Cyclohexanone 99 5 Technical Grade Specification Coa
Cyclohexanone 99.5% technical grade is released as a solvent and chemical intermediate against a certificate of analysis that converts specification entries into batch-specific numerical results. The commercial specification gives assay at ≥99.5%, water at ≤0.05%, acidity as acetic acid at ≤0.01%, and color at ≤10 APHA. These values are not nominal claims; they are used to calculate feed stoichiometry in caprolactam oximation, to set dry-nitrogen handling requirements in urethane coating lines, and to determine whether a bulk storage tank has crossed an oxidative threshold. A COA generated under ISO 17025:2017 clause 7.8 includes the test result, the test method, uncertainty where applicable, and a conformity statement. In addition, the document carries the batch or lot number, production date, retest date, and the tank or drum identity that downstream users need for traceability under ISO 9001:2015 clause 7.5.3. The value of the COA is therefore not limited to purity; it provides the basis for mass-balance correction in plants that receive varied bulk logistics conditions.
What Does a 99.5% Technical Grade Certificate of Analysis Actually Control?
A technical-grade COA for cyclohexanone 99.5% controls the volatile impurity envelope, not merely total nonvolatile residue. Gas chromatographic purity is usually executed on a 30 m × 0.32 mm × 0.25 µm polyethylene glycol capillary column with flame ionization detection and split injection. The oven program ramps from 60 °C to 240 °C at 5 °C/min to separate cyclohexanol, cyclohexanone, cyclohexene, and cyclohexane. The area-percent result is accepted only when baseline resolution is achieved; co-elution of cyclohexanol with the ketone peak inflates the assay and obscures the reactive hydroxyl content. Release limits are shown in Table 1.
| Test parameter | Unit | Commercial limit | Test method |
|---|---|---|---|
| Purity | area % | ≥99.5 | GC-FID; internal method aligned to ISO 17025:2017 |
| Water | wt % | ≤0.05 | ASTM E203-24 Karl Fischer |
| Acidity as acetic acid | wt % | ≤0.01 | ASTM D1613-17 |
| Color | Pt-Co | ≤10 | ASTM D1209-05(2019) |
| Distillation range | °C | 153.0–157.0 | ASTM D1078-11 |
| Density at 20 °C | g/cm³ | 0.9460–0.9500 | ASTM D4052-22 |
| Refractive index nD20 | — | 1.4500–1.4510 | ASTM D1218-21 |
| Nonvolatile residue | wt % | ≤0.005 | ASTM D1353-13 |
| Cyclohexanol | wt % | ≤0.20 | GC-FID |
The GC assay by area percent has a known limitation: it does not quantify water or nonvolatile material, so separate Karl Fischer and evaporation methods must appear on the COA. In a bulk tank audit, an assay of 99.68% with water at 0.040% and nonvolatile residue at 0.003% corresponds to a true active content slightly below 99.6%. For precision batching, the formulator subtracts water, nonvolatile matter, and major identified hydroxyl impurities from the GC area figure rather than using the nominal assay directly. The specification in Table 1 is typical of commercial technical grade; individual supplier limits may be tighter for pharmaceutical or electronic applications.
Specification values are measured on the as-received sample, not on a predried or redistilled fraction. This distinction matters because technical-grade cyclohexanone is shipped in industrial containers, and the COA must reflect the material as it enters the user’s mass balance. If a received sample is predried in the laboratory before GC analysis, a water-laden bulk lot can be certified as conforming while still causing severe isocyanate side reactions. Therefore, the sampling procedure described in the COA should state whether the drum was homogenized, whether the sample was drawn from the bottom valve or top hatch, and whether the container was under nitrogen. The test method used for assay should be an area-normalization GC method with a defined integration threshold, typically rejecting peaks below 0.01% unless they are identified as cyclohexanol, cyclohexene, or cyclohexane.
