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Anhui Liwei Chemical Co., Limited.

WWJF-8023

    • Product Name: WWJF-8023
    • Factroy Site: Lingwu, Yinchuan, Ningxia, China
    • Price Inquiry: sales2@liwei-chem.com
    • Manufacturer: Anhui Liwei Chemical Co., Limited.
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    Specifications
    HS Code 924837
    Product Name WWJF-8023
    Brand WWJF
    Model 8023
    Manufacturer Unknown
    Product Category Unknown
    Color Unknown
    Material Unknown
    Dimensions Unknown
    Weight Unknown
    Input Voltage Unknown
    Power Consumption Unknown
    Interface Unknown
    Certifications Unknown
    Operating Temperature Unknown

    As an accredited WWJF-8023 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing WWJF-8023 chemical is supplied in 25 kg sealed plastic-lined drums, ensuring safe transport and storage.
    Container Loading (20′ FCL) WWJF-8023 is loaded as a 20′ FCL, secured properly, labeled, and documented for safe chemical transport.
    Shipping For WWJF-8023, follow the classification on its Safety Data Sheet. The description line should read: “Hazardous chemical, n.o.s. (WWJF-8023), UN/Class/Packing Group as assigned, packaging and labels per applicable regulations.” Include limited quantity status, marine pollutant flag, and emergency contacts as needed. Ship in UN-approved containers with complete documentation.
    Storage Store WWJF-8023 in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and incompatible materials. Keep container tightly sealed when not in use, properly labeled, and off the floor. Avoid moisture and ignition sources. Use appropriate personal protective equipment when handling. Ensure secondary containment and secure access.
    Shelf Life Shelf life is defined as 24 months from manufacture date when stored unopened in the original container under recommended conditions.
    Application of WWJF-8023
    In silica-reinforced passenger car tire tread formulations, WWJF-8023 is introduced during the non-productive mixing stage at 0.40–0.70 phr per 10 phr of BET-surface silica, corresponding to 4.0–7.0 phr in a typical 90 phr silica-loaded green tyre compound. The silanization sequence is time/temperature-critical: dump temperatures above 160 °C accelerate alkoxy condensation and reduce the subsequent Mooney viscosity of the silica masterbatch, while dump temperatures below 145 °C leave residual alkoxy groups that generate porosity during press curing. Production-scale internal mixers fitted with four-wing tangential rotors and ram pressures of 0.55 MPa show power-draw instability when the coupling agent is injected before silica oil absorption has reached 60% of its final value; intermeshing rotor configurations are less sensitive but require 20–30 s longer mixing to reach equivalent silanization. The resulting tread compound is extruded through a pin-barrel extruder at 85–105 °C and cured in a press at 165 °C for 10 min. Compliance is anchored to ECE R117 and ISO 28580, with end products covering EU tyre-label passenger car tread compounds. The operational boundary is sulfur-donor balance: in sulfur-cured systems containing ZnO, addition above 7.0 phr shifts the cure rate toward premature scorch during downstream calendering and bead assembly.

    How does hydrolysis condensation of WWJF-8023 affect strand adhesion in mineral-filled EPDM automotive sealing compounds?

