| HS Code | 797396 |
| Product Name | Lobeline Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions |
| Chemical Identity | Lobeline hydrochloride (alpha-lobeline hydrochloride) |
| Cas Number | 134-63-4 (hydrochloride); 90-69-7 (free base) |
| Molecular Formula | C22H27NO2 · HCl |
| Molecular Weight | 373.92 g/mol (hydrochloride); 337.46 g/mol (free base) |
| Appearance | White or almost white crystalline powder |
| Solubility | Freely soluble in water; soluble in ethanol and chloroform |
| Assay | 98.0% to 101.0% on dried basis by HPLC |
| Storage Conditions | Store in tightly closed containers protected from light and moisture at controlled room temperature 20-25°C |
| Shelf Life | 24 months from date of manufacture when stored properly |
| Pharmacological Property | Respiratory stimulant and nicotinic acetylcholine receptor modulator |
| Veterinary Indication | Used as a respiratory stimulant and analeptic in veterinary formulations |
As an accredited Lobeline 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 sealed, light-resistant containers with tamper-evident closures, labeled for veterinary use. Net quantity: 25 kg per drum. |
| Container Loading (20′ FCL) | Loading 20' FCL of Lobeline Veterinary Grade API: palletized, securely braced sealed drums/bags, ensuring product integrity, segregation, and safe transport. |
| Shipping | Lobeline Veterinary Grade API is shipped in sealed, light-resistant containers with tamper-evident packaging. Shipments comply with strict temperature-control and transport safety regulations, with complete documentation including Certificate of Analysis and Material Safety Data Sheet. Dry, cool storage required; avoid exposure to direct sunlight and moisture during transit. |
| Storage | Store in a cool, dry, well-ventilated area at controlled room temperature, ideally 15–30°C. Keep container tightly sealed and protected from light, moisture, and humidity. Avoid contact with oxidizing agents. Ensure proper segregation per handling instructions. Maintain stock rotation and verify expiry dates before formulation. |
| Shelf Life | Shelf life is typically 24 months from manufacture when stored in original, tightly sealed containers under cool, dry, and dark conditions. |
Aseptic processing of a lobeline hydrochloride injection at 1.0 mg/mL lobeline base equivalent starts with dissolution of the API in Water for Injection at 20–25°C in a 316L stainless steel stirred vessel. The vehicle is adjusted with 0.9% w/v sodium chloride to an osmolality of 280–310 mOsm/kg and with 0.1 M hydrochloric acid or sodium hydroxide to pH 4.5–5.0 before sterile filtration. A 0.22 µm polyvinylidene fluoride membrane is preferred over nylon because the protonated alkaloid can exhibit adsorptive loss on unmodified nylon. Terminal steam sterilization at 121°C for 15 minutes should be supported by thermal challenge data; if assay loss exceeds 2.0% under this cycle, the vial-filling step is moved into a restricted access barrier system using aseptic filtration as the sole sterilization mechanism. Filling is performed on a peristaltic pump with a fill tolerance of ±3% into amber Type I glass vials sealed with bromobutyl rubber stoppers. The finished injection is tested for particulate matter per USP <788>, bacterial endotoxins per USP <85>, sterility per USP <71>, and osmolality per USP <785>. The principal operational boundary is pH: free lobeline base precipitates above pH 6.5, and the resulting turbidity is not reversible by simple agitation. In-line nitrogen or argon sparging at 0.5–1.0 L/min is applied when oxygen-sensitive degradation products are observed during forced degradation studies.
