| HS Code | 191119 |
| Product Name | Phenol For Phenolic Resins |
| Chemical Formula | C6H5OH |
| Cas Number | 108-95-2 |
| Molecular Weight | 94.11 g/mol |
| Appearance | Colorless to pale pink crystalline solid or liquid when molten |
| Odor | Sweet, tarry, acrid |
| Melting Point | 40.5 °C (104.9 °F) |
| Boiling Point | 181.7 °C (359.1 °F) |
| Flash Point | 79 °C (closed cup) |
| Autoignition Temperature | 715 °C |
| Specific Gravity | 1.07 at 25 °C (water = 1) |
| Solubility In Water | Approximately 8.3 g/100 mL at 20 °C; miscible with water above 66 °C |
| Purity | ≥ 99.0% typical |
| Water Content | ≤ 0.5% typical |
As an accredited Phenol For Phenolic Resins factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Phenol for phenolic resins, supplied in 200 kg steel drums, sealed for safe handling and storage. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Phenol for phenolic resins ensures safe, dry stowage, preventing leakage, contamination, and moisture damage during transit. |
| Shipping | Phenol for phenolic resins is transported as hazardous material (UN1671, Class 6.1, toxic). It is shipped in sealed drums, bulk containers, or heated tankers, depending on form. Packaging must prevent leakage and moisture contact. Handling requires proper labeling, ventilation, and compliance with transport regulations to ensure safe delivery. |
| Storage | Store phenol for phenolic resins in a cool, dry, well-ventilated area away from direct sunlight and ignition sources. Use tightly sealed, corrosion-resistant containers made of compatible materials, avoiding copper, zinc, and aluminum. Maintain temperatures above its freezing point to prevent solidification. Isolate from oxidizing agents, acids, and foodstuffs, with secondary containment and proper labeling. |
| Shelf Life | Store in a cool, dry, well-ventilated area away from oxidizers. Shelf life typically 12-24 months under recommended conditions. |
In a novolac-based molding compound, the condensation of phenol with formaldehyde under acidic catalysis proceeds at a phenol-to-formaldehyde molar ratio of 1:0.80 ± 0.05, yielding a solid brittle resin with a softening point between 85 and 105 °C. The subsequent grinding and blending with 8–12 wt% hexamethylenetetramine (hexa) crosslinker, wood flour, mineral fillers, and lubricants produces a thermosetting molding powder whose activation energy for cure is deliberately balanced to prevent premature crosslinking during plastication. On the shop floor, the compound is processed on reciprocating-screw injection molding machines with electrically heated barrels maintained in a tight window of 65–95 °C and a nozzle temperature below 100 °C; mould temperatures are held at 165–185 °C with a clamp force typically exceeding 150 tonnes for multi-cavity tools. The curing cycle, lasting 20–45 s per millimetre of wall thickness, exploits the exothermic polycondensation that progressively fixes the network geometry. Compliance is assessed against ASTM D5948-21 for characterisation of moulding compounds and UL 94 V-0 flame classification at 1.5 mm section thickness, while electrical tracking resistance is verified by IEC 60112 comparative tracking index measurement. Terminal parts range from ignition distributor caps and relay bases to moulded-case circuit-breaker housings and appliance control knobs, all of which rely on the intrinsic creep resistance and dielectric rigidity imparted by the densely crosslinked phenolic framework.
Resole-stage liquid phenolic resins formulated with a phenol-to-formaldehyde molar ratio of 1:1.2–1.6 serve as the primary bond system for coated and bonded abrasives, where the wetting characteristic and cured strength of the resin film directly govern grain retention under mechanical load. In the manufacture of resin-bonded grinding wheels and abrasive belts, the liquid resole is blended with fillers, wetting agents, and abrasive grains such as aluminium oxide or silicon carbide; the resin loading typically falls between 5 and 15 wt% of the total granulate mass, a range dictated by the need to minimise porosity while avoiding brittle fracture of the bond bridges. The coated backing — paper, polyester, or cotton drill — receives a maker coat and a size coat applied via precision roll coating or curtain coating, with intermediate and final curing stages conducted in festoon dryers or continuous ovens operating at 90–130 °C for the pre-gel phase and up to 155 °C for full crosslinking. Cured adhesion is validated under ISO 2976:2020 methods for abrasive belts, and grain retention is often correlated with the Barcol hardness of the resole film. Finished products include resin-bonded grinding wheels, flap discs, and endless abrasive cloth rolls deployed in high-stock-removal operations, where thermal degradation of the phenolic matrix at the grit interface remains the principal failure mode.
In the production of structural laminated veneer lumber (LVL) and exterior-grade plywood, the adhesive system relies on an alkaline-catalysed resole resin where phenol and formaldehyde are reacted at a molar ratio of 1:1.8–2.3 to achieve a low-molecular-weight prepolymer with a solids content of 45–50% and a water tolerance exceeding 300%. The resin is applied at 4–8 wt% solids on dry veneer basis via curtain coater or foam extrusion, and the assembled lay-up is consolidated in a multi-opening hot press at a platen temperature of 130–150 °C while sustaining a specific pressure of 1.2–2.0 MPa for 4–8 min per panel thickness category. Temperature sensors embedded between press platens confirm that the innermost glue line must reach at least 115 °C to trigger the irreversible condensation that creates a dark reddish-brown bond line. Weathering resistance is certified according to EN 314-2 Class 3 (exterior bonded) through boil-dry-boil cyclic delamination tests, and emission profiles are validated against EN 717-2 for formaldehyde release. Typical end-products include concrete formwork panels, truck trailer flooring, and marine plywood keels, where the phenolic bond maintains integrity despite prolonged hydrothermal stress.
