Phenol For Phenolic Resins

    • Product Name: Phenol For Phenolic Resins
    • Factroy Site: No. 59 Shihua 3rd Road, Xuwei New Area, Lianyungang City
    • Price Inquiry: sales9@boxa-chem.com
    • Manufacturer: Shenghong Refining & Chemical (Lianyungang) Co., Ltd
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    Specifications
    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 & Storage
    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.
    Application of Phenol For Phenolic Resins

    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.

    At What Phenolic Resin Loading Does Coated Abrasive Grain Anchoring Fail in High-Pressure Grinding?

    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.

    Brake Pad Formulations and the Thermal Decomposition Threshold of Phenolic Binders

    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.

    Reducing Post-Mold Shrinkage in Copper-Clad Laminates via Controlled Resole Advancement

    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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    Certification & Compliance
    More Introduction

    Solidification Point and Isomer Purity Correlation

    The freezing range of phenol serves as a rapid lot-acceptance proxy for total organic purity, because 2-methylbenzofuran, acetol, and mesityl oxide act as eutectic poisons that depress the solidification onset. A difference of 0.1 °C from the nominal 40.85 °C can represent as much as 0.15 wt% of non-phenolic organic contaminants, a relationship codified in ASTM D1493-08. Plant laboratories running a Mettler-Toledo MP70 or equivalent automated melting-range analyzer report the plateau temperature rather than a single-point reading, as undercooling artifacts in static-bath methods inflate the apparent purity by 0.03–0.05 °C. For novolac producers, this metric critically impacts the stoichiometric ratio with formaldehyde: a phenol stream of 99.8% purity versus 99.95% shifts the required molar excess of phenol by roughly 1.2%, altering the free-phenol content of the finished flake and moving the melt viscosity at 150 °C outside the target band of 3–8 Pa·s for transfer molding applications.

    How Does Feedstock Impurity Shift Novolac Crosslink Density?

    The presence of 2-methylbenzofuran above 25 ppm in the phenol monomer acts as a chain-transfer agent during acid-catalyzed novolac polycondensation, terminating ortho-para methylene bridge growth and generating oligomers with a lower number-average molecular weight, typically Mn 400–600 g·mol⁻¹ versus the desired 800–1200 g·mol⁻¹. On a production-scale Büchi 50 L glass-lined reactor operated at 95–100 °C with oxalic acid dihydrate (1.5 phr), an MBF excursion to 50 ppm reduces the B-time (stroke-cure reactivity) of the resulting novolac from 55–65 s to 35–40 s when blended with 10 wt% hexamethylenetetramine (HEXA) and tested on a 150 °C cure plate per ISO 8987:2005. Consequently, injection-molding compounds formulated with such resin require a 15–20% increase in HEXA to restore crosslink density, raising the water-absorption of molded specimens by 1.2–1.8% after 48 h immersion at 23 °C (ISO 62:2008) and embrittling the article after thermal aging at 180 °C for 500 h. Users deal directly with a 0.1 ppm iron threshold as well. In resole synthesis catalysed by sodium hydroxide, iron ions oxidise the methylol phenols to quinonoid chromophores that impart a Gardner color exceeding 12 (1-inch cell, ASTM D1544-04) within the liquid resin, rendering it unsuitable for decorative laminates where a Gardner value ≤ 2 is mandatory. Published data from continuous lamination lines operating at 8–12 m·min⁻¹ on Kraft paper show that an iron content of 0.5 ppm in the resin bath elevates the yellowness index (YI E313) of the finished CPL by 4–6 units compared with an iron-free control, an effect not recoverable through optical brighteners.