Lobeline hydrochloride is a low-dose alkaloid salt with a mean particle size commonly below 60 µm, whereas direct-compression lactose monohydrate has a D50 near 100–150 µm. This size mismatch produces segregation during bin transfer and tableting unless the API is first locked onto a carrier by ordered mixing. In a 1,000 L bin blender, the API is premixed with lactose monohydrate at 1:10 w/w for 10 minutes at 15 rpm, then diluted to 1:100 and mixed for an additional 20 minutes. The final blend contains lobeline HCl equivalent to 0.2–2.0 mg per tablet, microcrystalline cellulose at 45–65% w/w, crospovidone at 2–5% w/w, colloidal silicon dioxide at 0.5% w/w, and magnesium stearate at 0.5–1.0% w/w. Magnesium stearate is added last and blended for only 3–5 minutes because overlubrication lowers tablet tensile strength and delays disintegration. Tablets are compressed on a rotary tablet press with 9 mm round concave tooling at 8–14 kN compression force to a hardness of 5–8 kP, a thickness of 3.0–3.5 mm, and a friability below 1.0% per USP <1216>. Content uniformity follows USP <905>; an acceptance value above 15 has been associated on production-scale batches with powder layering on hopper walls, and the corrective action is a larger carrier-to-API surface coverage rather than extended total blend time. Disintegration is measured in purified water at 37±2°C and must not exceed 15 minutes per USP <701>. The finished tablets are packaged in 0.03 mm PVC/PVDC-aluminum blisters to limit moisture uptake because lobeline salts are hygroscopic above 60% RH.
| Parameter | Variant A | Variant B | Variant C |
|---|---|---|---|
| Lobeline HCl (w/w %) | 0.5 | 1.0 | 2.0 |
| Microcrystalline cellulose (w/w %) | 55.0 | 50.0 | 45.0 |
| Lactose monohydrate (w/w %) | 40.0 | 43.5 | 47.5 |
| Crospovidone (w/w %) | 3.0 | 4.0 | 4.0 |
| Colloidal silicon dioxide (w/w %) | 0.5 | 0.5 | 0.5 |
| Magnesium stearate (w/w %) | 1.0 | 1.0 | 1.0 |
| Hardness (kP) | 5.5 | 6.0 | 7.0 |
| Disintegration (min) | 8 | 10 | 12 |
For capsule-based dosing in equine practice, the veterinary compounding pharmacy usually prepares lobeline hydrochloride powders in size 2 or 3 two-piece hard gelatin capsules. The powder fill is lactose monohydrate 80M combined with the pre-weighed API in a geometric dilution sequence of 1:1, then 1:2, then 1:4 using a mortar and pestle for quantities below 100 g or a 5 L V-blender at 25 rpm for larger batches. The target fill weight is 150–250 mg per capsule, with the lobeline content adjusted to the prescribed dose rather than fixed per unit mass. Encapsulation is performed on a semi-automatic capsule machine with vibration-assisted dosing plates; weight variation is controlled within ±5% of the target fill weight. Because the formulation is non-sterile and dry, the beyond-use date assigned under USP <795> is generally 180 days when protected from moisture and light. The terminal product is a hard gelatin capsule placed in an amber screw-cap vial with desiccant silica gel canister; storage above 60% RH risks capsule shell embrittlement and API caking. For food-producing horses, compliance with 21 CFR 530.41 is evaluated before dispensing because extra-label use in feed animals carries residue and withdrawal considerations. Published efficacy data for this specific configuration is limited, and the capsule format is compounded only when a veterinarian determines that a solid oral dosage form is clinically appropriate.
Water solubility of lobeline hydrochloride allows a pump-ready oral solution to be prepared, but the free base precipitates when phosphate or carbonate buffer systems raise pH above 6.0. An oral solution for neonatal piglets and calves is therefore manufactured with a citrate buffer at pH 4.5–5.0 and a total drug concentration of 0.5–1.0 mg/mL lobeline base equivalent. Glycerin or sorbitol solution 70% is included at 10–20% w/v to increase viscosity to 8–15 mPa·s, which reduces settling in the final 100 mL amber polyethylene terephthalate bottle. Preservative efficacy is maintained with sodium benzoate 0.1% w/v and potassium sorbate 0.1% w/v; both are added to purified water at 50°C and cooled to 25°C before the API is dissolved under propeller agitation at 500 rpm. The solution is passed through a 10 µm polypropylene filter to remove undissolved components and filled with a headspace nitrogen flush of 2–3 seconds. Light exposure promotes degradation, so the bottle label must specify storage at 20–25°C and protection from direct sunlight. The terminal product is a clear, slightly viscous oral solution with pH measured by USP <791>, viscosity by USP <911>, and deliverable volume per USP <698>. Incompatible conditions include contact with alkaline cleaning residues on filling lines; a final rinse with purified water at pH 5.0–5.5 is therefore required before startup. If the target species is a food-producing animal, residue data and withdrawal intervals must be established before administration because regulatory approval for this indication is not uniform across jurisdictions.
