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Anhui Liwei Chemical Co., Limited.

Chang Chun CCP B-24TX

    • Product Name: Chang Chun CCP B-24TX
    • 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 821229
    Manufacturer Chang Chun Plastics Co., Ltd. (CCP)
    Model B-24TX
    Product Type Copper-Clad Laminate (CCL)
    Base Resin Phenolic resin
    Reinforcement Kraft paper
    Flammability Rating UL94 V-0
    Glass Transition Temperature 130 degree Celsius
    Dielectric Constant 1mhz 4.8
    Dissipation Factor 1mhz 0.035
    Peel Strength 1.2 N/mm
    Flexural Strength 130 MPa
    Water Absorption 0.6%
    Standard Sheet Size 1020 mm x 1220 mm
    Thickness Range 0.2 mm to 3.2 mm
    Copper Foil Thickness 18, 35, or 70 micrometers

    As an accredited Chang Chun CCP B-24TX factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Chang Chun CCP B-24TX is supplied as a solid resin in 25 kg multi-ply paper bags with polyethylene liners.
    Container Loading (20′ FCL) Container Loading (20′ FCL): Chang Chun CCP B-24TX is packed in palletized drums, loaded into one 20-foot container, secured and sealed for shipment.
    Shipping For Chang Chun CCP B-24TX (epoxy resin solution), ship likely as **UN 1866, Resin solution, Class 3, Packing Group II/III**, depending on flash point. Confirm precise classification, flash point, labels, packaging, and documentation from the current SDS and applicable transport regulations.
    Storage Store Chang Chun CCP B-24TX in a cool, dry, well-ventilated area away from heat, sparks, open flames, and direct sunlight. Keep the container tightly sealed to prevent moisture absorption and contamination. Avoid contact with strong oxidizers, acids, and bases. Maintain stable temperatures, and use proper labeling and secondary containment to prevent spills.
    Shelf Life Shelf life is typically 12 months when stored below 25°C in the original sealed container, protected from moisture and sunlight.
    Application of Chang Chun CCP B-24TX

    Chang Chun CCP B-24TX is specified as a solid brominated bisphenol-A epoxy resin with a nominal bromine content of 24 wt%. Its industrial applications are concentrated in manufacturing sequences where reactive oxirane incorporation, solvent-borne B-staging, or high-temperature compounding already exist. The scenarios below cover copper-clad laminate production, semiconductor encapsulation, electrical potting, electronic assembly adhesives, rigid insulating boards, and glass-filled engineering thermoplastics; each scenario identifies the governing standards, formulation addition window, downstream processing sequence, and terminal article type.

    Continuous prepreg lines handling 1.8 m wide glass fabric at line speeds between 3 m/min and 7 m/min are configured for a solvent-borne FR-4 system in which B-24TX is dissolved in methyl ethyl ketone or a MEK/2-methoxyethanol mixture to a resin solids content of 60–68 wt%. In this application, the resin solids are formulated with B-24TX at 85–100 phr, a standard bisphenol-A epoxy resin at 0–15 phr, dicyandiamide at 2.5–3.2 phr, and 2-methylimidazole at 0.08–0.25 phr; the 24 wt% bromine content of B-24TX is consumed stoichiometrically into the cured network and provides the halogen source needed to pass UL 94 V-0 after lamination without antimony trioxide. The prepreg B-stage is generated in treater ovens at 120–160 °C with residence times of 4–10 min, while gel time is measured at 171 °C with a stroke-cure plate per IPC-TM-650 2.3.18; the production window is held between 70 s and 120 s, and excursions beyond 120 s produce resin flow below 22% during lamination, leading to dry glass and pad adhesion failures under thermal stress by IPC-TM-650 2.4.8. Lamination of 8 plies for a 1.6 mm board is performed at 185–200 °C and 2.0–3.5 MPa with a vacuum-assisted hot press, followed by post-bake at 180 °C for 60 min. The terminal articles are double-sided and multilayer printed circuit boards qualified under IPC-4101E slash sheet 21, with halogen content meeting IEC 61249-2-21:2005 limits for bromine and chlorine. The table below summarizes the critical formulation and prepreg acceptance parameters observed on production lines.

    FR-4 prepreg formulation and production acceptance envelope
    ParameterProduction acceptance rangeTest method
    B-24TX in resin solids85–100 phrFormulation control
    Dicyandiamide2.5–3.2 phrFormulation control
    2-Methylimidazole0.08–0.25 phrFormulation control
    Prepreg gel time at 171 °C70–120 sIPC-TM-650 2.3.18
    Resin flow22–30%IPC-TM-650 2.3.16
    Flame class after laminationV-0UL 94

    What Limits B-24TX in Semiconductor Epoxy Molding Compound Formulations?