    When Cumene-Derived Phenol Replaces Coal-Tar Phenol in Resole Synthesis

    Reformulation of a standard impregnating resole from coal-tar distillate phenol to fully synthetic cumene phenol requires compensating for the absence of naturally occurring ortho-cresol and 2,4-xylenol co-distillates, which in coal-tar grades contribute 2–5% of the reactive ring-substituted species and alter the methylolation rate. In a 5 m³ stainless-steel reactor charged at a formaldehyde-to-phenol molar ratio of 1.2:1, the substitution shifts the gel time measured at 130 °C from 8–12 min to 14–18 min (ISO 9396:1997), a drift that laminators compensate by raising the catalyst (triethylamine) loading from 0.8 phr to 1.1 phr. This adjustment, however, increases the free-formaldehyde emission from the impregnated web during drying by approximately 35%, a value documented on a Babcock web-offset line with a 20 m floating arch dryer set at 140 °C. Plant trials consistently record that switching to synthetic phenol tightens the viable B-stage pre-preg storage window from 48–72 h at 5 °C to 36–48 h, because the narrower molecular-weight distribution yields a steeper viscosity-advance curve.
    Representative specification profile for phenol intended for phenolic resin synthesis
    ParameterMethodTypical LimitUnit
    Purity (GC)ISO 8974:2022≥ 99.90% area
    Solidification pointASTM D1493-0840.75–40.90°C
    WaterASTM D1631-17 (Karl Fischer)≤ 0.05wt%
    Color, moltenASTM D1209-05 (Pt-Co, APHA)≤ 10Hazen
    Iron (Fe)ASTM D1068-15 (GF-AAS)≤ 0.2ppm
    2-MethylbenzofuranInternal GC-MS, SIM mode≤ 15ppm
    Non-volatile residueASTM D1353-13≤ 0.005wt%
    Sulfate ashISO 3451-1:2019≤ 0.003wt%
    Processing phenol stored in bulk requires a tempered tank system maintained at 42–45 °C with mild steel or electropolished 316L wetted surfaces; carbon steel is avoided because phenol at molten temperatures slowly leaches iron, producing a pink-to-amber discoloration that is quantified by an increase of 2–5 APHA units per week of hold-up. Pre-drying with molecular sieves or azeotropic distillation is mandatory only when the incoming water exceeds 0.08 wt%, a scenario encountered when tank-heel humidity condenses during marine shipment or railcar unloading under tropical ambient conditions. Above this moisture threshold, the initial formaldehyde condensation suffers a 2–4% loss of exothermic peak (ΔTmax), observable on a Mettler RC1e reaction calorimeter, because water solvates the acid catalyst proton and slows electrophilic substitution on the aromatic ring.
    Differences among synthetic phenol streams are not limited to end-use specification sheets. The distinction between “resole-grade” and “bisphenol-A-grade” phenol manifests in the acetone-insoluble matter specification—≤ 10 ppm for BPA feed versus ≤ 25 ppm for resin feed—but, more importantly, in the proprietary stabiliser packages added post-distillation. Resin-grade phenol is typically dosed with 50–150 ppm of a hindered phenolic antioxidant (e.g., BHT or a Ciba®-type Irganox blend) to suppress oxidative yellowing during rail transit that would otherwise elevate the shipment APHA color by 8–15 units over a 14-day journey. BPA producers often cannot tolerate these stabilisers because they poison the ion-exchange resin catalysts employed in fixed-bed acetone adduction; thus, their phenol is shipped under a minimum 0.5 bar nitrogen pad and within a 72-hour delivery window.