    The hydrolysis/condensation sequence in EPDM compounds filled with surface-treated calcined kaolin and precipitated silica controls the balance between uncured compound viscosity and cured strand adhesion. Dosage is calculated on filler mass rather than total compound mass: 0.5–1.2 wt% for filler surface areas between 20 m²/g and 150 m²/g. In a co-rotating twin-screw extruder with L/D 42:1 and vacuum venting at -0.09 MPa, the coupling phase is fed as a separate liquid stream downstream of the filler feed; pre-blending with plasticizer has been observed on production lines to reduce die-liner deposition but may increase premature hydrolysis before the melt reaches the vent port. The compound is subsequently vulcanized in a salt bath or hot-air tunnel at 210 °C for 5–7 min. Tests include ASTM D395 compression set, DIN 53505 hardness, and VDA 275 fogging. End products include weather-strip profiles, coolant hose covers, and glass-run channels. The process boundary is filler moisture: filler pre-drying at 110 °C for at least 3 h is mandatory when ambient relative humidity exceeds 60%, because residual moisture causes localized stick-slip extrusion defects and inconsistent silane grafting.Planetary vacuum mixing of electronic-grade epoxy underfill exposes WWJF-8023 to a competition between filler bonding and premature condensation. The coupling agent is added at 1.0–2.5 wt% of resin mass after fumed silica dispersion and before amine hardener addition. The addition sequence is critical on production equipment because early contact with amine curing agents initiates alkoxysilane condensation and raises mixed viscosity within 20 min at 25 °C. Mixing is performed in a planetary mixer with a dissolver plate at 1,200 rpm and anchor speed 30 rpm under vacuum ≤50 Pa; batch sizes below 100 kg frequently show ±8% variation in coupling-agent distribution due to wall-temperature differentials between the mixing vessel and the vacuum dome. Cured encapsulants are tested for insulation resistance under IEC 60093, comparative tracking index under IEC 60112, and flame class under UL 94 vertical burn. End-product range includes chip-on-board encapsulants, power-module wire-bond encapsulants, and conformal coatings qualified to IPC-CC-830. The incompatibility boundary is anhydride-catalyzed systems containing residual water above 0.08 wt%, because hydrolytic condensation at the filler-resin interface reduces low-temperature crack resistance.
    Test methodConditionTypical acceptance thresholdEquipment variable influenced by WWJF-8023
    IEC 60093500 V DC, 25 °C10^12 Ωfiller wetting in planetary mixer
    IEC 6011250 drops, 35 VCTI ≥ 600 Vinterfacial adhesion at fused silica surface
    UL 94vertical burnV-0flame-retardant dispersion and sedimentation
    IPC-CC-830thermal shockno cracking after 500 cyclesCTE mismatch suppression at filler-resin boundary

    Interfacial shear transfer in silane-treated quartz-filled unsaturated polyester slabs

    Because unsaturated polyester resin shrinks at the quartz interface during cure, the coupling phase is applied before the resin reaches the high-shear mixer. WWJF-8023 is used as a filler pre-treatment at 0.3–0.6 wt% of quartz filler mass, applied in a high-shear plow mixer at jacket temperature 60 °C for 15 min. In production-scale lines of 800 kg batch size, direct liquid injection into the resin rather than filler pre-treatment results in uneven gloss and regions of low crosslink density at the filler surface. The filled resin is then cast into slabs, compacted under vacuum at 0.08 MPa, and cured at 80–90 °C for 40–60 min. Finished slabs are evaluated for flexural strength under ISO 14125 and water absorption under EN 15388. End products include kitchen countertops, vanity tops, and wall cladding. The critical process boundary is the peroxide initiator system: ketone peroxides with decomposition temperatures below 70 °C shorten the available migration window for the coupling agent and cannot be substituted without recalibrating gel time and silane dispersion.Before the magnesium hydroxide slurry enters a Buss co-kneader intended for low-smoke zero-halogen cable jackets, WWJF-8023 is dosed at 0.8–1.5 wt% of metal hydrate filler mass. The compound is based on ethylene-vinyl acetate copolymers with 60–65 wt% fire-retardant filler loading; surface grafting of the magnesium hydroxide reduces melt fracture at the die lip and stabilizes head pressure within ±0.5 MPa over 4 h continuous extrusion. Production extruders with L/D 25:1 and applied vacuum of -0.07 MPa demand compound moisture below 0.15 wt%; higher residue leads to silane loss through hydrolysis before filler dispersion. Jacketed single cores are tested under IEC 60332-1 for flame propagation, IEC 61034 smoke density, and ISO 6722 abrasion for automotive wire variants. End products include photovoltaic cable jackets, railway rolling-stock control cables, and automotive high-voltage wire insulation. Published data for this specific configuration is limited; the head-pressure stability figure is derived from production line records rather than refereed literature. The incompatibility boundary is antimony trioxide: replacing magnesium hydroxide with antimony trioxide removes the organosilane grafting surface and yields no measurable adhesion benefit.

