| HS Code | 762320 |
| Product | Cinnamon Veterinary Grade API |
| Compatibledosageforms | Tablets, Injections, Capsules, Powders, Granules, Premix, Solutions |
| Apicategory | Veterinary-grade botanical active pharmaceutical ingredient |
| Botanicalsource | Cinnamomum cassia / Cinnamomum verum bark |
| Primaryactivemarker | Cinnamaldehyde |
| Casnumber | 104-55-2 |
| Molecularformula | C9H8O |
| Molecularweight | 132.16 g/mol |
| Physicalform | Fine free-flowing powder for dry extract grade; pale yellow to brown oily liquid for oil grade |
| Solubility | Soluble in alcohol and lipid solvents; practically insoluble in water |
| Assaypurity | Cinnamaldehyde >= 98% by HPLC |
| Lossondrying | <= 5.0% |
| Heavymetals | <= 10 ppm |
| Microbiallimits | Total aerobic count <= 1000 CFU/g; pathogens such as Salmonella, E. coli and S. aureus absent |
| Storageconditions | Store in tightly sealed containers protected from light and moisture, below 25°C |
| Shelflife | 24 months in original unopened packaging |
| Veterinaryactions | Antibacterial, antifungal, anti-inflammatory, antioxidant and digestive/carminative activity |
As an accredited Cinnamon 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 | Cinnamon Veterinary Grade API supplied in sealed, light-resistant containers, 25 kg net, suitable for tablets, capsules, powders, granules, premix, and injections. |
| Container Loading (20′ FCL) | 20′ FCL container loading securely transports Cinnamon Veterinary Grade API for tablets, injections, capsules, powders, granules, premix, solutions. |
| Shipping | Cinnamon Veterinary Grade API is shipped in sealed, inert containers with proper hazard labeling and documentation. Shipments comply with international transport regulations, using temperature-controlled, moisture-protected logistics. Handling follows veterinary safety protocols to prevent contamination, ensuring product integrity during domestic or international delivery. |
| Storage | Store Cinnamon Veterinary Grade API in tightly sealed, original containers in a cool, dry, well-ventilated area, protected from light, moisture, and heat. Maintain controlled room temperature (20–25°C) unless otherwise specified. Avoid freezing for solutions/injections. Keep separate from feed, food, and incompatible substances. Ensure containers remain labeled and closed when not in use. |
| Shelf Life | Shelf life is typically 24 months when stored in tightly sealed containers, protected from light, moisture, and heat. |
In broiler and layer integration units, cinnamaldehyde standardized to ≥ 98% area purity by gas chromatography is formulated as a phytogenic feed additive rather than as a simple aromatic flavoring. The predominant field application is in complete feed and drinking water for broilers, layers, and turkeys, where the target is modulation of intestinal Clostridium perfringens populations and reduction of gut-origin ammonia. Feed-grade products are normally supplied as a 10% spray-dried powder on a maltodextrin–gum arabic carrier, which is pre-blended before addition to the mixer. Compliance for this use falls under Regulation (EC) No 1831/2003, sensory additives, flavouring functional group 2(b), and under 21 CFR 582.20 for GRAS essential oil and oleoresin use in the United States; disease-treatment claims are outside the authorization boundary. Finished feed inclusion rates reported in commercial broiler programs cluster between 50 mg/kg and 150 mg/kg complete feed, while drinking-water applications are typically dosed at 20–60 mg/L final water concentration through a proportional medicator. The upper boundary is not governed by toxicology but by palatability: feed refusal and water intake suppression appear in young birds when cinnamaldehyde exceeds 200 mg/kg or 80 mg/L, respectively. Terminal product formats include broiler complete feed, layer concentrate premix, turkey water-soluble powder sachets, and powdered top-dresses for floor-reared pullets.