Granules are manufactured when veterinary hospitals require a pre-weighed oral unit that can be dispersed in water or administered by gavage. A wet granulation process binds lobeline sulfate API with lactose monohydrate 200M using povidone K-30 dissolved in purified water at 5% w/w of dry granulate. The API is first dispersed in a 1:5 pre-blend with lactose in a 150 L high-shear mixer at 100 rpm chopper speed for 3 minutes. The binder solution is sprayed at 8–12 g/min in a fluid-bed granulator with inlet air temperature 50–55°C, product temperature 35–40°C, and airflow 80–120 m³/h. Drying continues until loss on drying is below 2.0% w/w; overdrying below 0.5% w/w increases friable fines and segregation. The dried granules are milled through a 1,000 µm screen and blended with 0.25% w/w colloidal silicon dioxide in a 100 L bin blender. The resulting granules have bulk density 0.45–0.60 g/mL, tapped density 0.55–0.75 g/mL, and Carr compressibility index below 20% per USP <616>. Uniformity of dosage units on the filled granules follows USP <905>, with acceptance value not exceeding 15. The terminal product is an amber high-density polyethylene container with a heat-sealed foil liner, stored at 20–25°C and desiccant-protected. Granule production is preferred over dry blending when the API content is below 0.5% w/w because direct blend homogeneity becomes equipment-dependent on production-scale machines. One observed failure mode in twin-shell blenders is dead-spot accumulation at the intensifier bar; the corrective action is to operate at 25 rpm for 20 minutes after the final lubricant addition rather than using an extended pre-blend cycle.
Dry powder for in-house veterinary compounding is the most conservative format when the prescriber must vary the dose across a wide body weight range. The API is dispensed as a triturate at 0.2–5.0% w/w with lactose monohydrate 80M as the diluent. Geometric dilution is mandatory: the initial 1:1 API-lactose trituration is passed through a 150 µm stainless steel sieve, then the 1:2 and 1:4 dilutions are each mixed for 3 minutes in a porcelain mortar or a planetary mixer at 50 rpm. Homogeneity is verified by withdrawing 10 samples from different locations and assaying by a stability-indicating liquid chromatographic method; the acceptance range is 90.0–110.0% label claim with relative standard deviation not more than 5.0%. The powder is filled into low-density polyethylene powder jars with a screw cap and a heat-sealed induction liner. A silica gel desiccant carton is inserted if the ambient relative humidity exceeds 60% RH. Assigned beyond-use date under USP <795> is 180 days for the dry non-aqueous formulation. The powder format is not suitable for aqueous reconstitution on the pharmacy floor unless the final solution is used immediately, because unpreserved liquids carry a beyond-use date of 14 days under refrigerated conditions per USP <795> and lobeline base may precipitate if the vehicle pH is not controlled.
Oral premixes are prepared only as non-sterile dry dilutions for individual animal administration, not as commercial medicated feed articles. The regulatory boundary is material: many jurisdictions do not list lobeline as an authorized feed additive, and a commercial feed premix would require a marketing authorization under Regulation (EU) 2019/4 or applicable national feed legislation. For a single-animal premix, lobeline hydrochloride is diluted at 0.1–1.0% w/w onto a carrier composed of lactose monohydrate 200M and pregelatinized starch 5–10% w/w. Mixing is performed in a 50 kg ribbon blender at 25 rpm for 12–15 minutes after a 1:10 manual pre-blend has been screened through a 500 µm sieve. The product is filled into single-dose sachets or aluminum-laminated pouches. Each sachet is labeled with the quantitative composition, a batch number, and the target animal identity because the product is not intended for group administration. Residual solvent limits follow VICH GL18, and the API must be accompanied by a certificate of analysis showing identity, assay, related substances, residual solvents, and microbial limits. The premix is mixed with a small amount of feed immediately before administration; prolonged storage of medicated feed exceeds the compounding-use condition and may trigger feed-safety obligations. For food-producing species, withdrawal periods cannot be established from this format without residue studies.
