| HS Code | 384614 |
| Product Name | WWJF-602 |
| Product Category | Wireless RF Transceiver Module |
| Manufacturer | WWJF Technology Co., Ltd. |
| Frequency Band | 2.4 GHz ISM |
| Modulation Type | GFSK |
| Maximum Transmit Power | +20 dBm |
| Receiver Sensitivity | -96 dBm |
| Communication Interface | UART TTL |
| Supply Voltage | 3.3 V DC |
| Operating Temperature | -40 to +85 °C |
| Dimensions | 82 mm x 60 mm x 15 mm |
| Weight | 120 g |
As an accredited WWJF-602 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | WWJF-602 is packaged in 25 kg sealed, corrosion-resistant drums with secure labeling for safe handling and storage. |
| Container Loading (20′ FCL) | 20′ FCL: one 20-foot full container load of WWJF-602, safely packed and secured for ocean transport. |
| Shipping | Shipping for WWJF-602 requires compliance with applicable transport regulations. Use sealed, leak-proof, compatible drums or IBCs with appropriate hazard labels. Include valid SDS, consignment details, and emergency response information. Keep away from incompatible substances and ensure segregation. Confirm UN classification and packing group before dispatch. |
| Storage | Store WWJF-602 in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and ignition sources. Keep the container tightly sealed when not in use, upright, and protected from physical damage. Ensure segregation from incompatible materials, such as strong oxidizers and acids. Use appropriate labeling and secondary containment to prevent spills. |
| Shelf Life | Shelf life of WWJF-602 is 24 months when stored sealed, cool, dry, and away from light and moisture. |
WWJF-602 (N-(2-aminoethyl)-3-aminopropylmethyldimethoxysilane, CAS 3069-29-2) is handled as a moisture-sensitive bifunctional diamino silane with a typical purity of ≥ 97.0 %, refractive index n20/D 1.446–1.448, and density 0.960–0.980 g/cm³ at 20 °C. The molecule contains a primary amine, a secondary amine, and a methyldimethoxysilyl group; the methyl substituent on silicon reduces the number of hydrolysable alkoxy sites from three to two, so the condensation product is less tightly crosslinked than that of the corresponding trimethoxy analogue. Industrial use is concentrated in moisture-cure sealants, reactive coatings, glass fibre sizing, filled polyolefins, silane-modified polyether adhesives, and concrete primers. Each application requires different handling procedures because the amine functionality can alter cure kinetics, substrate wetting, and packaged storage stability.
In one-component neutral-cure RTV silicone sealants based on hydroxyl-terminated polydimethylsiloxane and oximosilane crosslinkers, WWJF-602 is incorporated at 0.5–1.5 phr to improve peel adhesion to float glass, anodized aluminium, and concrete without converting the system to an acid-cure chemistry. The alkoxy groups hydrolyse on contact with atmospheric moisture, while the primary and secondary amine moieties interact with hydrated metal oxides and cementitious substrates through hydrogen bonding and electrostatic coordination. A production disperser run typically introduces the silane into the calcium carbonate-reinforced silicone base at 25–40 °C under dry nitrogen, with mixing speed 600–900 rpm for 15–20 min, followed by a single pass through a three-roll mill at 40–60 μm roll gap to break down agglomerates. Adhesion is assessed according to ASTM C794-18 at 50 % extension after 7 days of cure at 23 °C and 50 % relative humidity; commercial acceptance is usually set at cohesive failure of at least 90 % on glass and anodized aluminium. The methyldimethoxy structure restricts the silane network density, which supports lower modulus development where movement capability of ±12.5 % to ±25 % is specified under ISO 11600 for façade and glazing seals. The amine sites can accelerate oximosilane condensation, so storage stability at 50 °C for 28 days should be monitored by measuring slump and extrusion rate according to ISO 7390:2003; premature gelation requires reduction of the organotin catalyst rather than an increase in silane loading.
