| HS Code | 450549 |
| Api Substance | Chlorphenamine Maleate (Veterinary Grade) |
| Molecular Formula | C20H23ClN2O4 (as maleate salt); C16H19ClN2 (as free base) |
| Molecular Weight | 390.86 g/mol (maleate salt) |
| Cas Number | 113-92-8 |
| Physical Appearance | White or almost white crystalline powder |
| Solubility | Freely soluble in water; sparingly soluble in ethanol; practically insoluble in ether |
| Melting Point | 132°C to 135°C |
| Pka Values | Approximately 4.0 and 9.2 in aqueous solution |
| Assay Content | 98.0% to 102.0% on dried basis |
| Ph Of 1 Aqueous Solution | 3.0 to 5.0 |
| Storage Conditions | Store in airtight, light-resistant containers at controlled room temperature |
| Pharmacological Property | Competitive H1 receptor antagonist with antihistamine activity for veterinary use |
As an accredited Chlorphenamine 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 | Packaged in 25 kg net double-lined polythene drums or sealed multilayer bags, protected from moisture, light, and contamination for veterinary grade use. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Chlorphenamine Veterinary Grade API, packed in sealed drums, for tablets, injections, capsules, powders, granules, premix, and solutions. |
| Shipping | Chlorphenamine Veterinary Grade API is shipped in sealed, inert containers to protect purity and stability. Transport follows cold-chain or temperature-controlled protocols as required, with proper hazardous material labeling and handling. Full documentation, including COA, MSDS, and veterinary compliance certificates, accompanies every shipment for regulatory clearance and safety. |
| Storage | Store Chlorphenamine Veterinary Grade API in tightly sealed, moisture-proof containers in a cool, dry, well-ventilated area, protected from direct sunlight and strong light. Maintain temperatures below 25°C. Keep away from oxidizing agents and incompatible materials. Ensure facility is secure and clearly labelled, adhering to veterinary GMP guidelines and local regulations. |
| Shelf Life | Shelf life is 36 months when stored in original sealed container, below 25°C, protected from light and moisture. |
In small-animal antihistamine tablet manufacturing, chlorphenamine maleate is incorporated at a nominal 4 mg per tablet for canine pruritus and 2–4 mg per tablet for feline use, with the active pharmaceutical ingredient fraction at 2.0% w/w in a 200 mg core. The API must conform to Ph. Eur. 0386 and USP Chlorpheniramine Maleate, with assay on dried basis 98.0–102.0% and related substances not more than 0.5%. The finished tablet must meet USP <905> or Ph. Eur. 2.9.40 uniformity of dosage units with an acceptance value not greater than 15.0, and dissolution per USP <711> Apparatus II at 50 rpm in 900 mL of 0.1 M hydrochloric acid at 37±0.5°C; a typical premarketing specification is Q=80% at 30 min. The tablet core comprises microcrystalline cellulose 45–55% w/w, anhydrous lactose 30–40% w/w, crospovidone 2–4% w/w, colloidal silicon dioxide 0.5–1.0% w/w, and magnesium stearate 0.5–1.0% w/w. Wet granulation is preferred over direct compression when the chlorphenamine maleate source is micronized with a D90 below 75 µm because low-dose blend segregation has been observed in bin blenders at 12 rpm when API particle size D50 drops below 10 µm.
The aqueous granulation binder is hypromellose 3 mPa·s at 1.5–2.5% w/w, added in a top-drive high-shear granulator at impeller tip speed 5–8 m/s; wet massing is held to 2–4 min. The granulate is dried in a fluid-bed dryer with inlet air at 60–70°C and product temperature 35–40°C to a loss-on-drying window of 1.5–3.0% w/w; batches with LOD below 1.5% w/w show increased capping on 27-station rotary tablet presses, while LOD above 3.0% w/w produces sticking to B2/D2 tooling at main compression above 15 kN. The dried granulate is passed through a 0.8 mm oscillating sieve, lubricated in a V-blender at 60% volumetric fill for 5 min, and compressed with precompression 3–6 kN and main compression 8–15 kN to 50–80 N hardness. Tablet friability must be not more than 1.0% per USP <1216>, and package light transmission is controlled per USP <671> because chlorphenamine maleate photodegradation accelerates in non-amber packaging. Terminal dosage forms are round, single-scored biconvex tablets in 60 cc HDPE bottles with a 2 g silica-gel desiccant, or in PVC/PVDC blister. A known process conflict is that magnesium stearate levels above 1.0% w/w slow dissolution to below 80% at 30 min due to hydrophobic film formation on the granules; therefore, lubrication time is capped at 5 min and the stearate is screened through 500 µm before use.