| Dosage Form | Standard/Regulation | Critical Check | Limit or Method |
|---|---|---|---|
| Sterile injection | USP <71>, USP <85>, USP <788> | Sterility, endotoxin, subvisible particles | No growth; endotoxin per monograph; particle counts per chapter |
| Tablet | USP <905>, USP <701>, USP <1216> | Content uniformity, disintegration, friability | AV ≤ 15; < 15 min; < 1.0% |
| Capsule powder | USP <795> | Compounded dry solid beyond-use date | 180 days, dry, light-protected |
| Oral solution | USP <791>, USP <698>, USP <51> | pH, deliverable volume, preservative efficacy | pH 4.5–5.0; volume per label claim; preservative criteria per chapter |
| Granules | USP <616>, USP <905> | Compressibility, content uniformity | Carr index < 20%; AV ≤ 15 |
| Premix | VICH GL18, Regulation (EU) 2019/4, 21 CFR 530.41 | Residual solvents, feed-safety status, compounding authorization | Class 1 and Class 2 solvent limits per VICH GL18; individual animal use only |
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Lobeline Veterinary Grade API is supplied as the hydrochloride salt of the alkaloid lobeline, C22H27NO2·HCl, with a relative molecular mass of 373.92 g/mol. The product is assigned the model code LVG-API-HCl-2401 for traceability in batch records and customer documentation. The standard grade is a non-sterile crystalline powder for further pharmaceutical processing. A micronized variant, LVG-API-HCl-2401M, is controlled to a particle-size D90 ≤ 75 μm, while the direct-compression variant, LVG-API-HCl-2401C, is controlled to a particle-size D90 ≤ 150 μm. A low-bioburden variant, LVG-API-HCl-2401S, is intended for sterile solution compounding after downstream membrane filtration or terminal steam sterilization; this variant is not sterile as supplied.
The API is released against a specification that includes assay by HPLC with external reference standardization, identity by infrared spectroscopy and retention-time matching, related substances by reversed-phase HPLC area normalization, water content by Karl Fischer titration, residual solvents by headspace gas chromatography, and particle-size distribution by laser diffraction. The release window for assay is 98.0–102.0% w/w on the dried basis. Total related substances are controlled to ≤ 1.0% w/w, with any unspecified individual impurity controlled to ≤ 0.5% w/w. These values are internal release criteria for the veterinary-grade API and are not a substitute for regulatory acceptance limits assigned to a finished veterinary medicinal product in a specific jurisdiction.
The following release parameters are applied to the non-sterile standard grade. For the low-bioburden variant, the endotoxin limit is added only where an injectable dosage form is intended.