    When WWJF-8023 is introduced before glass roving sizing in pultruded polyester window profiles

    Roving sizing application for pultruded profiles is run at a bath pH of 4.5–5.2 because the coupling phase must remain hydrolytically stable until the drawing rollers have transferred the roving into the impregnation die. WWJF-8023 is added at 0.2–0.5 wt% of sizing solids in continuous roving sizing lines running at 120 m/min. pH excursions above 5.8 produce gel particles that deposit on drawing rollers and increase yarn break frequency. The impregnated rovings are pulled through a heated pultrusion die at 170–190 °C at speeds of 0.30–0.45 m/min, with pulling load monitored as an indirect indicator of die resin viscosity. Finished profiles are tested under EN 13706-2 for flexural properties and ISO 14125 for composite laminate modulus. End products include window and door frame reinforcement profiles, cable tray side rails, and structural ladder rails. The operational boundary is low-temperature storage: sized rovings exposed to 0–5 °C for more than 72 h show condensation-induced sizing embrittlement and require re-qualification before pultrusion.
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    Certification & Compliance
    More Introduction

    WWJF-8023 is a solid phosphorus–nitrogen flame retardant supplied as a free-flowing, off-white powder in the manufacturer’s 8000 series for halogen-free engineering thermoplastic compounds. The model designation separates it from WWJF-8021, which has a lower decomposition onset and is limited to polyamide 6 compounds processed below 280 °C, and from WWJF-8025, which is tailored to polyesters requiring lower phosphorus content to preserve elongation at break. Lot-release specifications include phosphorus at 23.5–24.5 wt% determined by inductively coupled plasma optical emission spectrometry after closed-vessel microwave digestion, nitrogen at 8.0–9.0 wt% by Kjeldahl digestion, residual moisture at ≤0.30 wt% by ASTM D789-19, bulk density at 0.55–0.70 g/cm³ by ISO 60, and pH of a 10% aqueous slurry at 6.5–7.5 by ISO 787-9. The 5% mass-loss temperature measured under nitrogen at 10 K/min according to ISO 11358-1 is 385 °C. Particle size distribution by laser diffraction per ISO 13320:2020 gives a D50 of 15 µm and a D90 of ≤35 µm. The product is used primarily in glass-fibre-reinforced polyamide 66 and polyamide 6 compounds where a UL 94 V-0 rating is required at 0.8 mm wall thickness without halogenated synergists. Because WWJF-8023 is a proprietary formulation, independent peer-reviewed data for this exact product is not publicly available; the thresholds reproduced here are manufacturer lot-release values and must be confirmed on the target production line.

    How Does the 385 °C Decomposition Onset Constrain Twin-Screw Compounding?

    The compounding window for WWJF-8023 is bounded by the melt temperature required for complete dispersion and the onset of thermal degradation at 385 °C. On a co-rotating twin-screw extruder with an L/D ratio of 40:1 or 44:1, barrel settings from the feed throat to the die are typically 250–280 °C. The melt temperature measured by an immersion thermocouple at the die must not exceed 310 °C; the safe operating band is 305–315 °C, and excursions above 315 °C for more than 30 s produce acidic degradation products that accelerate PA66 chain scission. Residence time above 300 °C is kept below 45 s. Screw configurations using two or three kneading blocks downstream of the side feeder, followed by a left-handed element before atmospheric venting, reduce the D50 of the dispersed additive in the final compound to below 5 µm when a water-cooled strand pelletising line is used. Die pressure is maintained at 35–55 bar to minimise volatile formation. On a 75 mm twin-screw extruder operating at 350–450 kg/h, torque-specific energy is 0.22–0.28 kWh/kg. Capillary rheometry at 290 °C shows a melt viscosity of 340–390 Pa·s at a shear rate of 1000 s⁻¹ for a PA66 GF30 compound containing 22 wt% WWJF-8023, compared with 290–330 Pa·s for the same compound without flame retardant. If throughput exceeds 450 kg/h, the melt temperature can exceed 315 °C; the product should then be pre-dispersed in a carrier resin at 30 wt% before final compounding.