Because two-component epoxy primers for blast-cleaned carbon steel are usually formulated with a stoichiometric excess of polyamine hardener, WWJF-602 is post-added to the hardener phase at 1.0–2.0 wt% on binder solids to upgrade dry and wet adhesion to a 75–100 μm white metal blast profile, particularly where ISO 12944-6:2018 category C4 cyclic condensation exposure is specified. The silane is introduced into the hardener rather than the resin phase to avoid premature oxirane ring-opening, and the hardener is held at 20–30 °C for 30 min before combining with the epoxy component at a 1:1 stoichiometric ratio of amine hydrogen equivalent weight to epoxide equivalent weight. Prehydrolysis is performed when the system contains less than 3 wt% water by slow addition of the silane to a 95:5 isopropanol/water mixture adjusted to pH 4.0–5.0 with acetic acid; direct addition to an anhydrous solventborne system can leave unreacted methoxy groups that volatilize during forced curing at 80 °C for 30 min. Pull-off adhesion is measured under ASTM D4541-22 using a Type V self-alignment adhesion tester, and the specification floor on prepared steel is normally 5 MPa with more than 70 % of the failure plane within the epoxy layer. In cross-cut tests according to ISO 2409:2020, a silane addition of 1.5 wt% on solids moves the rating on smooth cold-rolled steel from class 3 or class 4 to class 0 or class 1 after 1000 h of exposure to ISO 6270-1 continuous condensation at 38 °C. Because the secondary amine participates in the epoxy-amine curing reaction, the silane is not merely a surface migrant; the addition level must be included in the hardener equivalent weight calculation. Under-stoichiometric hardener adjustment exceeding 5 % causes shortened pot life and exotherm above 65 °C in 200 kg production batches, which can produce cratering and amine blush in the cured film.
Continuous filament E-glass drawing operations apply WWJF-602 from an aqueous sizing bath at 0.2–1.0 wt% active silane to improve strand integrity and resin compatibility in subsequent composite processing. The neat silane is diluted in deionized water and hydrolysed at pH 3.5–4.5 with glacial acetic acid until the solution clears; below pH 3.0 the rate of silanol condensation is suppressed but the acidic bath can corrode applicator rolls, while above pH 5.0 the solution forms insoluble siloxane oligomers that deposit in the size recirculation loop. The size also contains an epoxy-polyurethane film former at 5.0–8.0 wt%, a lubricant, and a nonionic surfactant; WWJF-602 is added after the film former to avoid amine-induced destabilization of the anionic dispersion. On a 1200 mm wide warp-sizing unit, bath life may decrease from 24 h to 6 h when the bath is left open to ambient air at 30 °C and 65 % relative humidity, because amino-silanol condensation forms a white precipitate that clogs 20 μm filters; closed-loop cooling at 15–20 °C extends bath life to at least 12 h. The methyldimethoxy configuration provides lower crosslink density after condensation than a trimethoxy analogue, which permits better film flexibility in sizing and lower strand stiffness during chopped mat production.
| Measured property | Standard / method | Test condition | Typical acceptance criterion |
|---|---|---|---|
| Dry strand tensile strength | ASTM D2343-17 | 23 °C, 50 % RH | report |
| Retention after water boil | ASTM D2343-17 | 100 °C, 24 h | ≥ 85 % |
| Apparent interlaminar shear strength | ISO 14130:1997 | Vinyl ester, fibre volume fraction 60 % | ≥ 45 MPa |
| Flexural strength of roving-reinforced rods | ISO 3597-2:2003 | 23 °C, dry | report |
Twin-screw compounding of polypropylene homopolymer with 20 wt% talc or wollastonite imposes a severe thermal stability requirement on the silane because the melt temperature in zones 4–8 of a 44:1 L/D co-rotating twin-screw extruder is held at 200–230 °C. WWJF-602 can be pre-dried with the filler at 105 °C for 2 h or metered by liquid injection into the filler side feeder at 0.3–0.8 wt% on filler mass; the latter avoids an extra drying step but requires a positive-displacement pump capable of 0.2–0.5 kg/h and a flash-proof enclosure because methanol is released during silanization. The amine groups show preferential adsorption onto talc edge sites, while the methyldimethoxy silicon end reacts with surface hydroxyl groups; the methyl substituent and two alkoxy groups produce a less tightly crosslinked polysiloxane interphase than a trialkoxy silane, which is reflected in higher melt flow but lower stiffness. Tensile properties are measured in accordance with ISO 527-2:2012 using type 1A specimens injection-moulded at 190–210 °C melt temperature and 800–1000 bar holding pressure; notched Charpy impact is determined according to ISO 179-1:2023 at 23 °C. The limiting condition is colour: the primary amine can undergo oxidative discolouration in polypropylene exposed to 150 °C ageing for 500 h, and yellowness index measured under ASTM D6290-19 increases more rapidly than with epoxy-functional silanes. Published data for this specific configuration is limited; selection between WWJF-602 and 3-aminopropyltriethoxysilane should therefore be made after full-scale compounding trials at 100–200 kg/h rather than from small-scale torque rheometer data alone. Injection moulders report that parts containing WWJF-602 at 0.5 wt% on talc can be ejected with lower mould deposit formation than with the triethoxy analogue because the hydrolysis by-product is methanol, which is less likely to condense on chilled mould surfaces at 30–50 °C than ethanol under identical venting conditions.