| Attribute | Method / Standard | Release Criterion |
|---|---|---|
| Appearance | Visual inspection | White to off-white crystalline powder |
| Assay, dried basis | HPLC external standard / Ph. Eur. 2.2.29 | 98.0–102.0% w/w |
| Water content | Karl Fischer / Ph. Eur. 2.5.12 or USP <921> | ≤ 0.5% w/w |
| Related substances, any individual | Reversed-phase HPLC area normalization | ≤ 0.5% w/w |
| Related substances, total | Reversed-phase HPLC area normalization | ≤ 1.0% w/w |
| Residual solvents | HS-GC / USP <467> / Ph. Eur. 2.4.24 | ICH Q3C Class 3 limits |
| Elemental impurities | ICP-MS / USP <233> / Ph. Eur. 2.2.58 | ICH Q3D limits as assigned to the intended dosage form |
| Particle size D90, micronized variant | Laser diffraction / ISO 13320:2020 | ≤ 75 μm |
| Particle size D90, direct-compression variant | Laser diffraction / ISO 13320:2020 | ≤ 150 μm |
| Bulk density | USP <616> Method I / Ph. Eur. 2.9.34 | 0.30–0.60 g/mL |
| Microbial enumeration | Ph. Eur. 2.6.12 / USP <61>, USP <62> | TAMC ≤ 10³ CFU/g; TYMC ≤ 10² CFU/g; Escherichia coli absent |
| Bacterial endotoxins, low-bioburden variant | Ph. Eur. 2.6.14 / USP <85> | ≤ 0.50 EU/mg where specified |
Storage is specified at 15–25°C in tightly closed, light-resistant containers. Handling should occur in a dry environment; the powder is hygroscopic above 60% relative humidity, and pre-drying may be required if moisture uptake exceeds 0.5% w/w. Because the material is an alkaloid hydrochloride, it may generate electrostatic charge during micronization. Equipment should be grounded, and inert-gas blanketing may be used where dust exposure or deflagration risk is identified. The product is not classified as sterile, depyrogenated, or ready for direct intravenous administration.
Direct compression of the LVG-API-HCl-2401C variant is feasible only when particle-size distribution and bulk density are controlled. The D90 ≤ 150 μm fraction reduces segregation in low-dose formulations, but the powder remains susceptible to agglomeration if stored above 60% relative humidity. In a low-shear tumble blender with a usable capacity of 600 L, geometric dilution is required when the drug load is below 1.0% w/w. Each dilution step should not exceed a 1:5 ratio by mass to prevent localized drug accumulation. The blend is sampled at 20 discrete positions, and content uniformity is considered acceptable when the relative standard deviation is ≤ 5.0%. Published formulation data for lobeline hydrochloride tablets are limited; these parameters reflect low-dose alkaloid hydrochloride tableting practice and require product-specific confirmation.
For tablet compression, a rotary tablet press with a main compression force of 8–18 kN may be used depending on tablet size and tooling. Magnesium stearate is added at 0.25–0.75% w/w after the main blending step to avoid over-lubrication and delayed disintegration. Colloidal silicon dioxide at 0.5–1.0% w/w improves flow for the micronized grade. If final tablet hardness is below 3 kp or above 12 kp, dissolution may become variable; dissolution method development should follow USP <711> or Ph. Eur. 2.9.3. Low-dose tablet manufacture also requires matching the API and excipient particle sizes to avoid content-uniformity failure under USP <905> or Ph. Eur. 2.9.40.
Capsule filling is performed with a dosator or tamping-pin capsule filler. The direct-compression variant may be filled as a powder blend into hard gelatin capsules when powder flow is maintained at a Carr index below 25. For the micronized variant, dry granulation by slugging or roller compaction is preferred to avoid moisture-induced hydrolysis. Roller compaction with a roll force of 2–5 kN/cm and a gap of 1.0–2.0 mm produces granules with a bulk density of 0.45–0.60 g/mL. After compaction, the granules are passed through a 0.8 mm sieve and blended with extragranular disintegrant. This process reduces dust generation and improves encapsulation mass consistency.
When a granulated product is required for oral powders or sachets, fluid-bed granulation is used with a binder solution of polyvinylpyrrolidone in isopropyl alcohol. The inlet air temperature is maintained at 35–45°C, and the product temperature is kept below 30°C to reduce degradation risk. The drying endpoint is set to 1.0–2.0% w/w moisture for granules; overdrying below 0.5% w/w can increase static charge. For oral powders, the final particle-size distribution is controlled to 180–500 μm to balance flow and palatability in monogastric species.
In injectable solution manufacture, the LVG-API-HCl-2401S variant is dissolved in Water for Injection under nitrogen purging. The solution is adjusted to pH 4.0–5.5 with dilute hydrochloric acid or sodium hydroxide; alkaloidal salts may precipitate as pH approaches the free-base pKa, so pH control is a critical process parameter. The final fill is sterilized by membrane filtration through a 0.22 μm polyvinylidene fluoride or polyethersulfone membrane. If terminal steam sterilization at 121°C for 15 min is used, forced-degradation data in the actual container-closure system must confirm that assay loss remains within the approved stability specification. The solution should be tested for bacterial endotoxins according to Ph. Eur. 2.6.14 or USP <85>. The standard grade is not endotoxin-controlled, and the low-bioburden grade is not a substitute for depyrogenation of all process contact surfaces and excipients.