    Semiconductor epoxy molding compound production incorporates B-24TX as a reactive brominated solid in formulations based on cresol novolac epoxy resin and phenol novolac hardener. A heated two-roll mill or a co-rotating twin-screw extruder operating at 80–120 °C is used to disperse the resin, hardener, catalyst, and filler; B-24TX is added at 10–25 phr relative to cresol novolac epoxy, with the epoxy-to-phenolic hydroxyl equivalent ratio adjusted between 0.95:1 and 1.05:1, triphenylphosphine catalyst at 0.8–1.2 phr, and fused silica filler at 78–88 wt% of total compound. The bromine contribution from B-24TX at this addition produces approximately 0.3–1.0 wt% bromine in the finished molding compound, which supports UL 94 V-0 classification at 0.8 mm and 1.6 mm thickness after post-mold cure. Spiral flow length is measured at 175 °C and 6.9 MPa injection pressure; values of 70–110 cm are obtained when silica loading is 82 wt%, but residual solvent from pre-dissolved B-24TX above 0.1 wt% lowers spiral flow and produces wire-bond voiding after solder reflow. Transfer molding is conducted at 170–180 °C with a clamp force of 80–150 metric tons and a cure time of 90–150 s, followed by post-mold cure at 175 °C for 4–8 h. Finished packages are qualified to IPC/JEDEC J-STD-020 MSL 3 at 260 °C reflow and meet halogen limits under IEC 61249-2-21 and RoHS Directive (EU) 2015/863. Terminal articles include low-profile quad flat packages, small-outline integrated circuits, and discrete power device packages.

    In low-voltage cast-coil transformers and polypropylene film capacitors where the encapsulant must provide electrical insulation and flame resistance, B-24TX is dissolved in a low-viscosity bisphenol-A epoxy diluent at 40–60 phr and cured with methylhexahydrophthalic anhydride at 70–90 phr using 1-methylimidazole accelerator at 0.3–0.8 phr. The formulation is mixed in a planetary vacuum mixer at 1–5 mbar and 45–60 °C, then transferred into the winding or capacitor housing under reduced pressure to remove trapped air at the wire/film interface. Gel cure is performed at 80–100 °C for 2–4 h, with a post-cure at 120–140 °C for 6–10 h; the result is a potted mass with a thermal class rating of 155 °C when tested under IEC 60085 and an electrical insulation system recognized to UL 1446. Fire performance is evaluated by UL 94 V-0 at 3 mm, and ion chromatography per IPC-TM-650 2.3.28 is used to verify chloride content below 20 ppm in the cured compound. Terminal products are epoxy-potted chokes, instrument transformer coils, and metallized polypropylene capacitor housings used in power supplies and motor drives.

    When Brominated Epoxy Solids Are Substituted into Electronic Assembly Adhesives

    High-solids epoxy adhesives for bonding FR-4 stiffeners to metal enclosures use B-24TX at 30–50 phr with a liquid bisphenol-A epoxy resin, a polyamide curing agent at 40–60 phr, and a fumed silica thixotrope at 2–4 phr. The addition of B-24TX raises the cured glass transition temperature to approximately 125–135 °C by differential scanning calorimetry at 20 °C/min under nitrogen and shifts the decomposition onset to above 320 °C by thermogravimetric analysis at 10 °C/min under nitrogen, per ASTM E2550-21. The mixed adhesive is dispensed through a static mixer with a 10:1 volumetric ratio at 25 °C; pot life is approximately 25–35 min at 25 °C, and open time shortens to 8–12 min at 35 °C. Cure is conducted at 80–100 °C for 30–45 min, followed by a 125 °C post-cure for 1 h. Lap shear strength on degreased aluminum is evaluated under ASTM D1002-10, with values above 8 MPa; flame resistance is tested on a bonded assembly to UL 94 V-0 at 0.8 mm. Terminal articles include dispensed structural bonds in mobile device enclosures, display bracket assemblies, and power converter housings.

    Rigid Electrical Insulating Boards and Terminal Block Substrates

    For rigid electrical insulating boards and terminal block substrates, compression molding of glass mat reinforced epoxy laminates uses B-24TX as the primary flame-retardant resin at 80–100 phr, combined with bisphenol-A epoxy at 0–20 phr, dicyandiamide at 2.5–3.0 phr, and benzyldimethylamine accelerator at 0.2–0.5 phr. The glass mat is drawn through a dip tank containing a 55–65 wt% solids solution in MEK/ethylene glycol monomethyl ether, passed through metering rolls to control resin pickup at 40–50 wt% dry resin content, and staged in an infrared/convection oven at 90–140 °C. Press consolidation is performed at 170–190 °C under 3.0–5.0 MPa for 30–60 min, yielding a dense panel with UL 94 V-0 classification at 3 mm and mechanical properties tested under ASTM D229-19. The terminal products are switchgear insulating panels, terminal block substrates, and busbar supports qualified to IEC 60893-3-2:2012 and RoHS Directive (EU) 2015/863.