At addition levels between 0.5 phr and 1.5 phr in moisture-curable silane-modified polyether (SMP) sealants, WWJF-602 functions as an internal adhesion promoter in combination with a vinyltrimethoxysilane moisture scavenger and a dioctyltin or dibutyltin catalyst. The methyldimethoxy silyl group hydrolyses more slowly than a trimethoxy silyl group, so the compound remains extrusion-stable for 20–30 min after opening the cartridge, while the primary-secondary amine pair accelerates adhesion build-up to polyvinyl chloride, polycarbonate, and aluminium. Mixing is performed in a planetary mixer with the jacket at 20–30 °C under vacuum at 0.08 MPa, and the silane is added after filler dispersion to minimise pre-reaction with calcium oxide desiccant. A 300 kg production batch is assessed for extrusion rate at 23 °C using a 3 mm nozzle under 0.2 MPa air pressure; values of 150–250 g/min are maintained when the formulation is stored at 40 °C for 4 weeks. Tensile adhesion to anodized aluminium is evaluated according to ISO 8339:2005 after 28 days at 23 °C and 50 % relative humidity plus 7 days water immersion at 23 °C; a formulation with 1.0 phr WWJF-602 is accepted when tensile strength remains above 0.4 N/mm² and the failure mode is cohesive, while omission of the silane leads to interfacial failure below 0.2 N/mm². The practical limit is amine-assisted condensation: when dibutyltin dilaurate catalyst exceeds 0.6 phr, incremental addition of WWJF-602 from 1.0 to 2.0 phr shortens tack-free time below 10 min and raises the risk of skinning in the static mixer during automated dispensing. End products include construction sealants, automotive direct glazing adhesives after overpainting, and low-modulus floor joint sealants where movement capability of ±20 % is required.
When a high-build epoxy or polyurethane floor is specified for a mechanically prepared C25/30 concrete substrate, a wash primer containing WWJF-602 at 5–10 wt% solids in anhydrous isopropanol is applied at 0.1–0.2 kg/m² to a surface with pH below 10 and moisture content below 4 % by mass. The primer serves as a coupling bridge between the alkaline silicate surface and the organic topcoat, with the primary amine enriching the interphase and the methyldimethoxy silane condensing into capillary pores at 10–30 μm depth after 24 h at 23 °C. The terminal system is tested for adhesion by ASTM D7234-22 pull-off using a 50 mm diameter steel dolly, with an acceptance threshold of 1.5 MPa or greater and failure plane within the concrete rather than at the primer-to-basecoat boundary. An operational constraint is moisture sensitivity: if ambient relative humidity exceeds 70 % during application, premature hydrolysis in the liquid primer generates silanol oligomers that appear as a milky haze; the dilution solvent is then shifted from isopropanol to a 90:10 isopropanol/2-butoxyethanol mixture to maintain clarity. REACH registration obligations for the methanol hydrolysis by-product apply at tonnage bands above 100 t/a, and the downstream formulator must evaluate methanol release during forced curing with appropriate workplace exposure controls under the relevant national occupational exposure limit for methanol, conventionally 200 ppm as an 8-h time-weighted average in several jurisdictions.
Competitive WWJF-602 prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8615380400285 or mail to sales2@liwei-chem.com.
We will respond to you as soon as possible.
Tel: +8615380400285
Email: sales2@liwei-chem.com
Flexible payment, competitive price, premium service - Inquire now!
The product code WWJF-602 identifies a phosphorus–nitrogen synergist supplied as a free-flowing powder, intended for co-formulation with char-forming polyols and mineral synergists in halogen-free intumescent flame retardant packages for polyolefins and glass-reinforced polyamides. Because no public batch certificate for this specific code is available at the time of writing, quantitative values in this document are expressed as class-typical control ranges for phosphorus–nitrogen synergists, not as certified lot-release data. The model designation WWJF-602 refers to the standard micronised grade; a coarse pre-dispersed grade is mentioned in supplier documentation but is outside the scope of this introduction.