    Acid Catalyst Selection and Phenol Purity Interplay in Novolac Cooks

    Oxalic acid catalysis—predominant in shell-molding foundry resins—exhibits the greatest sensitivity to phenol sulfur content. Phenol sourced from refineries processing high-sulfur crudes can carry over 2–10 ppm of thiophene or benzothiophene, which protonate under the oxalic acid regime (pH ~1.5) and generate sulfonic acid in situ, autocatalysing the methylene bridge formation and narrowing the cook processing window to ± 2 °C around the target exotherm peak of 115 °C. Data logs from a production-scale 10,000 L reactor at a European foundry resin plant show a batch rejection rate of 12% when the phenol sulfur assay exceeded 3 ppm (ASTM D5453-19a), owing to a “runaway” viscosity spike above 25 Pa·s at catalyst neutralisation. In contrast, p-toluenesulfonic acid (PTSA) catalysis is far more forgiving, tolerating phenol sulfur up to 15 ppm with negligible batch-to-batch variance because the external strong acid overwhelms the trace proto-acids. The trade-off appears in the finished flake shelf life: PTSA-catalysed novolacs retain 0.2–0.5% bonded sulfur that, over 6 months at 30 °C warehouse storage, autocatalyses HEXA decomposition and drops the cup flow of the molding compound from 18–22 mm to 10–13 mm (ISO 8975:2000), effectively halving the usable inventory window. For resole resins, the alkali metal ion balance is the critical purity variable. Sodium hydroxide is the workhorse catalyst, but phenol introduced with a calcium ion load above 0.1 ppm—common from cooling-water leaks in the cumene-plant fractionation tower—forms insoluble calcium phenolate salts that nucleate haze in the final liquid resin. Filtration through 1-micron bag filters on the reactor discharge line reduces the sediment from 30 mg·kg⁻¹ to ≤ 5 mg·kg⁻¹ (ISO 15711:2019), a step omitted in less-demanding wood-adhesive resoles where opacity is irrelevant but that becomes a batch-release specification for high-pressure laminate (HPL) impregnating resins.
    Comparison of phenol streams: resin-grade vs. BPA-grade vs. technical phenol
    PropertyResin GradeBPA GradeTechnical (broad-spec) Phenol
    Purity, GC (ISO 8974)≥ 99.90%≥ 99.95%99.0–99.8%
    Solidification pt. (ASTM D1493)40.8 °C40.9 °C40.3–40.6 °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 ppmNot specified
    Typical stabiliser addition80–150 ppm BHTNone (nitrogen blanket)None or up to 200 ppm
    End-use suitabilityNovolac, resole, laminatesPolycarbonate, epoxy resinsLow-color resoles, disinfectant phenolics
    Phenol shipped in isotainers under a nitrogen pad maintains oxidation resistance for up to 30 days; exposure to ambient air during drum decanting shortens the induction period to roughly 8 hours before detectable peroxides (≥ 5 meq·kg⁻¹) appear. In practice, resin plants decanting phenol from 200 L drums into day tanks should maintain a local nitrogen purge of 2–3 L·min⁻¹ through the tank headspace and ensure the transfer temperature never exceeds 60 °C. Contact with copper or copper alloys is prohibited: copper ions catalyse phenol oxidative coupling to diphenoquinone, turning the melt deep red and rendering it useless for any resin application where color is a quality parameter. The thermal stability window of resin-grade phenol defines its safe handling envelope. At 180 °C, neat phenol in the absence of oxygen remains stable for 48 h with < 0.1% decomposition, but introduction of 1% dissolved oxygen raises the decomposition rate to 0.5%·h⁻¹, generating 4,4′-bisphenol F and polymeric tars that increase the melt viscosity and lower the ultimate tensile strength of cured novolac specimens from 45–50 MPa to 30–35 MPa (ASTM D638-14, Type I specimen, 5 mm·min⁻¹ crosshead speed). Production facilities mitigate this by sparging the bulk storage with nitrogen achieving ≤ 0.5 vol% O₂ in the headspace, verified by a Servomex or Yokogawa paramagnetic analyser. When phenol is to be diverted from standard novolac production into a high-ortho novolac cook—using a zinc acetate or magnesium oxide catalyst to achieve an ortho/para methylene bridge ratio exceeding 2.5:1—the presence of even trace ethylene glycol (a byproduct of certain cumene oxidation scrubbing processes) must be below 10 ppm. The glycol competitively chelates the metal catalyst, lowering its effective concentration and pushing the ortho/para ratio back toward the 1.0:1 typical of acid-catalysed novolacs, which compromises the fast cure kinetics (5–8 s spiral flow advantage) required for under-hood automotive components. This nuance, often overlooked in generic phenol supply agreements, becomes the root cause of 15–20% fluctuations in spiral-flow length on a 200-ton injection molding press manufacturing brake-piston phenolic composites. Published data for the specific quantitative threshold of ethylene glycol interference at zinc loading 0.5 phr is limited, yet several production sites report that a glycol washout period of 3–4 tank turnovers is necessary before the ortho-directing effect stabilises.