Sterile filtration of a 10 mg/mL chlorphenamine maleate injection is governed by the pH-dependent equilibrium between the water-soluble maleate salt and the poorly water-soluble free base; the solution is buffered to pH 5.0–5.5 with 0.1 M hydrochloric acid or sodium hydroxide, because above pH 6.5 free base precipitation reduces filter flux and raises subvisible particle counts. The formulation consists of chlorphenamine maleate 10 mg/mL, sodium chloride 9.0 mg/mL, water for injection q.s., and, if a multidose presentation is selected, benzyl alcohol 1.5% v/v; single-use vials omit the preservative but require a nitrogen overlay during filling. The solution is compounded in a 316L stainless steel jacketed vessel at 20–25°C, protected from light, and sparged with nitrogen to reduce dissolved oxygen below 0.5 mg/L. A 0.45 µm polypropylene prefiltration cartridge is followed by a 0.22 µm PVDF or PES sterilizing-grade membrane with a filter area of not less than 0.5 m² per 200 L batch; pressure differential is maintained below 1.0 bar because chlorphenamine maleate solutions above 25°C accelerate N-oxide degradation and can foul downstream membranes.
Industry compliance for this injectable line includes 21 CFR 210/211, USP <1>, USP <85>, USP <788>, USP <1207>, Ph. Eur. 5.1.1, and EU GMP Annex 1 with ISO 14644-1 Class 5 filling. Bacterial endotoxins are controlled per USP <85>; because the maximum bolus dose in equine practice can be 250 mg, the endotoxin limit is calculated from the 5 EU/kg/h parenteral threshold and the batch must typically meet an API endotoxin limit of not more than 0.5 EU/mg. Sterility testing follows USP <71> or Ph. Eur. 2.6.1 with 14-day incubation; container closure integrity is verified by vacuum decay per USP <1207>. Terminal sterilization by steam is not automatically feasible because the maleate salt can undergo hydrolytic degradation above 121°C; aseptic filtration is therefore the standard process, and any terminal sterilization program requires photostability and thermal stability data under ICH Q1B and ICH Q1A. The terminal product is filled into amber Type I borosilicate glass vials of 10 mL or 50 mL, closed with chlorobutyl rubber stoppers and aluminium flip-off seals. A known production failure mode occurs when line stoppages exceed 90 min between prefiltration and final filtration: microbial proliferation in the intermediate bulk can elevate bioburden above 10 CFU/100 mL and require batch reprocessing or rejection.
Because feline dosing frequently requires volumes below 0.5 mL, chlorphenamine maleate oral solution is manufactured at 0.4 mg/mL (2 mg/5 mL) with a target dose of 2 mg per cat every 12 h. The solution uses purified water as basis, sorbitol 70% non-crystallizing at 20–30% w/v, glycerin 10–20% w/v, citric acid–sodium citrate buffer to hold pH 4.5–5.5, sodium benzoate 0.1% w/v or potassium sorbate 0.15% w/v, and sucralose 0.05% w/v. The manufacturing sequence includes high-shear mixing at 1,800–2,500 rpm for 15 min to dissolve the API, pH adjustment with 0.1 N citric acid, and clarification through 1.2 µm followed by 0.45 µm polypropylene filters; the filtered bulk is held under nitrogen pressure below 0.5 bar until filling. Filling is performed on a 12-head volumetric liquid filler into amber PET bottles of 100 mL, with an in-process fill weight check every 15 min per 21 CFR 211.184. Compliance references include USP <795> for hospital dilution, VICH GL18 residual solvent testing, ICH Q3D elemental impurity limits, and USP <1231> water quality. Light stability under ICH Q1B is mandatory because aqueous chlorphenamine maleate forms N-oxide photodegradants; amber packaging and cartons are specified. The terminal dosage form is a 2 mg/5 mL oral solution with a graduated dropper calibrated to deliver 0.1 mL increments; batch release includes assay 95.0–105.0% of label claim, pH 4.5–5.5, preservative efficacy per USP <51>, and microbial limits of not more than 100 CFU/mL total aerobic microbial count and not more than 10 CFU/mL total yeast and mold count.
