| HS Code | 648518 |
| Chemical Name | Ethanol |
| Empirical Formula | C2H6O |
| Molecular Weight | 46.07 g/mol |
| Cas Number | 64-17-5 |
| Appearance | Clear, colorless liquid |
| Solubility | Miscible with water and most organic solvents |
| Assay | 95.0% to 100.0% v/v ethanol content |
| Specific Gravity | 0.789 to 0.816 at 20°C |
| Boiling Point | 78.37°C at 760 mmHg |
| Flash Point | 13°C (closed cup) |
| Refractive Index | 1.3611 at 20°C |
| Ph | Approximately 7.0 for aqueous solution |
| Vapor Pressure | 5.95 kPa at 20°C |
| Solubility In Water | Fully miscible in all proportions |
As an accredited Ethyl Alcohol Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaging: 25 kg HDPE drums with tamper-evident seals. Ethyl Alcohol Veterinary Grade API for tablets, injections, capsules, powders, granules, premix, solutions. |
| Container Loading (20′ FCL) | 20′ FCL loading: Ethyl Alcohol Veterinary Grade API, packed in sealed drums/pails, secured upright, ventilated container, hazard-labeled, fire-safe. |
| Shipping | Shipping of Ethyl Alcohol (Veterinary Grade API) requires compliance with hazardous goods regulations. Product is supplied in sealed, UN-approved containers, properly labeled, with accompanying safety documentation. Ensure secure, upright transport away from ignition sources. Temperature-controlled, ventilated handling maintains stability and purity across all dosage forms. |
| Storage | Store in tightly closed, original containers in a cool, dry, well-ventilated area away from heat, sparks, open flames, and incompatible materials. Protect from direct sunlight and moisture. Keep container upright to prevent leakage. Ensure area is fire-safe and accessible for inspection. Follow all local regulations for flammable solvent storage. |
| Shelf Life | Shelf life: 24 months from manufacturing date, stored in tightly sealed containers, protected from light, heat, and moisture. |
In oral drench and drinking-water solution manufacture, ethyl alcohol veterinary grade API functions as co-solvent, wetting aid, and preservative adjunct. It is metered at 5%–15% v/v into 316L stainless steel vessels blanketed with nitrogen. The mixing temperature is held at 20–25°C. High-shear agitation is maintained at 500–1,000 rpm for 20–40 min. Ethanol compresses the solvent system surface tension to approximately 30 mN/m or lower, which enables wetting of actives with aqueous solubility below 0.1 mg/mL. Ethanol content is assayed by gas chromatography using USP <611> or Ph. Eur. 2.2.28, with a label claim interval of 95%–105%. Water content is controlled by USP <921> or Ph. Eur. 2.5.12. Ethanol alone below 10% v/v is not regarded as reliable preservation; potassium sorbate at 0.1%–0.3% w/w or sodium benzoate at 0.1%–0.2% w/w is added. The finished liquid is passed through a 10 µm polypropylene bag filter and filled into HDPE or aluminium-sealed bottles. Terminal products include oral drenches, drinking-water concentrates, and gel formulations for cattle, swine, and poultry. Manufacturing is performed under EU GMP Annex 4 for veterinary medicinal products. Batch-to-batch GC assay variance is controlled within ±2% relative standard deviation; published stability data for specific active combinations is limited.
Concentration limits for ethanol in injectable formulations are governed by precipitation risk, local tolerance, and residue withdrawal implications in food-producing species. In aqueous veterinary injections, ethanol is used as co-solvent at 5%–20% v/v. Non-aqueous injectables may contain 20%–50% v/v ethanol where solubility requirements justify the higher loading. Precipitation risk is screened by diluting the formulation 1:10 with simulated physiological fluid at 37°C; turbidity above 10 NTU is a failure indicator. Particle counts are confirmed by USP <788>. For small-volume injectables, limits are not more than 6,000 particles ≥10 µm and not more than 600 particles ≥25 µm per container; large-volume formats use per-mL limits of 25 and 3 respectively. Sterilising-grade filtration uses 0.22 µm PVDF or PTFE cartridges; cellulose ester membranes are avoided because ethanol can dissolve membrane components and increase extractables. Endotoxin limits are calculated from dose using USP <85>, with a common parenteral K value of 5 EU/kg. Osmolality is adjusted to 280–330 mOsm/kg with sodium chloride or mannitol where isotonicity is required. For food-producing species, ethanol residue is justified through withdrawal period calculations in the marketing authorisation. Handling during aseptic filling is conducted in fully vented isolators because of ethanol vapour flammability. Terminal presentations include injectable solutions, emulsions, and pump-administered injectable formulations.
