| HS Code | 323232 |
| Productname | 4,4'-Difluorobenzophenone (DFBP) |
| Casnumber | 345-92-6 |
| Einecsnumber | 206-466-3 |
| Molecularformula | C13H8F2O |
| Molecularweight | 218.20 g/mol |
| Appearance | White to off-white crystalline powder or solid |
| Meltingpoint | 106-109 °C |
| Boilingpoint | 308.8 °C at 760 mmHg |
| Density | 1.276 g/cm3 |
| Flashpoint | 124.4 °C |
| Watersolubility | Insoluble in water |
| Organicsolubility | Soluble in common organic solvents |
| Purity | ≥99% typical product grade |
| Storageconditions | Store in a tightly closed container in a cool, dry place |
As an accredited 4,4'-Difluorobenzophenone DFBP factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
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4,4'-Difluorobenzophenone (DFBP, CAS 345-92-6) enters the highest-volume downstream application as the activated aryl fluoride monomer for polyetheretherketone synthesis, in which it is polycondensed with hydroquinone in diphenyl sulfone. In production-scale polymerizers the molar feed ratio of DFBP to hydroquinone is held between 0.998:1.000 and 1.002:1.000, and the DFBP is specified to a chromatographic purity of at least 99.5 %. The initial reactor slurry is heated to 150–180 °C to eliminate water released during the in situ formation of the potassium bisphenolate; any residual water hydrolyzes aryl fluoride end groups, caps the growing chain, and reduces the final melt viscosity that can be achieved. After dehydration the temperature is ramped to 320–340 °C under a nitrogen blanket, and the agitator torque is recorded as an indirect measure of molecular weight build. The step-growth stoichiometry creates a sharp process boundary: a drift of 0.5 mol% in the DFBP/hydroquinone ratio lowers the theoretical number-average degree of polymerization below 200 repeat units, so the monomer certificate of analysis and the balance calibration are checked before every charge.
Polymerization-grade DFBP is controlled for ionic residues because inorganic fluoride and potassium salts act as polar impurities during later melt processing. After the polycondensation, the diphenyl sulfone mass is cooled, milled, and extracted with acetone and deionized water to remove solvent and potassium fluoride. The isolated PEEK powder is dried to ≤0.1 % moisture and converted on a co-rotating twin-screw extruder with an L/D ratio of 40:1; barrel temperatures are set between 360 °C and 400 °C, and residence time is limited to avoid gel formation above 420 °C. Terminal products from this first-tier segment are unfilled pellets, 30 wt% glass-fiber compounds, and 30 wt% carbon-fiber compounds, which convert into injection-molded or extruded semi-finished stock. Food-contact resin is evaluated under 21 CFR 177.2415, while surgical implant resin is conditioned for testing under ASTM F2026. An operational boundary is that DFBP-derived PEEK should not be compounded with amine-based stabilizers, because the ketone carbonyl can undergo nucleophilic attack or condensation at melt temperature, shifting the melt flow index measured by ISO 1133-1:2022.
In laser-assisted tape placement of CF/PEEK prepreg, the DFBP-derived polyetheretherketone matrix is consolidated in a continuous out-of-autoclave process rather than an autoclave cure cycle. Unidirectional tape is supplied with a fiber volume fraction between 60 vol% and 65 vol%, and the placement head applies a nip pressure from 0.5 MPa to 1.0 MPa while the surface temperature reaches 380–400 °C. The polymer matrix must re-melt without degrading, which requires the DFBP monomer residual and chain-branching level to remain low enough to hold the zero-shear viscosity stable during the short molten path. Terminal components include fuselage clips, cable raceway brackets, and rib cleats, where titanium or aluminum machined parts are replaced by consolidated CF/PEEK laminates.
The critical process conflict in this application is crystallinity control: cooling too slowly produces a through-thickness spherulitic morphology that reduces compression-after-impact strength, while cooling too rapidly depresses interlaminar toughness because the matrix cannot reach the required degree of crystallinity. Laminators therefore control the cooling rate between 10 °C/min and 50 °C/min after the nip point, and verify the laminate by ultrasonic C-scan and compression testing to ASTM D3039. Flammability acceptance for aircraft interiors is tested under FAR 25.853, although published data for DFBP-specific lot-to-lot laminate performance is limited. Pre-drying of prepreg at 150 °C for 4–6 h is mandatory above 60 % relative humidity to prevent steam porosity at the tape surface.
A different processing discipline governs DFBP-derived PEEK in surgical implant stock shapes, because the polymer is not only injection-molded but subsequently annealed, machined, and cleaned under conditions that preserve chemical inertness. Implant resins are specified to ASTM F2026 and must pass cytotoxicity evaluation to ISO 10993-5:2009, irritation and sensitivity testing to ISO 10993-10:2010, and systemic toxicity endpoints relevant to the device classification. Unfilled and 30 wt% chopped carbon-fiber-reinforced grades are extruded into rods and plates; the semi-finished stock is annealed at 200–220 °C for 4–6 h to relieve molded-in stress before CNC machining into spinal cages, trauma fixation anchors, and cranial plates. The carbon-fiber-reinforced grade raises the flexural modulus by a factor of approximately 1.5–2 compared with unfilled PEEK under ISO 178:2019, which is relevant for load-bearing spinal devices.