Downstream production of the feed-grade powder begins with a high-shear pre-emulsion of cinnamaldehyde in water and gum arabic, followed by spray drying at inlet temperature 160–180°C and outlet temperature 70–85°C. Spray-dried particles with D50 80–150 µm are then blended in a double-ribbon mixer for 8–12 min with precipitated silica or calcium carbonate to reach a workable premix. For pelleted broiler feed, the product is best added after steam conditioning because free cinnamaldehyde exhibits measurable volatility at 85°C, and unprotected material can partition into the vapour phase during retention times of 45–90 s. For water-soluble powders, cinnamaldehyde is solubilized with polysorbate 80 and propylene glycol to form a concentrate of 20–40 g/L, then filtered through a 45 µm in-line cartridge before filling into sachets. The production bottleneck is not chemical degradation but segregation: if the spray-dried intermediate has a bulk density below 0.35 g/cm³, it can stratify in pneumatic transfer lines and create batch-to-batch dose variance.
Steam conditioning at 70–75°C before pellet compression creates two competing demands in swine creep and prestarter feed: the heat is required to gelatinize starch and bind the pellet, but it also accelerates volatilization of low-molecular-weight aldehydes when cinnamon API is added as a free oil. Field data from nursery flows show that unprotected cinnamaldehyde added before conditioning can lose a substantial fraction during holding, and the residual material may migrate to the cooler, outer surface of the pellet. The effective inclusion range for nursery pigs is 100–250 mg/kg complete feed; above 300 mg/kg, feed intake can decline due to aversive olfactory response in newly weaned pigs. Products designed for this application are therefore manufactured as hydrogenated vegetable oil–coated granules or adsorbed onto porous carriers such as fumed silica before extrusion. Compliance remains under Regulation (EC) No 1831/2003, sensory additives, flavouring functional group 2(b), and 21 CFR 582.20, with additional feed-mill hygiene control under ISO 6579-1:2017 for Salmonella absence in 10 g of final feed.
The standard production route for granulated cinnamaldehyde is fluid-bed top-spray coating. A starter core of crystalline dextrose or sodium chloride is sprayed with molten palm stearin at 58–62°C containing dissolved cinnamaldehyde, then cooled to ambient temperature over 20–30 min. The resulting granules are sized over a 20–80 mesh sieve before blending into a creep feed mineral-vitamin premix. In the feed mill, the premix is added to a horizontal paddle mixer for 5–7 min before post-pelleting liquid application or direct meal feeding. Pellet dies of 3.0–4.5 mm are used for prestarter crumbles, and the target moisture after conditioning is 15–17%. Terminal product formats include granulated prestarter crumbles, creep feed pellets, and top-dress powder for hospital pens. The critical control point is retained assay after extended storage in warm farrowing rooms; uncoated material stored at 30°C for 30 days can exhibit measurable loss, whereas lipid-coated granules show greater retention.
Addition of free cinnamaldehyde directly into a dairy total mixed ration horizontal mixer results in uneven distribution because the compound partitions onto oil-coated particles and can flash off when the mixer is operated under elevated summer ambient conditions. In commercial dairy and beef applications, cinnamon-derived API is therefore incorporated into rumen-protected or adsorbed matrices at 50–150 mg/kg dry matter, most often as a flavouring and appetite-stabilizing fraction rather than as a quantified methane inhibitor. Peer-reviewed in vitro data show shifts in acetate-to-propionate ratio under high-concentrate substrates, but published in vivo responses in high-forage TMR are inconsistent; the operational boundary is therefore limited to use as a sensory additive or complementary minor feed constituent. Compliance for this placement is governed by Regulation (EC) No 1831/2003, sensory additives, flavouring functional group 2(b), and 21 CFR 582.20 for US use. No US production claim for methane suppression is authorized for cinnamaldehyde.