Cyclohexanone technical grade can contain trace amounts of mesityl oxide, 2-cyclohexylidenecyclohexanone, and other aldol condensation products under prolonged basic or acidic conditions. These higher-boiling impurities are not always resolved by a simple GC program. If the distillation range widens and nonvolatile residue increases while the main assay remains above 99.5%, the COA should include a note on oligomeric material. In epoxy formulations, these condensation products can act as chain-transfer or reactive diluent impurities and change the equivalent weight of the resin system.
Density at 20 °C is specified between 0.9460 g/cm³ and 0.9500 g/cm³ under ASTM D4052-22 digital density metering. The narrow density window is a quality marker for cyclohexanone-rich streams; even small carryover of cyclohexane or water shifts the measured value outside the expected control range. Refractive index is set at 1.4500–1.4510 at 20 °C under ASTM D1218-21. A batch with refractive index above 1.4520 may contain autoxidation byproducts or oligomeric condensation products.
Distillation range testing under ASTM D1078-11 uses a 100 mL distillation flask at 101.3 kPa. The initial boiling point is controlled at ≥153.0 °C and the dry point at ≤157.0 °C. A spread greater than 1.5 °C between 5% and 95% recovery is a production-scale indicator of cyclohexanol carryover or residual water flashing. In continuous caprolactam feedstock lines, a widening distillation range above 2.0 °C triggers a density-corrected feed adjustment because the molar cyclohexanone content no longer aligns with the pump calibration.
| COA parameter | Batch result | Test method |
|---|---|---|
| Purity | 99.73% | GC-FID area normalization |
| Water | 0.021% | ASTM E203-24 |
| Acidity as acetic acid | 0.004% | ASTM D1613-17 |
| Color | 7 Pt-Co | ASTM D1209-05(2019) |
| Density at 20 °C | 0.9482 g/cm³ | ASTM D4052-22 |
| Distillation range | 154.1–156.3 °C | ASTM D1078-11 |
| Cyclohexanol | 0.11% | GC-FID |
| Nonvolatile residue | 0.002% | ASTM D1353-13 |
Water, Acidity, and Cyclohexanol Release Boundaries Are Interdependent
Water is limited to ≤0.05 wt % because cyclohexanone is hygroscopic enough to absorb atmospheric moisture during open drum transfer. In two-component isocyanate systems, residual water consumes the hardener through urea formation and carbon dioxide release. At 0.05 wt % moisture, a 1000 kg batch carries 0.5 kg of water, or 27.8 mol; each mole of water can consume two moles of NCO groups. This corresponds to about 2.33 kg of free NCO groups, or roughly 10 kg of an HDI trimer hardener with 23% NCO content. If the coating line is batched at a fixed NCO index without correcting for solvent water, this side reaction reduces the effective crosslink density and produces surface bubbles.
Acidity is limited to ≤0.01 wt % as acetic acid under ASTM D1613-17. Acidic species accelerate aldol condensation during storage and can corrode carbon steel transfer lines above 40 °C. In caprolactam oximation, free acidity shifts the pH set point of the hydroxylamine sulfate reaction; a pH drift of 0.2 units outside the 4.5–5.0 control band changes oxime yield and increases tar formation. Cyclohexanol is allowed up to 0.20% because it is a co-product in cyclohexane oxidation and is not fully removed in technical distillation. In adipic acid production, cyclohexanol is not inert; it participates in nitric acid oxidation and raises the nitrogen oxide emission load per ton of dibasic acid. A batch with 0.18% cyclohexanol requires a demonstrable correction in the nitric acid feed ratio in a 50,000 t/year continuous plant.
In caprolactam production, cyclohexanone 99.5% is fed to a continuous oximation reactor with hydroxylamine sulfate at 60–80 °C and pH 4.5–5.0. The ketone assay becomes a direct input to the molar feed ratio. If the assay database treats 99.5% as 100% active while water and cyclohexanol consume 0.25% of the stream, the oxime formation step drifts below target stoichiometry at high throughput. The drift is observed as a slow rise in unreacted ketone in the circulating organic phase and an increase in sulfate-laden aqueous purge. Plant control systems bias the mass flow meter by the certified water and cyclohexanol contents from the COA, using a density correction from ASTM D4052-22 rather than a fixed 0.948 g/cm³ density.