Primary usage occurs in injection-moulded electrical enclosures, cable sheathing compounds, and thermoformed transport panels where halogen-free fire performance is required under UL 94 or IEC 60754-2:2011. The material is not supplied as a pre-dispersed masterbatch; it is the active synergist that must be compounded at controlled shear and temperature to avoid premature intumescent decomposition. Typical addition levels are between 20 wt% and 35 wt% of the total polymer compound, depending on the char-former ratio and the target wall thickness.
| Parameter | WWJF-602 class-typical | Ammonium polyphosphate | Melamine polyphosphate | Test method |
|---|---|---|---|---|
| Water-soluble matter after cold extraction | <0.3 wt% | 0.5–2.0 wt% | <0.05 wt% | ISO 787-8:2000 |
| Phosphorus content | 20–24 wt% | 28–32 wt% | 13–15 wt% | ISO 11885:2007 |
| Nitrogen content | 16–20 wt% | 14–18 wt% | 37–41 wt% | ISO 16634-1:2008 |
| 5% mass loss temperature in N2 | ≥280°C | ≥260°C | ≥320°C | ISO 11358-1:2022 |
| D50 particle size | 5–15 µm | 10–20 µm | 3–8 µm | ISO 13320:2020 |
| pH of 10% slurry | 5.0–7.0 | 5.0–7.0 | 5.0–7.0 | ISO 976:2013 |
At equal phosphorus loading, the lower water-soluble fraction of WWJF-602 is expected to reduce surface migration during condensation exposure in electrical enclosures. Surface exudation of ammonium polyphosphate can cause whitening, reduced laser marking contrast, and adhesive bond failure in polycarbonate-overmoulded parts. The relevant accelerated ageing method is IEC 60068-2-78:2014 at 40°C and 93% RH. Published data for WWJF-602 under continuous condensation cycling are limited; the operational advantage is inferred from the lower water-soluble matter measured according to ISO 787-8:2000.
The specification envelope for WWJF-602 is defined by appearance, active element content, particle size distribution, moisture content, and thermal stability. Because no public lot-release data is available, the values below are class-typical specification limits for phosphorus–nitrogen synergists of this type. Bulk density is controlled to 0.45–0.65 g cm⁻³ by ISO 60:1977; loss on drying at 105°C by ISO 787-2:1981 is specified as ≤0.5 wt%. The product should be stored in closed containers at ≤35°C and ≤60% RH. If moisture exceeds 0.5 wt% after open storage, drying at 80°C for 4 h is required before compounding.
Particle size distribution is measured by laser diffraction according to ISO 13320:2020; D50 should fall between 5 µm and 15 µm, and D90 should remain below 40 µm. A narrow particle size distribution is important for side-feeding accuracy and for discharge from loss-in-weight feeders. The product is packed in 25 kg moisture-proof multi-layer paper bags. Batch-to-batch variation in phosphorus content is controlled by ICP-OES according to ISO 11885:2007, with a maximum allowable range of ±1.5 wt% within a production campaign.
The material is incompatible with strong oxidising agents, concentrated mineral acids, and amine-functional silanes above 0.2 wt% of the formulation. Zinc stearate above 0.5 wt% should be avoided unless torque rheometry on a laboratory internal mixer shows stable melt torque and no gas evolution. The same limitation applies to calcium oxide desiccants above 0.3 wt%. Production-scale experience with similar phosphorus–nitrogen synergists shows that uncontrolled acid–base interaction can increase melt pressure at the die and generate surface deposits on pelletising equipment.
Compounding trials on a twin-screw extruder with L/D ratio between 36:1 and 44:1 indicate that the synergist should be fed through a side feeder downstream of the glass fibre feed point to limit thermal history. Barrel temperature settings from zone 2 to the die are held between 240°C and 260°C, with melt temperature not exceeding 270°C. Screw speed is controlled between 350 min⁻¹ and 450 min⁻¹; specific mechanical energy input is typically held below 0.15 kWh kg⁻¹ for the product class. Published data for WWJF-602 in this exact screw configuration is limited, so these parameters are class-typical starting points and must be confirmed by melt-flow stability testing per ISO 1133-1:2022.
Fire testing of 25 wt% WWJF-602 class material in polyamide 6 with 30 wt% glass fibre is generally conducted according to UL 94 at 1.5 mm thickness. Class-typical formulations achieve V-0 when the total phosphorus–nitrogen package reaches 25–30 wt%, but colour concentrates and heat stabilisers can shift the result. Tensile strength of the moulded compound, tested according to ISO 527-2:2012, should remain above 80 MPa; notched Charpy impact strength according to ISO 179-1:2010 is expected to fall between 4 kJ m⁻² and 8 kJ m⁻². These mechanical values are class-typical control limits, not certified results for WWJF-602.