Equine top-dress granules containing chlorphenamine maleate are formulated at 1.25% w/w API to deliver 125 mg chlorphenamine maleate in a 10 g dose cup for a 500 kg horse at 0.25 mg/kg body weight. The carrier system is a dibasic calcium phosphate–lactose composite 85–92% w/w, povidone K30 2–4% w/w as a wet binder, and microcrystalline cellulose 5–10% w/w as a spheronization aid. The addition ratio is restricted to a maximum of 2.0% w/w because higher API loading reduces granule flow to below 10 g/s through a 15 mm orifice and increases dusting below 45 µm; dusting is limited to not more than 15% w/w of the granulation and measured by sieve analysis per USP <786> or Ph. Eur. 2.9.38. The process runs in a top-drive high-shear granulator at an impeller tip speed of 5–8 m/s, with the binder solution added at 8–12% w/w and wet massing held at 2–4 min. Drying in a fluid-bed unit at 60–70°C inlet air to a final loss on drying of 1.5–2.5% w/w is followed by size classification over 0.5 mm and 1.0 mm sieves; granule D50 is controlled at 150–250 µm.
Compliance for this non-sterile oral powder product is anchored to 21 CFR 210/211, EU GMP Part I, VICH GL18 for residual solvents, and USP <905> blend uniformity with a stratified sampling plan across at least 10 locations; blend coefficient of variation should not exceed 5.0%. The terminal product is filled into 10 g graduated dosing cups or three-side-sealed sachets, with net weight variation not more than ±5% and water activity below 0.60. For operators, chlorphenamine maleate is an antihistamine with anticholinergic effects; engineering controls must limit airborne dust to the OEL established in the site hygienic plan, and ISO 14644-1 Class D is normally sufficient for product protection because the dosage form is not sterile. A notable process boundary is that ambient relative humidity above 60% during granulation and filling increases moisture uptake in the lactose carrier, raises granule stickiness, and generates 0.5–2.0 mm agglomerates that can cause dose cup weight variability. Published multi-batch process capability data for chlorphenamine maleate at this specific 1.25% w/w equine granule loading is limited; therefore, process validation typically uses a 3-batch homoscedasticity check rather than a compressed historical parameter range.
Because the labeled dose is 2 mg chlorphenamine maleate for cats and tablet splitting is considered inaccurate for home administration, hard gelatin capsule manufacture is selected; the capsule fill mass is 90 mg in a size 4 hard gelatin or hydroxypropyl methylcellulose capsule, giving an API fraction of 2.2% w/w. Direct filling is feasible only if the API is preblended in a 1:10 geometric dilution with lactose monohydrate for 10 min at 12 rpm in a bin blender; the preblend is then passed through a 500 µm screen before final blending at 60% volumetric fill for 15 min. Magnesium stearate is limited to 0.25–0.5% w/w and talc to 1–2% w/w; exceeding 0.5% stearate delays disintegration beyond 15 min in 0.1 M hydrochloric acid. Filling is performed on a dosator-type automatic encapsulator at 25,000–40,000 capsules/h with fill weight checks every 15 min; the weight variation standard is USP <905> or Ph. Eur. 2.9.40 with acceptance value not greater than 15.0. Dissolution testing uses USP <711> Apparatus I at 100 rpm in 900 mL of 0.1 M hydrochloric acid with Q=80% at 30 min. Compliance includes 21 CFR 211, ICH Q1A stability, ICH Q3D elemental impurities, and USP <61>/<62> microbial limits. Because capsules are moisture-sensitive, aluminium/PVC cold-form blister packaging is preferred over bottles, with USP <671> light-transmission containers. Terminal product is a 2 mg hard gelatin capsule in aluminium/PVC cold-form blister, stored below 25°C. A documented low-dose production issue is electrostatic adhesion of micronized chlorphenamine maleate to the walls of the bin blender after the geometric dilution step; if blender humidity drops below 30% RH, API recovery can fall below 95% of label claim, requiring post-blend API assay before encapsulation.