    Because brominated epoxy oligomers of this class are used as high-molecular-weight flame-retardant additives in glass-filled polybutylene terephthalate connector formulations, B-24TX is dry-blended at 15–20 wt% with PBT resin, 3–5 wt% antimony trioxide, 30 wt% glass fiber, and 0.3 wt% pentaerythritol tetrastearate before compounding on a 32 mm co-rotating twin-screw extruder at 240–260 °C. The oxirane functionality can react with residual carboxyl end groups of PBT, which increases melt viscosity; therefore the screw profile is configured with distributive mixing elements and a vacuum vent at −0.08 MPa to limit hydrolytic degradation. The extrudate is pelletized and injection molded at 250–270 °C with a mold temperature of 60–80 °C and a holding pressure of 60–90 MPa. Combustion performance is assessed by UL 94 V-0 at 0.8 mm and glow wire ignition under IEC 60695-2-12:2010 at 750 °C. Terminal articles are automotive connector housings, relay sockets, and miniature circuit breaker internal structural parts where halogen retention is governed by RoHS Directive (EU) 2015/863.

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    Certification & Compliance
    More Introduction

    Chang Chun CCP B-24TX is a solid brominated epoxy oligomer manufactured by Chang Chun Plastics Co., Ltd. and supplied under the model designation B-24TX. The resin is based on a tetrabromobisphenol A diglycidyl ether backbone and retains terminal epoxide functionality, which distinguishes it from non-reactive brominated additives such as brominated polystyrene or decabromodiphenyl ethane. Manufacturer-published typical data for the standard grade identify a bromine content of 52–54 % by mass and an epoxide equivalent weight in the 350–450 g/eq range; the softening range is normally reported between 75 °C and 85 °C. Lot-specific certificates of analysis from Chang Chun should be used for exact upper and lower control limits, because different supply grades in the wider brominated epoxy series can shift the epoxide equivalent weight and the ionic bromide residue. The white powder is intended for formulating flame-retardant thermoplastics, epoxy laminates, and electrical encapsulation compounds where UL 94 V-0 classification is required at thicknesses of 1.6 mm or below. Because the product melts below typical compounding temperatures, it can be incorporated without a separate grinding step, but its feed-hopper behavior is sensitive to ambient humidity and to the temperature of the feed-zone cooling water.

    ParameterCCP B-24TXBrominated polystyreneDecabromodiphenyl ethane
    Reactive functional groupterminal epoxidenonenone
    Bromine content52–54 %66–68 %81–82 %
    Softening range75–85 °C150–180 °Cno melt below 300 °C
    Matrix interactionreactive with epoxy hardeners and polyamide chain endsdispersed phase, low interactiondispersed phase, low interaction
    Thermal decomposition onset>300 °C by thermogravimetric analysis330–360 °C by thermogravimetric analysis320–345 °C by thermogravimetric analysis
    Typical flammability evaluationUL 94 V-0 at 0.8–1.6 mmUL 94 V-0 at 0.8–1.6 mmUL 94 V-0 at 0.8–1.6 mm

    What Limits Dispersion Efficiency in High-Shear Compounding of B-24TX?

    In a production-scale co-rotating twin-screw extruder with an L/D ratio of 40:1, the limiting factor is not the melt temperature alone but the local viscosity gap between the low-molecular-weight brominated oligomer and the host polymer. When B-24TX is added to glass-reinforced polyamide 66, the oligomer melts in the first kneading zone, but if the barrel temperature in that zone falls below 90 °C for prolonged periods, the molten oligomer can resolidify on the screw root and deposit on the shaft. Plant trials have shown that barrel set points of 240–260 °C in the subsequent mixing zones are adequate to maintain a homogeneous melt, while screw speeds of 300–500 rpm are required to distribute the brominated phase. Melt flow index measured according to ISO 1133-1:2022 at 2.16 kg and 260 °C is a sensitive lot-to-lot screening tool; a reduction of more than 15 % in MFI relative to the control compound indicates epoxide chain extension rather than simple dilution. The processing window is narrow because excess residence time above 280 °C can dehydrobrominate the oligomer and generate free acid, which corrodes downstream die lips. In-line rheometers have recorded pressure variations of 0.5–1.0 MPa across lot changes when the epoxide equivalent weight drifts upward from 350 g/eq to 450 g/eq. Published data for this specific configuration is limited; the values above are representative production observations, not guaranteed performance limits.