The downstream production route for dairy premix begins with adsorption of cinnamaldehyde onto fine-particle calcium carbonate or wheat middlings to create a 5–10% active intermediate, followed by blending with trace minerals and vitamins in a double-cone mixer for 10–15 min. For molasses lick blocks, the intermediate is mixed with molasses and urea liquor, heated to 55–60°C, and poured into forms; the product must cool below 35°C before wrapping to avoid exudation. In pelleted beef mineral supplements, the cinnamaldehyde fraction is best introduced after pellet cooling via a liquid spray drum because the pellet die temperature exceeds the vapour pressure threshold of the free aldehyde. Terminal product formats include dairy TMR premixes, beef mineral granules, molasses-urea block supplements, and dry cow mineral packs. The principal limitation is uniform distribution: if the active premix is not pre-diluted to at least 1:9 with ground corn or rice hulls before addition to the TMR mixer, dose heterogeneity can exceed 25% relative standard deviation.
| Application zone | Typical inclusion range | Dominant process loss mechanism | Process control route |
|---|---|---|---|
| Poultry drinking water | 20–60 mg/L | aqueous solubility instability | polysorbate 80 stock solution; metered dosing |
| Poultry complete feed | 50–150 mg/kg | steam conditioning volatilization | spray-dried microcapsules; post-conditioning addition |
| Swine creep feed | 100–250 mg/kg | pellet compression heat and oxidation | lipid-coated granules; post-pelleting spray |
| Dairy TMR | 50–150 mg/kg DM | mixer volatility and particle segregation | adsorbed premix; rumen-protected matrix |
| Aquafeed | 0.5–1.0 g/kg | extrusion barrel flash-off; water leaching | vacuum oil coating with emulsifier |
| Canine dental tablets | 0.1–0.5% w/w | plasticization of tablet matrix | wet granulation; adsorbent pre-blend |
| Topical solution | 0.5–2.0% w/v | oxidation and pH drift | cold mixing with antioxidant; dark container fill |
Extrusion cooking of shrimp and tilapia feed raises the feed mass to 110–135°C at the die, which exceeds the thermal stability window of free cinnamaldehyde; therefore the only practical point of addition is post-extrusion vacuum coating. In aquaculture applications, cinnamon-derived API is used at 0.5–1.0 g/kg dry feed as a feed attractant and antimicrobial adjunct in oil-coated pellets, with published trials in whiteleg shrimp and tilapia clustering in this range. The compliance framework is Regulation (EC) No 1831/2003, sensory additives, flavouring functional group 2(b), and 21 CFR 582.20 in the United States, without an aquaculture-specific MRL because cinnamaldehyde is not classified as a pharmacologically active residue. Post-extrusion vacuum coating is performed at 0.3–0.5 bar negative pressure with fish oil or soybean oil as the carrier; liquid retention time in the coater is 6–10 min, and the oil temperature is kept below 50°C to reduce volatile stripping. Terminal product formats include extruded whiteleg shrimp pellets, tilapia floating feed, and ornamental fish flakes.
Process control in aquafeed top-dressing is dominated by emulsion stability and leaching. If cinnamaldehyde is introduced as a neat liquid into the coater, it is poorly distributed and can volatilize during vacuum release; the standard procedure is to pre-solubilize the API in the coating oil with a non-ionic emulsifier at 0.5–1.0% of oil volume. Vacuum-coater paddle speed is set to avoid pellet breakage while maintaining oil uptake uniformity; pellet oil content is commonly raised to 6–10% to seal surface pores and limit leaching into pond water. For high-fat salmonid feeds, absorption capacity of the extrudate limits the coated cinnamaldehyde dose, and over-coating can reduce water stability. The operational boundary is the lack of direct gastric retention specificity in fish: the ingredient functions as a waterborne sensory cue during pre-consumption and as a gut antimicrobial only after ingestion; published data for this specific configuration is limited for cold-water species.
Tablet compression of cinnamon-derived cinnamaldehyde presents a plasticization boundary: the liquid aldehyde can reduce tensile strength by coating binder particles, causing punch sticking and weight variability in high-speed rotary presses. For canine oral-care chew tablets and breath-freshening tablets, cinnamaldehyde is used as a flavouring and mild antimicrobial at 0.1–0.5% w/w of the tablet mass, a concentration that does not dominate the formulation but is sufficient to alter compaction behaviour. The preferred production route is wet granulation of the API with polyvinylpyrrolidone and dibasic calcium phosphate in a high-shear granulator, followed by fluid-bed drying at inlet 45–55°C. Compression is carried out on a rotary tablet press at 12–20 kN main compaction force, with friability controlled to ≤1.0% according to USP <1216>. Compliance for pet food supplements is covered by 21 CFR 582.20 and AAFCO ingredient definitions, with residual solvent limits under USP <467>.