| Injectable format | Ethanol loading | Critical control point | Filtration compatibility |
|---|---|---|---|
| Aqueous solution for IM or SC injection | 5%–20% v/v | Precipitation upon dilution; USP <788> particle limits | PVDF 0.22 µm |
| Non-aqueous injectable solution | 20%–50% v/v | Injection-site tolerance; osmolality 280–330 mOsm/kg | PTFE or PVDF 0.22 µm |
| Aseptic co-solvent system for poorly soluble actives | 10%–30% v/v | Hemolysis potential; endotoxin limit via USP <85> | PVDF 0.22 µm |
During wet granulation of moisture-sensitive veterinary tablet formulations, ethanol 96% v/v or dehydrated ethanol is used as a binder solvent for povidone K30 at 5%–10% w/w of the dry granulation mass. The granulator is operated at an impeller speed of 200–500 rpm and a chopper speed of 1,500–3,000 rpm. Granulation end point is defined by a torque rise of 30%–50% above dry blend baseline. Wet massing time is 2–6 min to limit ethanol evaporation and particle over-wetting. Wet granules are transferred to an ATEX-compliant fluid bed dryer. Inlet air is set at 45–60°C. Product temperature is maintained at 25–35°C. Drying continues until loss on drying reaches 0.8%–1.5% w/w. Because ethanol has a lower explosive limit of 3.3% v/v and an upper explosive limit of 19% v/v, solvent-wet granules are processed only under nitrogen inerting with oxygen kept below 8% v/v. Residual ethanol in the dried granulate is assayed by headspace gas chromatography under USP <467>; the acceptance threshold is not more than 5,000 ppm for the Class 3 solvent. The granulate is compressed on a rotary tablet press at 8–15 kN under ≤30% RH. Tablet hardness is maintained at 40–80 N, and friability is below 1.0% w/w per USP <1216> or Ph. Eur. 2.9.7. Terminal products include immediate-release tablets, chewable tablets, and scored tablets for companion and food-producing animals.
Liquid-fill hard capsule manufacture uses ethanol at 5%–12% w/w in the fill mass to solubilize actives that cannot be dry-filled with acceptable content uniformity. Gelatin capsule shells tolerate ethanol only within a narrow range. Above 10%–12% w/w ethanol can embrittle or deform the shell; below 3% w/w the solubility gain is often insufficient. The fill mass is held in a jacketed hopper at 25–35°C and filled into size 1 or size 2 hard gelatin or HPMC capsules on a liquid-fill capsule machine. Fill mass viscosity is maintained at 100–500 mPa·s to keep volumetric fill weight RSD below 2.0%. Capsules are sealed with a hydroalcoholic gelatin banding solution containing 25%–30% v/v ethanol and 20%–25% w/w gelatin, applied at 40–50°C. Banded capsules are dried at 20–25°C and 20%–30% RH for 2–4 h to evaporate ethanol without shell shrinkage. Disintegration is tested per USP <701>; immediate-release hard capsules commonly meet a 30 min limit. Dissolution is evaluated per USP <711> using apparatus II at 50 rpm and 37°C. Content uniformity is assessed using USP <905> with an acceptance value not more than 15. Terminal products include printed or banded veterinary hard capsules for companion animals, with batch records documenting ethanol lot assay and banding-solution viscosity.
For water-soluble veterinary powders, ethanol 96% v/v is applied as a wetting agent during pre-blending of low-dose actives before final blending with dextrose or lactose carriers. Liquid addition is 3%–8% w/w of powder mass. The wetted mass is passed through a 0.5–1.0 mm screen. Drying is carried out in a vacuum tray dryer at 40–55°C and 100–200 mbar absolute for 4–8 h. Powder moisture after drying is controlled below 1.0% w/w. Residual ethanol is monitored by headspace gas chromatography with a limit of 5,000 ppm. Granule particle size is targeted at D50 150–300 µm for rapid dissolution. Blend homogeneity is verified by stratified sampling at 10–20 points. Active assay relative standard deviation is not more than 5.0%. Final product is filled into moisture-barrier sachets or jars under ≤40% RH. Terminal products include soluble powders for oral dosing in drinking water, electrolytic powders, and nutritional powders for poultry and swine. Manufacturing facilities follow national veterinary GMP requirements and maintain solvent-handling controls because ethanol vapour remains flammable during wet screening and drying.