Dry-mix friction material preparation begins with the blending of a powdery novolac phenolic resin — synthesised at a phenol-to-formaldehyde molar ratio of 1:0.82 and subsequently cured in situ with 10–12 wt% hexa — with reinforcing fibres, ceramic fillers, and friction modifiers, yielding a granulate in which the resin constitutes 15–25 wt% of the total formulation. The green mixture is cold-pressed into preforms, transferred to a hot-press cavity, and compression-moulded at 155–180 °C under 30–50 MPa specific pressure; the dwell time of 5–12 min is calibrated to achieve a crosslink density that shifts the onset of thermal decomposition beyond 400 °C in thermogravimetric analysis (TGA) under nitrogen. Post-cure is conducted in convection ovens programmed with a graduated ramp to 200 °C to eliminate residual volatiles and stabilise the friction coefficient. Performance conformity is demonstrated against SAE J661 brake lining friction test procedure and regulated under ECE R90 for replacement brake linings; the formulation typically must deliver a hot friction coefficient above 0.35 at 300 °C drum temperature without excessive rotor scoring. The final components are disc brake pads for passenger cars and drum brake linings for commercial vehicles, where the phenolic matrix functions as the sacrificial thermal management layer under repeated high-energy stops.
When carbon-magnesite bricks for basic oxygen furnaces require medium-temperature carbonisation resistance, a liquid phenolic resin derived from phenol — commonly a resole with a phenol-to-formaldehyde molar ratio of 1:1.2 — is introduced as the binder and in-situ carbon source at 2–4 wt% of the refractory batch. The resin is added to the magnesia and graphite aggregate during high-intensity mixing, and the moist mix is shaped under 100–150 MPa in a hydraulic press before undergoing curing in a temperature-controlled tunnel dryer where the brick core must plateau at 180–220 °C for at least 4 h. The controlled pyrolysis of the phenolic binder during the initial heat-up of the ladle generates a secondary carbon bond that improves hot modulus of rupture, a property evaluated per ISO 20292:2018 and validated by thermal shock cycling between 1,200 °C and ambient water quench. Widespread end-products are magnesia-carbon bricks installed in slag lines, impact pads, and purging plugs of steel ladles, where published data for exact carbon nanostructure development remains limited but industrial practice confirms a service-life improvement of 15–30% over pitch-bonded equivalents.
Impregnation of electrical-grade kraft paper for copper-clad laminates employs a low-viscosity resole resin synthesised at a phenol-to-formaldehyde molar ratio of 1:1.03–1.20, with the condensed vacuum-stripped resin adjusted to a specific gravity of 1.15–1.20 and a gel time of 90–150 s at 150 °C on a hot plate. The paper web is saturated in a vertical or horizontal treater, passing through metering rolls that control resin pickup to 45–55% by dry weight, and then drawn through a staged drying zone with air temperatures descending from 160 °C in the first chamber to 120 °C near the exit, where the B-staging advancement must arrest at a volatile content of 4–6% to prevent blistering during final lamination. The dried prepreg sheets are cut, layered, and pressed between mirror-finished steel plates in a multi-daylight laminating press under 8–12 MPa at 150–170 °C for 60–90 min; the cure curve is engineered to pass the resin’s B-stage trough while minimising post-mould shrinkage that could warp single-sided copper-clad boards. The finished laminate is assessed against IPC-4101C specification 42 (phenolic paper, flame retardant), satisfying UL 94 V-0 and a maximum dielectric constant of 5.0 at 1 MHz as per IEC 61249-2-4. Typical end-products are single-sided printed circuit boards for consumer power supplies, LED lighting substrates, and transformer insulation plates, where the laminate thickness ranges from 0.8 to 3.2 mm and the copper foil peel strength must exceed 1.2 N/mm after solder float at 260 °C.
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| Parameter | Method | Typical Limit | Unit |
|---|---|---|---|
| Purity (GC) | ISO 8974:2022 | ≥ 99.90 | % area |
| Solidification point | ASTM D1493-08 | 40.75–40.90 | °C |
| Water | ASTM D1631-17 (Karl Fischer) | ≤ 0.05 | wt% |
| Color, molten | ASTM D1209-05 (Pt-Co, APHA) | ≤ 10 | Hazen |
| Iron (Fe) | ASTM D1068-15 (GF-AAS) | ≤ 0.2 | ppm |
| 2-Methylbenzofuran | Internal GC-MS, SIM mode | ≤ 15 | ppm |
| Non-volatile residue | ASTM D1353-13 | ≤ 0.005 | wt% |
| Sulfate ash | ISO 3451-1:2019 | ≤ 0.003 | wt% |
| Property | Resin Grade | BPA Grade | Technical (broad-spec) Phenol |
|---|---|---|---|
| Purity, GC (ISO 8974) | ≥ 99.90% | ≥ 99.95% | 99.0–99.8% |
| Solidification pt. (ASTM D1493) | 40.8 °C | 40.9 °C | 40.3–40.6 °C |
| 2-Methylbenzofuran | ≤ 20 ppm | ≤ 5 ppm | ≤ 50 ppm |
| Iron (Fe) content | ≤ 0.2 ppm | ≤ 0.05 ppm | ≤ 1.0 ppm |
| APHA color, molten | ≤ 10 | ≤ 5 | ≤ 30 |
| Acetone insolubles | ≤ 25 ppm | ≤ 10 ppm | Not specified |
| Typical stabiliser addition | 80–150 ppm BHT | None (nitrogen blanket) | None or up to 200 ppm |
| End-use suitability | Novolac, resole, laminates | Polycarbonate, epoxy resins | Low-color resoles, disinfectant phenolics |