In hospital feed preparation, a non-sterile oral premix intermediate containing chlorphenamine maleate at 5.0% w/w is incorporated at 0.1% w/w of final feed, equivalent to 1 kg premix per 1,000 kg feed, to yield 50 mg/kg API in feed and deliver 125 mg chlorphenamine maleate per 2.5 kg feed for a 500 kg horse at 0.25 mg/kg. The carrier is ground oat hulls or maltodextrin 80–90% w/w, with silicon dioxide 1–2% w/w as flow aid and corn starch 5–10% w/w as dust binder. Mixing uses a double-cone blender at 60% volumetric fill and 10 rpm for 20 min; a geometric dilution sequence in three steps is required because the API is active at 5% while the final feed concentration is only 0.005% w/w. Homogeneity is assessed by sampling at 10 locations with a coefficient of variation not more than 5.0% for the premix and not more than 10% for the diluted feed.
Regulatory status varies by jurisdiction: under EU Regulation (EU) 2019/4 on medicated feed, equidae are food-producing unless permanently excluded from the food chain, so the horse’s non-food status must be documented and the premix must not enter supply chains for food-producing species. In the United States, 21 CFR 225 current good manufacturing practice for medicated feed applies if the premix is used in a commercial feed mill; hospital extemporaneous dilution may instead fall under USP <795>. Cross-contamination control is the primary operational risk: because chlorphenamine maleate is a pharmacologically active antihistamine, dedicated scoops and dust extraction are used, and cleaning validation is performed with swab limits derived from a health-based exposure assessment per EMA guidance rather than a fixed visual-clean criterion. Published residue data for chlorphenamine maleate in feed premix equipment is limited; therefore, a conservative default cleaning limit of 1 µg/cm² is often applied until a product-specific permitted daily exposure is calculated. Terminal packaging is 1 kg foil-lined HDPE jars or 5 kg aluminium foil bags with desiccant, stored below 25°C and protected from light. The premix is not sterile, not suitable for parenteral use, and not authorized in several jurisdictions for food-producing animal feed.
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Chlorphenamine Veterinary Grade API is the maleate salt of chlorphenamine, CAS 113-92-8, supplied as a white to almost white crystalline powder with nominal molecular weight 390.86 g/mol. The active entity is a propylamine H1 histamine receptor inverse agonist; the maleate counterion confers high aqueous solubility and allows direct formulation into aqueous solution dosage forms. The veterinary-grade designation is not a single pharmacopoeial monolith: the material is controlled against the relevant chlorphenamine maleate monograph for assay, identification, related substances, loss on drying, residue on ignition, residual solvents, and elemental impurities, with additional endotoxin and particle-size specifications appended for injection, premix, and low-dose solid oral presentations. Supplier-specific model designations typically correspond to these appended controls rather than to a change in the active chemical identity. When procurement requires a specific model, the request should specify end-use parameters such as “micronized, endotoxin-controlled, injection-grade chlorphenamine maleate” or “granular, low-dust premix grade,” because compendial grade alone does not ensure fitness for direct compression or aseptic filtration. The API is intended for incorporation into tablets, injections, capsules, powders, granules, premix, and solutions; it is not intended for direct administration in undiluted form.