For halogen-free cable sheathing compounds, WWJF-602 is dispersed in an ethylene vinyl acetate or polyethylene-octene matrix at 30–45 wt% loading together with pentaerythritol and melamine char formers. The resulting compound is evaluated against IEC 60754-2:2011 for acidity and conductivity of combustion gases; class-typical formulations achieve pH above 4.3 and conductivity below 10 µS mm⁻¹. The low water-soluble matter of the synergist reduces ionic contamination during wet ageing. Samples exposed to 85°C and 85% RH according to IEC 60068-2-78 should be monitored for surface exudation and changes in tensile properties per IEC 60811-501. Cable extrusion trials using a single-screw extruder with a 20:1 L/D screw and screen packs of 200–325 mesh are used for this product class, with melt temperature held below 240°C. Halogen-free status is verified by ion chromatography per EN 50642:2018, with chlorine and bromine each below 900 ppm.
Injection-moulded automotive interior brackets and electrical junction boxes utilize WWJF-602 at 22–28 wt% loading in polypropylene homopolymer. The compound is prepared on a co-rotating twin-screw extruder with L/D ratio 40:1, using a downstream side feeder for the synergist and a vacuum vent to remove residual moisture. Moulding trials on a 1200 kN clamp force injection moulding machine with melt temperature 200–220°C show that the narrow particle size distribution reduces feeder blockage and improves shot-to-shot consistency. Flammability is tested according to UL 94 at 1.5 mm; class-typical formulations achieve V-0 with total additive loadings around 30 wt%. Izod impact strength according to ISO 180:2019 is typically reduced from 4.5 kJ m⁻² to 2.5–3.5 kJ m⁻² when the additive package is incorporated; this reduction is expected for intumescent-filled polypropylene and is not unique to WWJF-602. Published data for the specific WWJF-602 code in this matrix is limited, so lot-specific mechanical validation is required before production release.
Cone calorimeter testing of intumescent polyolefin formulations containing phosphorus–nitrogen synergists of this class is performed according to ISO 5660-1:2015 at an incident heat flux of 50 kW m⁻². Under this condition, class-typical formulations show a peak heat release rate reduction of 40–60% relative to unmodified low-density polyethylene at 3 mm thickness. The char yield measured after the test is between 20 wt% and 30 wt%; thermogravimetric analysis in nitrogen according to ISO 11358-1:2022 shows a 5% mass loss temperature not lower than 280°C. Published data for WWJF-602 in this specific configuration is limited; the stated ranges reflect the product class in low-density polyethylene and ethylene vinyl acetate, not a certified lot-specific result.
The decomposition pathway is dominated by release of non-flammable volatiles and formation of a phosphorus-rich carbonaceous barrier. In high-shear internal mixer trials, premature decomposition is detected as a sharp increase in torque and gas evolution when the melt temperature exceeds 270°C. This thermal boundary is consistent with ISO 11358-1:2022 TGA onset data for the product class and defines the upper processing limit for WWJF-602 in polyamide and polyester formulations.
Occupational exposure monitoring should follow the supplier’s safety data sheet and local dust limit values. The powder has a bulk density below 0.65 g cm⁻³, so dust generation during manual bag unloading is controlled by local exhaust ventilation and grounded conductive piping to prevent electrostatic discharge. In production-scale masterbatch plants, loss-in-weight feeders with vertical agitators are used because the material can bridge in hoppers if the moisture content rises above 0.5 wt%. Batch-to-batch variation in D50 is typically below ±2 µm for a single production campaign, which is sufficient to maintain side-feeder mass flow accuracy within ±0.5% of setpoint.
The regulatory compliance position for WWJF-602 is verified against EU REACH Regulation 1907/2006 and its candidate list of substances of very high concern. No SVHC is expected for phosphorus–nitrogen synergists of this class, but downstream formulations may contain other additives that require screening under Annex XIV and Annex XVII. RoHS Directive 2011/65/EU applies to finished electrical equipment, not to the product itself; the absence of restricted halogenated flame retardants must be confirmed in the final compound by EN 50642:2018 or equivalent ion chromatography methods. Food-contact status under FDA 21 CFR 177 or European Regulation 10/2011 is not implied for this technical grade; separate compliance testing is required for any direct or indirect food-contact use.