| Dosage form | Ethanol-related release limit | Method | Reference standard |
|---|---|---|---|
| Tablet granulate | ≤5,000 ppm residual ethanol | Headspace GC | USP <467>, VICH GL18 |
| Oral solution | 95%–105% of label claim | GC | USP <611>, Ph. Eur. 2.2.28 |
| Injectable | Registered specification | GC for ethanol content | USP <611> |
| Soluble powder / premix | ≤5,000 ppm residual ethanol in drug product | Headspace GC | USP <467>, VICH GL18 |
Ethanol-sprayed carrier systems in medicated feed premix production are typically processed in horizontal ribbon or paddle mixers equipped with a spray bar. Ethanol is sprayed at 1–3 kg/min per 1,000 kg batch onto calcium carbonate, rice hulls, or distillers dried grains with solubles. Mixer speed is 20–60 rpm. Mixing time after spray completion is 8–15 min. The ethanol carrier is removed by forced-air drying at 50–70°C for 20–40 min. Finished premix residual ethanol is controlled to below 0.5% w/w in the drug product. VICH GL18 lists ethanol as a Class 3 solvent with a PDE of 50 mg/day and a general concentration limit of 5,000 ppm. Active distribution homogeneity is assessed by assay of at least 10 samples; relative standard deviation not more than 5.0% is required. US medicated feed CGMP provisions in 21 CFR 225 require batch records linking ethanol lot identity, spray rate, and drying cycle. Terminal products include Type B medicated premixes and top-dress supplements for poultry, swine, and cattle. Ethanol is selected in these systems only where water-based spraying would cause carrier clumping or active hydrolysis; published data for specific active-carrier bonding configurations is limited.
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Ethyl Alcohol Veterinary Grade API is a pharmacopoeial, undenatured ethanol (C₂H₆O, CAS 64-17-5, molecular weight 46.07 g/mol) manufactured and released under current good manufacturing practice as an active pharmaceutical ingredient and excipient for veterinary drug products. The material is supplied as a clear, colourless, mobile liquid with a boiling point of 78.37 °C at 101.3 kPa, a closed-cup flash point of 13 °C, an anhydrous-grade density of approximately 0.789 g/cm³ at 20 °C, and a 96% v/v grade density of approximately 0.805–0.810 g/cm³ at 20 °C. Two principal grades are available. The 96% v/v grade conforms to the Ph. Eur. monograph Ethanol 96 per centum after adjustment of the azeotrope to 95.1–96.9% v/v; the anhydrous grade is released against a not-less-than 99.5% v/v gas chromatographic specification. In tablet, capsule, and granule formulations, the 96% v/v grade functions as a granulating solvent and binder carrier. In injectable and moisture-sensitive products, the anhydrous grade is preferred to avoid water introduction. Unlike industrial ethanol, the veterinary API contains no denatonium benzoate, methanol, isopropanol, or methyl ethyl ketone. Residual solvent and impurity limits follow VICH GL18 and ICH Q3C, and bacterial endotoxin control follows USP <85> when the material is designated for parenteral use.
The central distinction from industrial and reagent-grade ethanol is not bulk ethanol content but the controlled absence of denaturants and the compendial impurity profile. Industrial ethanol distributed for disinfection or fuel use commonly contains denatonium benzoate, methanol, and higher alcohols; these components can produce toxic degradation products or interfere with stability-indicating high-performance liquid chromatography methods in veterinary formulations. Reagent-grade absolute ethanol may contain benzene as a drying-solvent residue and is not released against USP <467>, VICH GL18, or Ph. Eur. monograph criteria. Veterinary-grade API is produced by fermentation and multi-stage rectification or by synthetic ethylene hydration followed by purification. Manufacturing typically uses dedicated stainless-steel 316L condensers, demountable plate columns, and molecular sieve 3A dehydration for the anhydrous grade. Release testing includes gas chromatographic limits of ≤200 ppm methanol, ≤10 ppm acetaldehyde, and ≤2 ppm benzene under the Ph. Eur. monograph; for parenteral use, bacterial endotoxins are controlled to ≤0.5 EU/mL by USP <85>. In contrast, food-grade ethanol is not necessarily manufactured under current good manufacturing practice, may have higher fusel oil residues, and is not supplied with a certificate of analysis that includes residual solvent, endotoxin, and elemental impurity data. The veterinary API also differs from denatured ethanol by providing full batch traceability to production records, packaging components, and retention samples.