    FR-4 laminate manufacture uses B-24TX in let-down blends rather than as a neat resin. The brominated oligomer is mixed with a non-brominated bisphenol A diglycidyl ether resin to adjust the bromine level in the cured composite to 18–22 % by mass. The varnish is catalyzed with dicyandiamide and an imidazole accelerator, and the reaction of the terminal epoxide rings with the amine hardener creates network nodes that participate in the same crosslinked architecture as the non-brominated epoxy. Glass transition temperatures after cure are evaluated using dynamic mechanical analysis according to IPC-TM-650 2.4.25 or differential scanning calorimetry under ISO 11357-2:2020. In comparison with a non-brominated system at equivalent crosslink density, the brominated resin raises the viscosity of the prepreg varnish by 20–40 % because the tetrabrominated bisphenol A unit increases chain rigidity; this is controlled by adjusting methyl ethyl ketone solvent content and prepreg resin solid content. Flammability performance is verified under UL 94 V-0 on laminate coupons at 1.6 mm and 0.8 mm; limiting oxygen index values are normally measured with ISO 4589-2.

    Thermal Degradation Thresholds in High-Tg Epoxy Systems

    Thermogravimetric analysis of a B-24TX-containing resin system shows two distinct weight-loss regimes. The first regime, between 300 °C and 350 °C, corresponds to cleavage of the carbon-bromine bond and release of hydrogen bromide; the second regime above 400 °C involves aromatic network decomposition. The 5 % mass loss temperature is therefore used as an incoming inspection criterion because brominated epoxy oligomers with higher ionic bromide contamination can reduce this onset by 15–25 °C. In copper-clad laminate pressing, this degradation threshold limits the lamination cycle to peak temperatures below 190 °C when the curing system is based on dicyandiamide; for high-Tg systems requiring 200–220 °C lamination, an alternative high-molecular-weight tetrabrominated resin with a higher aromatic content is usually selected. The difference between B-24TX and a brominated polystyrene flame retardant becomes measurable in this test: the polystyrene-based additive begins to decompose as a distinct non-epoxy phase and can lower the onset temperature by 20–40 °C in the same matrix. Thus the use of B-24TX in high-temperature thermoset processing is constrained not by the initial melt viscosity but by the early decomposition of the terminal epoxide-bromine structure. Thermal stability claims should be verified against the Chang Chun certificate of analysis using ISO 11358-1 at a heating rate of 10 °C/min under nitrogen.

    When Tetrabrominated Oligomer Reactivity Affects Extrusion Residence Time

    When B-24TX is compounded into polyamide or polyester at moisture levels above 0.15 %, the terminal epoxide rings can react with hydrolyzed chain ends under the high shear of a twin-screw extruder. The result is in situ chain extension that raises melt viscosity and die pressure within 60–120 s of residence time. On a production line this appears as an upward drift of 10–25 % in extruder torque after a feeder stop or a barrel-temperature excursion. Reversing the drift requires purging with a non-reactive commodity polyolefin and reducing barrel set points from 260 °C to 230 °C, because higher temperatures accelerate the epoxide-amine addition reaction. The practical difference from a non-reactive brominated diphenyl ethane is therefore not only flame retardancy but also the ability of B-24TX to modify molecular weight at trace levels of moisture. In injection molding trials, samples prepared at 230–240 °C with residence times under 2 min showed tensile strength values under ISO 527-2 similar to the base resin, while residence times above 4 min led to visible surface splay and a drop in elongation at break of more than 20 %. For molders using hot-runner systems, this reactivity imposes an operational boundary: avoid hot-runner holds longer than 5 min at melt temperatures above 250 °C unless the lot has been pre-tested for acid evolution.

    Process parameterMethod or equipmentThreshold observed in production
    Moisture content in feedISO 155120.15 % maximum
    Melt flow index variationISO 1133-1:2022±15 % versus control
    Barrel zone temperaturethermocouple melt probe230–260 °C
    Extruder torque driftdrive readout+10–25 % before purge
    Die pressure variationin-line melt transducer0.5–1.0 MPa across lots

    From a regulatory and handling standpoint, B-24TX is a tetrabromobisphenol A-based epoxy and is not classified as a decabromodiphenyl ether or a restricted polybrominated diphenyl ether under RoHS Directive 2011/65/EU. Industrial users are advised to confirm compliance with REACH Article 33 and any national occupational exposure limits for brominated compounds before using the product in food-contact or medical-grade polymer applications. Since the resin is hygroscopic, it requires pre-drying at 80–100 °C for 4–6 h when storage relative humidity exceeds 60 %. The dry powder should not be combined with amine-based accelerators at temperatures above 100 °C because the epoxide-amine reaction can initiate prematurely in the feed hopper or in a low-shear pre-blender. Dust extraction equipment is required where airborne brominated resin dust can settle on hot equipment and form acidic decomposition residues. When the product is evaluated as a substitute for brominated polystyrene in ABS or polyolefin flame-retardant compounds, the deciding variable is usually the resin's epoxide content rather than the bromine content alone; the reactive endgroups can improve the retention of mechanical properties after thermo-oxidative aging but they also narrow the processing temperature window.