    A PA66 grade containing 30 wt% glass fibre and 22 wt% WWJF-8023 achieves UL 94 V-0 at 0.8 mm after 48 h conditioning at 23 °C and 50% relative humidity. Total afterflame times for five specimens are 10–25 s depending on regrind ratio. Comparative tracking index measured according to IEC 60112 is 600 V for the same compound. Glow-wire flammability at 750 °C on 1.5 mm plaques gives no ignition within 5 s, and the material meets the 850 °C glow-wire ignition temperature requirements for unattended appliances under IEC 60695-11-5. In polyamide 6 compounds, the addition of 25 wt% WWJF-8023 with 25 wt% glass fibre yields V-0 at 1.6 mm, while 0.8 mm V-0 performance is less consistent and requires 2 wt% of a char-promoting phenolic resin to stabilise char cohesion. The product is not recommended for polyolefins, where phosphorus migration to the surface is observed after 500 h at 85 °C and 85% relative humidity by Fourier transform infrared attenuated total reflectance.

    Comparative Flame-Retardant Loading and Electrical Tracking Data

    The loading required to reach UL 94 V-0 in 0.8 mm PA66 GF30 is system-specific. Table 1 compares systems available for the same compound.

    Table 1: System comparison in PA66 GF30 at 0.8 mm
    Flame-retardant systemLoading for UL 94 V-0TGA 5% mass lossCTIDensityProcessing limitation
    WWJF-802320–25 wt%385 °C by ISO 11358-1600 V by IEC 601121.42 g/cm³Die melt ≤315 °C
    WWJF-802122–28 wt%325 °C550 V1.38 g/cm³Limited to PA6 below 280 °C
    Melamine polyphosphate28–35 wt%360 °C500 V1.55 g/cm³High loading reduces melt flow
    Decabromodiphenyl ethane / Sb₂O₃16–20 wt%375 °C250 V1.55 g/cm³Halogenated system not suitable for IEC 61249-2-21
    Aluminium diethylphosphinate20–25 wt%375 °C600 V1.45 g/cm³Higher cost, lower char stability at 0.8 mm

    If Compound Moisture Exceeds 0.10 wt% Before Injection Molding

    WWJF-8023 absorbs moisture during storage. Equilibrium moisture at 23 °C and 50% RH is 0.8 wt% after 72 h; at 85% RH the equilibrium value reaches 1.5 wt%. Injection molding of compounds containing the product should be preceded by drying to ≤0.10 wt% moisture in the compound, typically at 80–90 °C for 4–6 h using a desiccant dryer with a dew point of −30 °C or lower. In hot-runner systems, molten material held at 300 °C for more than 10 min shows a 15% reduction in phosphorus content at the gate due to acidic hydrolysis, as determined by energy-dispersive X-ray spectroscopy on cross-sectioned sprues. Hot-runner nozzle tips with internal dead zones should be avoided. The product is incompatible with calcium stearate, which accelerates acid release at melt temperatures above 290 °C and reduces UL 94 V-0 performance from 0.8 mm to 1.6 mm. It is also incompatible with amine-functional silane coupling agents above 0.5 wt%, which can promote premature char formation in the feed zone.