The core specification profile for compendial chlorphenamine maleate includes assay, identity, loss on drying, residue on ignition, related substances, residual solvents, and elemental impurities. The limits shown in the table are the standard monograph-aligned acceptance values when not superseded by a supplier’s internal specification. For injection-grade material, bacterial endotoxin, sterility of the finished dosage form, and particulate matter are not solely API properties but must be considered during formulation. The API itself cannot be labeled sterile unless it is supplied as a sterile powder with a sterility claim supported by USP <71> / Ph. Eur. 2.6.1.
| Control parameter | Acceptance criterion | Method / standard |
|---|---|---|
| Assay as C16H19ClN2·C4H4O4, dried basis | 98.0%–102.0% | Liquid chromatography, relevant pharmacopoeia |
| Loss on drying | ≤0.5% | Ph. Eur. 2.2.32 / USP <731> |
| Residue on ignition / sulphated ash | ≤0.1% | Ph. Eur. 2.4.14 / USP <281> |
| Residual solvents | ICH Q3C Class 2/3 limits | USP <467> / Ph. Eur. 2.4.24 |
| Elemental impurities | Class 1 and 2A limits | USP <232>/<233> / Ph. Eur. 2.4.20 |
| Bacterial endotoxins, injection-grade | Derived from maximum dose and route | USP <85> / Ph. Eur. 2.6.14 |
| Particle size, if model specifies | D50/D90 per supplier CoA | Laser diffraction ISO 13320-1 |
In direct compression formulations, the critical API attributes are particle size distribution, bulk density, and flow function character. A micronized grade with D90 ≤ 75 µm and D50 ≤ 25 µm can support content uniformity when processed through a suitably validated direct-compression blend; however, these values are vendor-lot dependent and must be confirmed by laser diffraction according to ISO 13320-1. Tablet dosage units must meet USP <905> with acceptance value ≤15. If the blend shows a Carr index above 25 under USP <1174>, direct compression may require glidant adjustment or a change to wet granulation. In wet granulation, chlorphenamine maleate’s high aqueous solubility can generate a sticky granule when an aqueous binder is applied at high water addition; therefore, binder solution application is typically staged, and the wet mass is dried to a moisture endpoint consistent with the formulation, commonly 1.0%–2.5% loss on drying in the granule. Low-shear tumble blending and fluid-bed drying operations reduce overgranulation risk compared with intensive high-shear mixers. At production scale, blending time should be validated, because excessive blending of low-dose direct-compression formulas can cause segregation due to particle size mismatches between API and excipients. For capsules, the same granulation or direct blend may be filled on dosator or tamping-pin machines; USP <711> dissolution and USP <905> uniformity are the release controls. The API does not contribute lubricant function, so magnesium stearate concentration is typically held at or below 0.5% w/w to avoid dissolution retardation.
Chlorphenamine maleate injection solutions are formulated in Water for Injection, typically buffered to a mildly acidic pH because the drug is a weak base with pKa approximately 9.2. At pH values above 7.0, the unionized free base fraction increases; the solubility advantage provided by maleate decreases, and precipitation risk must be evaluated under the final formulation pH, tonicity, and fill. Stainless-steel preparation vessels with jacketed temperature control at 20–25°C during compounding reduce local pH excursions. The bulk solution is filtered through a validated 0.22 µm sterilizing-grade membrane; compatibility with the selected PES or PVDF membrane should be demonstrated by filter challenge and adsorption studies because published data for chlorphenamine maleate filter adsorption is limited. Filling is performed aseptically after terminal sterilization or on an aseptic line under isolator control. Finished injections are controlled for particulate matter by USP <788>, bacterial endotoxin by USP <85>, sterility by USP <71>, and visible particles. If the formulation is heat-stable, terminal sterilization at 121°C for 15 minutes may be used only after confirming assay and related substances; for light-sensitive formulations, light-resistant packaging is required. The limiting factor for injection-grade API is not assay but the introduction of endotoxin and particulate matter that cannot be removed downstream by the dosage-form manufacturer.