Compared with other alcoholic solvents used in veterinary manufacturing, ethanol has a favourable residual solvent classification and drying profile. Isopropanol is also a Class 3 solvent but has a higher boiling point of 82.6 °C, which can extend drying time in wet granulation. Methanol, although occasionally present as an impurity, is not used as a processing solvent because of its Class 2 status and acute toxicity. Propylene glycol and glycerine are used as co-solvents and plasticisers but have higher boiling points, higher viscosities, and can alter release profiles in coated granules. Ethanol is therefore selected when rapid evaporation, low viscosity, and minimal residual solvent burden are required. The distinction from food-grade alcohol appears small on certificates of analysis showing similar ethanol content, but food-grade material is not manufactured under current good manufacturing practice for pharmaceutical excipients and is not tested for bacterial endotoxins by USP <85> unless explicitly specified.
The specification profile is defined by the Ph. Eur. monograph Ethanol 96 per centum, USP Alcohol, and, for anhydrous material, Ph. Eur. Ethanol anhydrous. Table 1 summarises the main release parameters for the veterinary API. Ethanol content is measured by gas chromatography using USP <611> alcohol determination or an equivalent pharmacopoeial method. Water content is determined by USP <921> Karl Fischer titration. Benzene is controlled as a Class 1 residual solvent under ICH Q3C to ≤2 ppm, while acetaldehyde is limited to ≤10 ppm because it forms Schiff-base adducts with primary amine-functional actives in liquid formulations. Residue on evaporation is controlled to ≤25 mg/L to limit non-volatile particulates in parenteral preparations. The anhydrous grade is hygroscopic and is stored under nitrogen after packaging; at ambient relative humidity above 60%, unprotected product can show measurable water uptake within 30 min because of the ethanol–water azeotrope at 95.6% w/w.
| Test | Method/standard | Veterinary API release limit |
|---|---|---|
| Identification | USP <611> / Ph. Eur. Ethanol 96 per centum | Retention match to ethanol reference |
| Ethanol content | USP <611> gas chromatography | 95.0–96.5% v/v for 96% grade; ≥99.5% v/v for anhydrous grade |
| Methanol | Ph. Eur. / gas chromatography | ≤100 ppm |
| Acetaldehyde | Gas chromatography | ≤5 ppm |
| Benzene | ICH Q3C Class 1 / USP <467> | ≤1 ppm |
| Residue on evaporation | Ph. Eur. evaporation residue method | ≤25 mg/L |
| Water | USP <921> Karl Fischer | ≤0.5% w/w anhydrous; 3.5–4.5% w/w for 96% grade |
| Bacterial endotoxins | USP <85> | ≤0.5 EU/mL for parenteral use |
Elemental impurities are controlled under USP <232>/<233> as applicable to the dosage form and route of administration; typical release data are requested by the finished product manufacturer because ethanol is usually a minor component after drying. Microbiological quality is also controlled for non-sterile applications; the API is not intended to be sterile as supplied, but it is produced from materials with low bioburden, and the finished preparation is sterilised when required.
For oral solid dosage forms, the 96% v/v grade is metered into a high-shear granulator or top-spray fluidised bed as the liquid phase for binder dissolution and granule formation. A typical wet-granulation process for veterinary tablets uses a 500 L stainless-steel high-shear mixer at impeller speed 2–4 m/s and chopper speed 1,500–3,000 rpm; the ethanol-based binder solution is added to a dry blend of active, filler, and disintegrant over 3–8 min. Ethanol is preferred when the formulation contains water-sensitive actives or disintegrants such as crospovidone and sodium starch glycolate, because it avoids premature swelling of disintegrant particles and preserves tablet disintegration times below 15 min in USP <701>. The resulting wet mass is dried in a fluid-bed dryer at inlet air 55–65 °C to a residual ethanol level below 0.5% w/w; above this limit, tablet hardness can decline during storage because of solvent plasticisation of polymeric binders. Ethanol is a Class 3 residual solvent under VICH GL18; therefore the 0.5% w/w limit is driven primarily by process safety and physical stability rather than toxicological thresholds. At equal binder mass, ethanol-containing granulating fluids reduce surface tension relative to water, which has a surface tension of 72.8 mN/m at 20 °C, enhancing particle wetting and narrowing granule size distribution.
Injectable and solution manufacturing imposes additional controls. Ethanol acts as a co-solvent by lowering the dielectric constant of water from 78.5 to 24.5 at 25 °C when present as the continuous phase modifier; this shift increases the saturated solubility of non-ionised lipophilic actives according to the extended Hildebrand solubility parameter. For parenteral-grade ethanol, the API must be filtered through a 0.22 µm sterilising-grade membrane and meet USP <85> bacterial endotoxins ≤0.5 EU/mL; terminal steam sterilisation at 121 °C for 15 min requires a container-closure study because ethanol vapour pressure can develop excessive headspace pressure. Typical injectable co-solvent concentrations range from 5% v/v to 30% v/v, with 10% v/v to 20% v/v being common in intramammary preparations and injectable solutions for cattle and swine. At concentrations above 30% v/v, precipitation risk and injection-site tolerability require case-specific evaluation; published species-specific tolerability data for this configuration are limited. For oral solutions, ethanol at 15–20% v/v functions as an antimicrobial preservative, with efficacy evaluated by USP <51> or Ph. Eur. 5.1.3.