When Polyurethane Coating Lines Demand Water Below 0.05%
Two-component polyurethane coil coatings and automotive clearcoat intermediates use cyclohexanone as a tail solvent for flow and levelling without evaporating before the crosslinking window closes. In these lines, the water limit of ≤0.05% is not only about pot life; it is about film optics after flash-off. Moisture introduced with the solvent reacts with isocyanate to produce primary amine and carbon dioxide, generating bubble nucleation in a 50 µm wet film during a 140 °C forced-air cure. Transfer pumps with wetted Viton or PTFE seals are preferred because plasticizer extraction from flexible hoses adds nonvolatile contamination not detected by the GC assay. Viscosity drift in moisture-sensitive clearcoats is monitored by rotational methods such as ISO 3219:2021 or ASTM D2196-20; any upward drift relative to a water-free control is treated as a solvent quality excursion, not as a resin batch error.
Bulk storage of 99.5% technical cyclohexanone in carbon steel tanks above 5000 L is not recommended unless the tank is internally coated with a phenolic epoxy system and inerted with nitrogen. Dissolved iron at 0.5 ppm accelerates auto-oxidation to cyclohexanone hydroperoxide and darkens the product. A 1.0 m³ stainless steel tote fitted with a desiccant breather and inerted to 2% oxygen is considered a robust package; uninerted steel or lined drums exposed to repeated headspace air ingress during partial withdrawals are more likely to show incremental color and peroxide rise. Published data for this specific storage configuration is limited; suppliers may provide stability data under non-disclosure agreement. Peroxide index by iodometric titration is often not on the standard COA, but it should be requested for material intended for pharmaceutical-adjacent use, with a typical acceptance limit of ≤10 mg/kg as hydrogen peroxide.
Standard package configurations include 190 kg stainless steel drums, 1000 L stainless steel IBCs, and bulk tank wagons. Paper phenolic-lined drums are acceptable only for short-duration transit because moisture vapor transmission across the gasket can raise water content in humid climates. Procurement specifications frequently require that the COA be issued by the manufacturer’s quality control laboratory and not by a distributor. This is because intermediate storage in shared tanks can introduce water and iron. A distributor COA that omits the original production batch number is insufficient for pharmaceutical or aerospace process validation. In solvent recycling operations, recovered cyclohexanone is not automatically equivalent to virgin technical grade; it may contain dimethyl sulfoxide, alkylbenzene, or other entrainers that co-distill in the 153–157 °C range and require additional gas chromatography–mass spectrometry confirmation.
COA Retention, GHS Classification, and Bulk Handling Limits
Under the EU CLP regulation, cyclohexanone is classified as Flam. Liq. 3, H226; Acute Tox. 4, H302; Acute Tox. 4, H332; Skin Irrit. 2, H315; Eye Dam. 1, H318; STOT SE 3, H335. The closed-cup flash point is approximately 44 °C, which places the material just inside the combustible liquid band for ambient storage. Charging lines should be electrically continuous and grounded for flow velocities above 1 m/s. Vapor extraction at drum stations must maintain airborne concentration below the applicable national occupational exposure limit; many EU member states operate below 10 ppm as an 8-hour TWA, but the specific limit varies and must be taken from the current SDS. Air monitoring is typically performed by NIOSH Method 1300 or a validated equivalent.
Analytical laboratories supporting COA release operate under ISO 17025:2017 and maintain calibration records for the density meter, Karl Fischer titrator, and gas chromatograph. Retention samples are stored in sealed amber glass bottles under nitrogen at 2–8 °C for at least 24 months, which is a typical supplier quality management practice under ISO 9001:2015 clause 7.5.3. The COA archive is linked to the production batch and to the transport container so that a complaint or out-of-spec investigation can be traced back to the receiving tank or drum filling line. This traceability is part of the technical purchase specification, not a separate regulatory afterthought.