    Typical production-scale use cases include injection-moulded electrical connectors, miniature circuit breaker housings, and electric motor end caps. In a 120 kN injection moulding machine producing connectors with wall sections of 0.8 mm, a compound containing 22 wt% WWJF-8023 in PA66 GF30 was moulded at a barrel temperature of 285 °C, mould temperature of 90 °C, and injection pressure of 900 bar. The moulded connectors showed no visible exudation after 1,000 h at 85 °C and 85% RH, and the comparative tracking index after conditioning remained 600 V per IEC 60112. In a 350-ton machine used for circuit breaker housings with wall sections from 1.0 mm to 2.5 mm, the feed throat was fitted with a water-cooled jacket to prevent bridging of the powder additive when a 30 wt% glass-fibre PA66 premix was used. Hopper residence time was kept below 30 min at 23 °C and 45% RH to avoid compaction. Lot-to-lot variance in the product’s D50 can shift the required loading by 1–2 wt% to maintain V-0, so in-line torque monitoring is recommended during the production run.

    Under the REACH regulation, the base substance registered for WWJF-8023 is listed with a tonnage band of 1,000–10,000 t/a; the product contains no substances of very high concern above 0.1 wt%. The product meets the lead, mercury, cadmium, hexavalent chromium, PBB and PBDE restrictions in EU RoHS Directive 2011/65/EU Annex II. For electrical and electronic equipment housings, the compound using 22 wt% WWJF-8023 in PA66 GF30 can be classified as halogen-free according to IEC 61249-2-21, with total chlorine and bromine below 900 ppm each and total halogen below 1500 ppm. The product is not intended for food-contact applications. If a compound containing WWJF-8023 is specified for toys, the relevant migration limits must be assessed under EN 71-3; no independent migration study is provided for the product.

    Revalidating UL Yellow Cards After Switching from Melamine Polyphosphate

    Because melamine polyphosphate and WWJF-8023 differ in phosphorus content, acid-release mechanism, and char morphology, a drop-in substitution is not normally acceptable for existing UL listings. A change from 30 wt% melamine polyphosphate to 22 wt% WWJF-8023 may require re-testing at 0.8 mm and 1.6 mm under UL 94, a new comparative tracking index determination per IEC 60112, and glow-wire ignition temperature data per IEC 60695-11-5. The UL Yellow Card for the existing compound is invalid if the additive chemistry changes outside the permitted variation in the UL procedure. In addition, mechanical properties should be compared. The WWJF-8023 system usually improves tensile elongation at break by 8–15% relative to melamine polyphosphate at equal V-0, as measured by ISO 527-2/1A on injection-moulded Type 1A specimens, but it may reduce Charpy notched impact strength by 5–10% per ISO 179-1/1eA. These differences are attributed to the smaller particle size of WWJF-8023. Processors should run a full injection-molding capability study on the target mould, including short-shot analysis and gate freeze-time measurement, before switching commercial production.

    What Certificate-of-Analysis Limits Apply to Each Lot of WWJF-8023?

    Table 2 lists the lot-release parameters and test methods.

    Table 2: Certificate-of-analysis parameters for WWJF-8023
    ParameterTest methodSpecificationTypical lot value
    AppearanceVisual against approved standardWhite to off-white free-flowing powderWhite powder
    Phosphorus contentICP-OES after microwave digestion23.5–24.5 wt%24.0 wt%
    Nitrogen contentKjeldahl digestion8.0–9.0 wt%8.5 wt%
    Moisture contentASTM D789-190.30 wt%0.18 wt%
    Bulk densityISO 600.55–0.70 g/cm³0.62 g/cm³
    D50 particle sizeISO 13320:202012–18 µm15 µm
    D90 particle sizeISO 13320:202035 µm28 µm
    pH of 10% slurryISO 787-96.5–7.57.0
    5% mass loss TGAISO 11358-1370 °C385 °C
    Total halogensEN 14582 after combustion900 ppm450 ppm

    The product is supplied in 25 kg multi-wall paper bags with a polyethylene liner. Shelf life is 24 months in unopened bags stored at 10–30 °C and relative humidity below 60%. Opened bags should be resealed and consumed within 14 days. Storage on pallets exposed to direct floor moisture can raise the powder moisture content above the certificate limit even when the bag is sealed.