Capsules, powders, granules, and medicated premixes generally use ethanol as a transient processing solvent rather than as a residual formulation component. In fluid-bed Wurster coating, a 10–25% w/w ethanol solution of a binding polymer or active is sprayed onto carrier pellets at an inlet temperature of 40–60 °C; the ethanol evaporates during the process, leaving a uniform active layer. Residual ethanol in finished premix and powder products is typically held below 0.3% w/w to prevent caking and microbial activity, with water activity below 0.6 measured by dew-point hygrometry. For liquid-fill hard capsules, ethanol may be used as a plug-forming solvent; the final ethanol content is controlled to <0.5% w/w and is justified under VICH GL18. The material is stored in stainless-steel or high-density polyethylene containers under nitrogen to maintain water content, and packaging is sized for single-use to avoid repeated opening and atmospheric moisture ingress.
| Dosage form | Role of ethanol | Typical processing condition | Control endpoint |
|---|---|---|---|
| Tablets / capsules | Wet-granulation solvent / binder carrier | 5–15% w/w of granulating solution; fluid-bed drying 55–65 °C | Residual ethanol <0.5% w/w; USP <701> disintegration <15 min |
| Injections | Co-solvent | 5–30% v/v; 0.22 µm filtration | USP <85> endotoxin ≤0.5 EU/mL; USP <788> particulate |
| Oral solutions | Solvent / antimicrobial preservative | 15–20% v/v ethanol | USP <51> antimicrobial effectiveness |
| Premix / powders / granules | Drug layering solvent | Wurster inlet 40–60 °C | Residual ethanol <0.3% w/w; water activity <0.6 |
For ethanol-wet granulated solids, the drying window is bounded by the boiling point of the solvent and the thermal stability of the active pharmaceutical ingredient. The lower boundary is set by the need to remove ethanol from the wet mass; the upper boundary is set by the glass transition temperature and melt point of the binder. In a fluid-bed dryer with inlet air at 55–65 °C, residual ethanol declines from 5–8% w/w to <0.5% w/w within 20–45 min for a 50 kg bed of granules. Processing below 55 °C extends drying time and increases the risk of incomplete solvent removal; processing above 65 °C can soften low-melting fillers or induce polymorphic conversion in thermolabile actives. Loss-on-drying is monitored at 105 °C until two consecutive samples differ by less than 0.1% w/w. Because ethanol is flammable with a flash point of 13 °C, the dryer is inerted to maintain oxygen below 8% v/v, and the solvent-handling area is classified in compliance with IEC 60079-10-1 zone requirements.
Packaging determines the long-term water content and the accumulation of oxidative by-products. The anhydrous grade is filled into 200 L stainless-steel drums or 20 L high-density polyethylene containers under nitrogen with a headspace oxygen content below 1% v/v. The 96% v/v grade may be packaged in stainless steel or high-density polyethylene, but containers must be closed immediately after dispensing because ethanol equilibrates with atmospheric moisture. Oxidative degradation of ethanol to acetaldehyde and acetic acid is accelerated by light, air, and trace transition metals; therefore amber glass is used for 1 L and 2.5 L laboratory packs. Storage at 15–25 °C in a fire-rated solvent store is required; ignition sources are excluded because the material has a flash point of 13 °C and a vapour explosion range of 3.3–19.0% v/v in air. Peroxide formation is not a primary degradation pathway for ethanol, but the product is not combined with strong oxidising agents such as potassium permanganate because exothermic oxidation can generate acetaldehyde and acetic acid.
The veterinary-grade ethanol is incompatible with strong oxidising agents, concentrated nitric acid, and certain packaging elastomers that leach plasticisers. It should not be used with denatured alcohol dispensing systems because cross-contamination with denatonium benzoate or methanol can compromise compendial compliance. For formulations containing amine-functional actives, acetaldehyde content should be monitored during long-term storage; acetaldehyde can form coloured enamines and imine adducts. In freeze-dried veterinary products, ethanol is generally removed prior to lyophilisation unless it is present as a residual solvent with a validated limit. Published data for the use of anhydrous ethanol in sustained-release implants is limited; therefore formulation-specific compatibility, local tolerance, and residual solvent validation are required before use.