Extractables testing is the key DFBP-monomer-related acceptance gate. Residual DFBP, diphenyl sulfone, and potassium fluoride are determined by liquid chromatography–mass spectrometry on implant resin samples; converters typically require residual DFBP below 100 ppm in the finished material. The injection molding process uses a melt temperature of 370–400 °C, a mold temperature of 180–200 °C, and a cushion position that keeps the gate from freezing before packing pressure is applied. The limiting operational boundary is that implant-grade PEEK cannot be reprocessed from reclaimed runner material without additional biocompatibility validation, and the addition of radiopaque fillers must not exceed levels that move tensile strength below the lower bound of the implant manufacturer’s design dossier.
| End-use sector | DFBP-derived material form | Controlling standard | Monomer-linked process variable |
|---|---|---|---|
| Surgical implant stock shapes | Unfilled PEEK or 30 wt% carbon-fiber-reinforced PEEK | ASTM F2026, ISO 10993-5:2009 | Residual DFBP below 100 ppm; annealing at 200–220 °C before machining |
| Carbon-fiber/thermoplastic aerospace parts | CF/PEEK unidirectional tape with 60–65 vol% fiber | ASTM D3039, FAR 25.853 | Consolidation at 380–400 °C; cooling rate between 10 °C/min and 50 °C/min |
| Semiconductor wafer handling | Machined PEEK retaining rings and combs | SEMI F57, SEMI S2 | Ionic extractables below 10 ppm; through-thickness crystallinity variation below 5 % |
| Oil and gas downhole equipment | 30 wt% glass-fiber-reinforced PEEK | ISO 23936-1 | Melt processing at 360–400 °C; water absorption below 0.5 % before dimensional acceptance |
When CMP retaining rings are machined from DFBP-derived PEEK stock shapes, the residual fluoride and potassium distribution from the monomer synthesis becomes the primary quality variable because ionic contamination at the wafer surface alters local oxide removal rate. The material is specified to SEMI F57, and ionic extractables are kept below 10 ppm after extraction in ultrapure water at 80 °C for 24 h. Fluoroelastomer seals in wafer-handling modules can also be attacked by hydrofluoric acid generated from fluoride salts in the polymer surface under humid cleanroom conditions, so the PEEK stock shape supplier anneals the extrudate at 200–220 °C and then stabilizes the machined parts at 150 °C for 8 h to drive off surface moisture and volatile residues.
Dimensional tolerance on ring groove diameters is typically ±10 µm, which means that through-thickness crystallinity variation must remain below 5 % as measured by differential scanning calorimetry. The extrusion process of thick plate is run with a barrel temperature of 360–400 °C and a cooling rate of 10–30 °C/min to balance crystallinity and residual stress. In semiconductor front-end equipment, compliance is also evaluated under SEMI S2 for equipment safety, and the PEEK must not emit outgassed condensables above the user’s specified threshold when tested at 100 °C for 24 h. The operational boundary is that DFBP-derived PEEK stock shapes should not be exposed to hot concentrated sulfuric acid or strong oxidizing acid mixtures, because the aromatic ether linkages and ketone groups can be oxidized, causing dimensional drift and surface roughening.
For downhole seal stacks and electrical connector insulation, DFBP-derived PEEK is compounded with 30 wt% glass fiber to increase compressive creep resistance and reduce thermal expansion. The compound is injection-molded with a melt temperature of 360–400 °C and a mold temperature of 180–200 °C; hot-runner systems are maintained with a residence time below 10 min because prolonged hold at melt temperature increases the probability of polymer chain branching and shifts the crystallization temperature upward. Seal backup rings, ball valve seats, and electric submersible pump connector bodies are machined from molded blanks after annealing at 220 °C for 4 h to stabilize dimensions. The material for sour-service environments is assessed under ISO 23936-1 and the end-user’s fluid compatibility protocol; water absorption is held below 0.5 % by mass before dimensional acceptance.
The failure mode that must be excluded in DFBP-derived PEEK downhole parts is not tensile yield but creep under sustained compressive load at temperatures above 150 °C; glass-fiber reinforcement reduces creep strain but does not eliminate it. Published data for specific seal stack geometries in high-pressure sour gas is limited, so validation is performed at the sub-assembly level with representative seals and backup rings. The processing boundary is that the polymer cannot be used in the presence of hot concentrated sulfuric acid or fluorine-containing gas streams that can degrade the aromatic ether backbone; in those environments, metal-to-metal seals or perfluoroelastomers are substituted. Terminal products include subsea electrical connector insulators, compressor valve plates, and seal backup rings for API wellhead equipment.
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