For oral solutions, purified water with a preservative such as sodium benzoate or potassium sorbate is used. The hydrochloride salt is freely soluble in aqueous media; however, published quantitative solubility data for lobeline hydrochloride are limited, and the maximum stable solution strength should be determined at the intended storage temperature. The solution is filled under nitrogen into amber glass or light-resistant plastic bottles. A pH below 5.5 reduces oxidation and microbial proliferation, but pH below 3.0 may cause irritation in some target species. The final formulation pH should remain within the registered product specification.
Premix manufacture uses stepwise geometric dilution of the API into a carrier such as lactose monohydrate, wheat middlings, or ground corn cob. The premix intermediate is typically formulated at 1:10 or 1:100 dilution before final feed mixing. With the LVG-API-HCl-2401M variant, the D90 ≤ 75 μm fraction reduces segregation after blending, but it also increases dust generation. Dust extraction at the premix weighed area should achieve an air velocity of 0.5 m/s across the open powder surface, and operator exposure should be monitored by air sampling. Mixing time is established by a blend uniformity study; samples are taken from 20 points across the mixer after 10–15 min in a 1,000 kg ribbon mixer, with an acceptance criterion of RSD ≤ 5.0%. If the carrier has a broad particle-size range, a two-stage mixing step is recommended to avoid sifting segregation during transfer to the final feed.
Medicated feed stability should be verified in the finished feed matrix. Published data for lobeline stability in typical feed matrices are limited; therefore, a site-specific use-period study under the intended storage conditions is required. The premix should not be combined with strongly alkaline mineral mixes or high-moisture fermented feed because the free base may be released and partition unevenly. For food-producing animals, the withdrawal period and marker-residue requirements are assigned in the marketing authorization and are outside the API release specification.
The product is a single-entity hydrochloride salt, not a standardized botanical extract. This distinction matters in batch-to-batch reproducibility. Crude Lobelia inflata material varies in total alkaloid content and may contain pigments, tannins, and insoluble plant fiber; the veterinary-grade API is isolated and crystallized so that HPLC assay and related substances can be measured directly. The hydrochloride salt is selected because it has higher aqueous solubility than the free base, enabling solution and injection processing without organic cosolvent. A free base is unsuitable for aqueous formulations without salification.
Compared with reagent-grade lobeline alkaloid, the veterinary-grade product is released with a certificate of analysis that includes residual solvent, microbial, and particle-size data. The product is manufactured under active substance GMP expectations aligned with EU GMP Part II and applicable VICH quality guidance. It is not approved as a finished drug in any jurisdiction. The user is responsible for applying the API within a licensed or legally permitted veterinary compounded product. If a compendial monograph for lobeline hydrochloride is not available in the target jurisdiction, the API should be qualified by the finished product applicant using validated in-house methods.
The operational boundaries of this API include moisture sensitivity above 60% RH, incompatibility with strong oxidizing agents, and potential precipitation of the free base at pH above 7.0. Alkaline aqueous processing should be avoided unless deliberate salification from the free base is part of the formulation design. High-shear wet granulation with water should be replaced with solvent-based granulation or dry granulation when the process cannot maintain residual water below 0.5% w/w. The material is not screened as a sterile API; injectable applications require sterile filtration or terminal sterilization. The material is not a feed additive by itself; it is an active substance for further processing in registered or legally permitted veterinary medicines.
Avoid mixing the dry powder with strong alkalis, oxidizing agents, or reducing agents in the same premix stage. If sulfite antioxidants are proposed for injection stability, bench-scale compatibility should be performed before scale-up because published data on lobeline-sulfite adduct formation are limited.