For oral powders, granules, and reconstitutable dry syrups, the API is either dry-blended with a diluent such as lactose monohydrate or mannitol in a bin blender, or granulated and then dried. The primary stability risk is hydrolytic degradation of the active in the presence of free water; package desiccant and controlled moisture vapor transmission rate are used. Oral solution formulations are adjusted to pH 4.5–5.5 and often contain a buffer system; if the pH drifts upward, the concentration of unionized base can increase and alter solubility. Light-protected storage is used because photodegradation has been reported for chlorphenamine in dilute solution; amber containers and light-protective blister components are standard. The API grade for dry powders may require a spray-dried or compacted granule with a bulk density selected to minimize segregation; no single bulk density is legally required, but it must be justified by mixer uniformity data on the production line.
Feed-premix applications present a different set of constraints because the API is diluted into animal feed at very low concentrations. The API grade for premix should be selected for low dusting, controlled particle size, and minimal electrostatic adhesion to stainless steel mixing surfaces. The product is not added directly to the final ration; a staged geometric dilution from API to preblend to final Type B or C medicated feed is used. Horizontal ribbon mixers or drum mixers with validated mixing time and fill level are used. Mixer coefficient of variation is determined by collecting multiple thief samples and analyzing assay; production-scale mixer validation often uses CV acceptance of ≤5% in the final blend, but the applicable limit is established in the feed mill’s mixing study and must meet the regulatory authority’s feed GMP expectations. Chlorphenamine maleate, because it is a crystalline salt, can acquire static charge during dry transfer; pneumatic transfer lines should be designed with ground bonding and inert gas or low-velocity air. The difference from tablet-grade product is primarily in particle surface area and dusting propensity; injection-grade material is normally unsuitable for premix because its small particle size increases electrostatic movement and dust losses. Feed mills operating under 21 CFR 225 CGMP expectations document the type of mixer, clean-out procedure, and sequencing of ingredients to minimize carryover and cross-contamination.
The principal chemical comparator is dexchlorpheniramine maleate, the dextrorotatory enantiomer of chlorphenamine. Chlorphenamine maleate is a racemic mixture; dexchlorpheniramine maleate provides higher H1-receptor binding activity per unit mass. The formulation consequences are relevant for dose proportionality and analytical method separation: quantitative methods for racemic chlorphenamine maleate do not separate the enantiomers unless a chiral method is specified. In contrast to second-generation H1 antagonists such as cetirizine, chlorphenamine maleate has higher octanol-water partition coefficient, log P approximately 3.39, and greater CNS penetration; this does not alter the API’s compendial controls, but it does affect worker exposure control during weighing and dust containment. Cetirizine is amphoteric and may require different pH adjustment; chlorphenamine maleate is readily water-soluble with acidic pH in solution due to maleate. The table below summarizes route suitability differences across the registered presentations.
| Dosage form | Critical API attribute | Typical processing equipment | Release method / standard |
|---|---|---|---|
| Tablets | Particle size D50/D90, flow, compactibility | Rotary tablet press, high-shear granulator, fluid-bed dryer | USP <905>, USP <711> |
| Capsules | Bulk density, flow, moisture | Dosator or tamping-pin capsule filler | USP <905>, USP <711> |
| Injections | Endotoxin, particulate matter, pH, filter compatibility | Stainless-steel compounding vessel, 0.22 µm sterilizing filter, aseptic fill line | USP <71>, USP <788>, USP <85> |
| Powders / granules | Particle size, moisture, bulk density, dusting | Bin blender, ribbon blender, sachet filling line | USP <905>, loss on drying test |
| Premix | Particle size matching, electrostatic behavior, low dusting | Horizontal ribbon mixer, staged geometric dilution vessel | Mixer uniformity validation, feed GMP record |
| Solutions | pH-dependent solubility, light stability, buffer compatibility | Stainless-steel vessel, in-line filter, glass or plastic bottle line | USP <71> if sterile, otherwise stability-indicating HPLC |