Terminal product formats include chewable oral-care tablets, dental powder sachets, and oral sprays. In tablet production, the addition of cinnamon API is delayed until the granulation end phase to avoid over-wetting the binder solution; direct compression is possible only when the API is pre-adsorbed onto fumed silica or calcium silicate at 1:1 ratio. The critical defect mode is capping at low moisture content, so granule moisture is held at 2.0–3.5% before tableting. Oral-spray solutions are prepared separately by cold mixing cinnamaldehyde with ethanol, polysorbate 80, and buffered water to a final concentration of 0.05–0.2% w/v. Published data for cinnamaldehyde release kinetics in canine dental matrices is limited; compendial dissolution methods are adapted from human chewable dosage forms only as an internal quality target.
| Market or scope | Standard or regulation | Relevant control parameter |
|---|---|---|
| EU feed sensory additive | Regulation (EC) No 1831/2003 | flavouring functional group 2(b) |
| US GRAS feed use | 21 CFR 582.20 | natural extractive and flavouring; no disease claim |
| Salmonella absence in feed | ISO 6579-1:2017 | absence in 10 g |
| Residual solvents in API | USP <467> | Class 2 solvent limits |
| Tablet friability | USP <1216> | ≤1.0% |
Dilution of cinnamon oil or cinnamaldehyde to 0.5–2.0% w/v final concentration, most often in polysorbate-solubilized aqueous systems, is used in veterinary dermatology as an adjunctive preparation for superficial dermatophytosis and yeast management in companion animals. Production is carried out by cold mixing cinnamaldehyde with propylene glycol and polysorbate 80, then incorporating purified water, with pH adjusted to 5.0–6.5 using citric acid or sodium citrate; the solution is filtered through a 0.45 µm membrane and filled into dark HDPE containers to limit photodegradation. Terminal product formats include ear wash solutions, skin rinse concentrates, hoof-care sprays, and dilute wound-irrigation adjuncts. Compliance for topical veterinary preparations follows 21 CFR 582.20 for GRAS status of the ingredient and current good manufacturing practice for finished pet products, but dermatological claims are subject to local regulatory review. Dermal tolerance is concentration-dependent: undiluted cinnamaldehyde is a strong irritant and should not be applied directly; repeated topical exposure at concentrations above 2.0% w/v may induce erythema and vesiculation. Injectable formulations are not represented in this scenario set because no compendial veterinary parenteral monograph supporting cinnamon-derived cinnamaldehyde was identified; published safety and efficacy data for this specific indication remain limited.
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Model CINN-VET-API 25/200 is a standardised dry extract prepared from Cinnamomum verum J. Presl bark and supplied as an active pharmaceutical ingredient for veterinary tablets, capsules, oral powders, granules, feed premixes, oral solutions, and—in a dedicated reduced-endotoxin grade—injectable preparations. The standard grade is designated CINN-VET-API 25/200; the parenteral grade is designated CINN-VET-API 25/200-P and is tested for bacterial endotoxin according to Ph. Eur. 2.6.14. The extract is standardised to not less than 25.0% and not more than 30.0% cinnamaldehyde by gas chromatography with flame ionisation detection. The material is a pale tan to brown free-flowing powder with a characteristic aromatic odour, controlled particle-size distribution, and residue profile intended for pharmaceutical blending rather than spice or food use.
