

    The principal technical differentiation against PA6-GF30 and PA66-GF30 is the lower equilibrium moisture absorption of the polyamide 12 backbone. At 23 °C and 50% relative humidity, PA12-GF30 typically reaches 0.5–0.8% moisture content, while PA6-GF30 and PA66-GF30 under the same conditions attain approximately 1.5–2.2% and 1.2–1.8% respectively. Saturated water uptake measured to ISO 62 remains near 1.2% for PA12-GF30. This lower uptake limits the plasticising effect of water diffusion and reduces the dry-to-conditioned modulus shift that is more pronounced in short-chain polyamide matrices. For water-meter housings, valve bodies, filter heads, pneumatic manifolds, and other components exposed to intermittent wet service, the lower moisture-induced dimensional movement reduces seasonal variation in flatness and snap-fit engagement.

    Why Does the Dry-to-Conditioned Shift Matter in Glass-Fibre-Reinforced Polyamide 12?

    Mechanical data are reported in both dry-as-moulded and conditioned states. Supplier-published values for this grade, obtained by ISO 527-1/-2 at 23 °C, generally place dry tensile modulus in the 8.5–10.0 GPa band and tensile stress at break at 120–140 MPa. After conditioning to 50% relative humidity, the modulus typically decreases to 5.5–7.0 GPa and stress at break to 85–105 MPa, while elongation at break increases from 3–5% dry to 5–8% conditioned. Notched Charpy impact strength by ISO 179-1/1eA is approximately 12–15 kJ/m² dry and 15–18 kJ/m² conditioned. The conditioned values are relevant for water-contact applications; finite-element simulations using only dry data will over-predict rigidity in humid or immersed service. Published data for long-term hot-water ageing on the exact black 9225 variant is limited, so verification coupons should be aged and tested according to ISO 527-2 and ISO 179-1/1eA after the intended service interval.

    Representative material-class comparison for 30% glass-fibre-reinforced polyamides at 23 °C
    PropertyPA12-GF30 (Grilamid LV-30H)PA6-GF30PA66-GF30
    Density [ISO 1183-1]1.24–1.26 g/cm³1.35–1.37 g/cm³1.36–1.39 g/cm³
    Saturated water uptake [ISO 62]1.2%2.0–2.4%1.6–2.0%
    Heat deflection temperature, 1.8 MPa [ISO 75-2/A]155–165 °C185–195 °C225–240 °C
    Tensile modulus dry [ISO 527-1/-2]8.5–10.0 GPa8.5–9.5 GPa9.0–10.0 GPa

    The comparison illustrates that PA12-GF30 is selected not for maximum heat resistance but for a combined reduction in density, water uptake, and humid-environment property shift. In dry-stiffness terms, PA6-GF30 and PA66-GF30 are competitive; their distinction is thermal performance and matrix cost. In fuel vapour or glycol-water contact, the PA12 backbone also offers better stress-cracking resistance than many short-chain polyamides, but this generalisation does not cover aggressive additive packages. Service chemical compatibility should be evaluated to ISO 175 and, where external strain is present, to ISO 22088-2 bent-strip environmental stress-cracking procedures.

    Fibre Orientation Governs Weld-Line Efficiency in Ribbed Components

    In the moulded skin layer, glass fibres align preferentially in the flow direction, producing a tensile modulus along flow that is higher than the cross-flow response. At weld lines, fibre alignment is perpendicular to the bonding interface, so weld-line tensile strength commonly falls to 60–70% of the parent-material value. For constrained snap-fits and pressure-retaining covers, weld-line placement is therefore a design control; short-shot studies on the production tool are used because process simulation only approximates local fibre interaction. Mould shrinkage data on ISO 294-4 plaques typically fall in the 0.2–0.6% flow-direction and 0.4–0.8% transverse ranges, but exact values vary with gate location, wall thickness, and mould temperature. Post-mould annealing at 80–120 °C for 2–4 h can relieve frozen-in orientation and improve dimensional stability. Annealing above the amorphous-phase glass-transition range also permits secondary crystallisation and must be validated on the actual part geometry before release.

    Processing Envelope, Drying Threshold, and Residence-Time Ceiling

    Pre-drying is required when residual moisture exceeds 0.10%. Supplier recommendations typically specify drying at 80 °C for 4–8 h in a desiccant dryer with a dew point below −30 °C. If ambient relative humidity is above 60%, opened containers should be maintained in hopper dryers at 80 °C and transfer lines should be closed to avoid intermittent moisture uptake. Melt temperature at the nozzle is usually set at 240–280 °C, while mould-wall temperature is maintained at 60–80 °C. Mould temperatures below 50 °C depress crystallinity and increase post-mould dimensional movement; above 80 °C, cycle time is extended without a significant additional gain in PA12 crystallisation kinetics.

    Screw back pressure in the 3–7 MPa range is sufficient for glass-fibre dispersion when the non-return valve is in good condition. Screw surface speed should be set according to the screw diameter, typically in the 0.1–0.3 m/s range. Shot volume should remain between 50% and 75% of barrel capacity. Total residence time above 260 °C should not exceed 8–10 min; longer residence degrades the PA12 chain and can reduce notched impact by 10–20% when tested to ISO 179-1/1eA. Regrind levels up to 25% are permitted in non-safety-critical parts, but fibre attrition lowers dry tensile modulus and increases lot-to-lot viscosity variability. Melt-volume-flow-rate monitoring to ISO 1133-1 is advisable for incoming lots and after regrind addition.

    When Chlorinated Detergents or Glycol-Water Mixtures Expose a Candidate to Stress Cracking

    In chlorine-containing potable water, environmental stress cracking resistance is a decisive selection criterion. PA12 grades generally exhibit lower crack-growth susceptibility than PA6 or PA66 at equivalent molecular weight, but the advantage decreases when free chlorine concentration exceeds 3 ppm at 60 °C. No design should rely on general PA12 rankings without testing the actual black 9225 formulation under service strain and temperature. The material resists aliphatic and aromatic hydrocarbons, oils, greases, and many neutral aqueous media at ambient temperature. Strong mineral acids, phenols, concentrated formic acid, and oxidising agents degrade polyamide 12; at elevated temperature, acidic hydrolysis proceeds at rates that require thickness and stress derating. For fuel or brake-fluid exposure, the specific additive package of the fluid must be tested. The grade has been used in water-meter bodies, pump impellers, valve housings, pneumatic connectors, and light structural carriers. Published data for this exact FWA black 9225 formulation in direct fuel-line applications is limited; where permeation or swelling limits are regulated, a dedicated fuel-resistant grade from the EMS portfolio or an alternative barrier material should be evaluated.

    Compliance verification for the grade is batch- and region-dependent. Under UL 94, the product is commonly classified HB at 1.6 mm thickness, but the current Yellow Card must be checked for the specific colour and thickness range. The supplier declaration for RoHS 2011/65/EU including delegated amendment 2015/863 and the REACH SVHC threshold of 0.1% w/w should be requested for the exact material code. Potable-water contact approvals are not globally uniform; national or regional certification, such as drinking-water scheme lists, must be confirmed for the end-use market. If the part is used in a regulated water-contact application, testing should cover the finished component because mould release residues, post-mould trimming, and assembled seals may alter extractable content.

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