Release testing combines pharmacopoeial botanical identity with residue and particle-size controls specific to veterinary dose-form processing. The methods are drawn from current pharmacopoeial and ISO protocols; the extract is released only after all parameters in the following matrix meet the stated limits.
| Quality attribute | Test method | Acceptance criterion |
|---|---|---|
| Appearance | Visual / organoleptic | Pale tan to brown free-flowing powder |
| Identification | HPTLC fingerprint against cinnamaldehyde reference | Positive match |
| Assay, cinnamaldehyde | GC-FID, external standard | 25.0%–30.0% w/w |
| Eugenol content | GC-FID | ≤2.5% w/w |
| Coumarin content | HPLC-UV | ≤0.10% w/w |
| Loss on drying | Ph. Eur. 2.2.32 | ≤5.0% |
| Heavy metals | Ph. Eur. 2.4.8 | ≤20 mg/kg |
| Lead | ICP-MS | ≤3.0 mg/kg |
| Arsenic | Ph. Eur. 2.4.2 | ≤2.0 mg/kg |
| Residual solvents | ICH Q3C Option 1 | Class 1 absent; Class 2 within PDE |
| Microbial limits | Ph. Eur. 5.1.4 | TAMC ≤10³ CFU/g; TYMC ≤10² CFU/g; Escherichia coli absent in 1 g; Salmonella absent in 25 g |
| Bacterial endotoxin, parenteral grade | Ph. Eur. 2.6.14 | ≤0.5 EU/mg |
| Particle size | ISO 13320, laser diffraction | D90 ≤250 µm; D50 75–150 µm |
| Bulk density | Ph. Eur. 2.9.15 | 0.45–0.65 g/mL |
| Tapped density | Ph. Eur. 2.9.15 | 0.55–0.75 g/mL |
Direct aqueous injection of the dry extract is not operationally feasible because cinnamaldehyde has low water solubility, typically below 2 g/L at 25 °C, and the co-extracted polyphenol fraction can generate turbidity in simple aqueous vehicles. Injectable formulations should be compounded with a co-solvent system consisting of propylene glycol and sulfobutylether-β-cyclodextrin at a cinnamaldehyde-to-cyclodextrin molar ratio between 1:1 and 1:3, adjusted to pH 4.5–6.5 with citrate buffer. The solution is prefiltered through a 0.45 µm PVDF membrane and sterilised by filtration through a 0.22 µm PVDF membrane. Terminal steam sterilisation at 121 °C is not recommended unless oxidative degradation products are monitored, because cinnamaldehyde is susceptible to oxidation in aqueous media. The parenteral grade is controlled to ≤0.5 EU/mg bacterial endotoxin and is tested for particulate matter according to Ph. Eur. 2.9.19. Fluoropolymer-coated stoppers are required; uncoated rubber closures may release vulcanisation accelerators into the cinnamaldehyde-containing vehicle. Published stability data for this exact co-solvent system remain limited; pilot-scale filter compatibility studies are advised before commercial batch manufacture.
Tablet manufacture with the standard grade requires attention to aldehyde volatility and flow. In direct compression, the extract is preblended with microcrystalline cellulose and crospovidone for 5 min at 12 rpm in a bin blender, then lubricated with magnesium stearate for 3 min. Direct compression is limited to extract loadings not greater than 15% w/w; above this level, die-fill variation on rotary presses can exceed 3% RSD and tablet weight variability increases.
At extract loadings above 15% w/w, wet granulation is preferred. The extract, lactose monohydrate, and microcrystalline cellulose are granulated with an aqueous binder containing 5% w/v polyvinylpyrrolidone K30 in a high-shear granulator at impeller speed 250 rpm and chopper speed 1500 rpm. Granules are dried in a fluid-bed dryer at inlet air temperature 50 °C until loss on drying reaches 2%–4% w/w, then milled through a 1.0 mm screen. Drying above 60 °C is avoided because marker loss and colour darkening increase. Compressed tablets are produced to a hardness of 50–80 N; friability is controlled to ≤1.0% using Ph. Eur. 2.9.7.
For hard gelatin capsule filling, the extract is milled through a 500 µm conical mill, blended with lactose monohydrate at 1:3 w/w to 1:5 w/w, and filled on a dosator capsule machine. If the extract fraction exceeds 15% w/w, colloidal silicon dioxide at 0.5% w/w is added to keep angle of repose below 35° and reduce segregation. Capsules are packaged in high-barrier aluminium blister or amber glass because cinnamaldehyde can diffuse into low-density plastic films. Powders for oral administration are prepared by geometric dilution in 3 steps with dextrose or lactose monohydrate in a ribbon mixer; final in-feed cinnamaldehyde levels below 100 mg/kg require a preblend to prevent carryover. Granules for sachets are wet-granulated as above, but milled to a narrower cut between 0.5 mm and 1.25 mm to improve reconstitution in drinking water. Feed premixes are produced by adsorbing the extract onto precipitated silica at 1:1 w/w, then mixing with calcium carbonate carrier in a double-shaft paddle mixer for 10 min; the adsorbed premix remains free-flowing at storage humidities up to 60% RH. Oral solution concentrates are prepared as a 10% w/v stock in propylene glycol and polysorbate 80, heated to 40 °C under nitrogen, and dispersed at 6000 rpm for 10 min before filtration through 0.45 µm; dilution with reverse-osmosis water should be used within 24 h unless the reservoir is covered and protected from light.
The processing envelope is summarised below.
| Dosage form | Typical loading range | Critical processing equipment | Primary failure mode controlled |
|---|---|---|---|
| Tablets, direct compression | 5–15% w/w | Bin blender, rotary tablet press | Die-fill variation, capping |
| Tablets, wet granulation | 15–30% w/w | High-shear granulator, fluid-bed dryer | Segregation, excessive friability |
| Capsules | 5–15% w/w; higher with glidant | Conical mill, dosator capsule filler | Segregation, poor flow |
| Injections | 0.5–5% w/v | PVDF membrane filtration train, 0.45/0.22 µm | Particulate matter, endotoxin |
| Oral solutions | 5–10% w/v stock | High-shear disperser, nitrogen blanketing | Oxidative loss, light sensitivity |
| Powders | 0.1–2% w/w in final feed | Ribbon mixer | Non-uniform distribution |
| Granules | 0.5–1.25 mm cut | Fluid-bed dryer, oscillating granulator | Caking on storage |
| Premix | 1–5% w/w extract on silica | Double-shaft paddle mixer | Caking above 60% RH |
The veterinary-grade standardised extract differs from commodity food-grade cinnamon powder in four measurable parameters. Cinnamaldehyde content is controlled to 25.0%–30.0%, whereas milled bark may vary from 0.5% to 4% depending on botanical origin, storage, and milling. Microbial limits are pharmacopoeial; Salmonella is absent in 25 g and Escherichia coli is absent in 1 g under Ph. Eur. 5.1.4. Particle size is engineered to a D90 of ≤250 µm by laser diffraction according to ISO 13320, whereas food powders retain irregular fibres that segregate during pharmaceutical blending. Coumarin is monitored by HPLC-UV and limited to ≤0.10%; this is a critical control for companion animals because Cinnamomum cassia-derived food products may contain substantially higher coumarin. Relative to synthetic cinnamaldehyde with an assay of ≥98%, the standardised extract retains native polyphenols and tannins; these co-extractives alter solubility, colour, and tablet binding, and can act as sacrificial antioxidants, but they also require GC-FID rather than UV assay because of spectral interference. Relative to cinnamon essential oil, the dry extract has lower volatility and fewer headspace losses during tableting and granulation; essential oil is liquid and must be adsorbed onto silica at loadings above 2% w/w to avoid processing losses.
Store the API in sealed, nitrogen-flushed HDPE drums at 2–8 °C. If the material is exposed to relative humidity above 60%, pre-dry at 40 °C for 4–6 h before tableting or capsule filling to prevent picking and weight variation. Avoid combination with strong oxidising agents and with primary amine-containing feed additives such as certain amino acid supplements, because aldehyde-amine Schiff base formation can reduce potency. The standard grade is not suitable for parenteral use; the dedicated CINN-VET-API 25/200-P grade must be specified for injectable products.