| HS Code | 322474 |
| Product Name | Maxingshigan Tablets Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions |
| Api Category | Veterinary Grade Active Pharmaceutical Ingredient from Traditional Chinese Medicine formula |
| Physical Form | Fine dry powder or semi-finished material for further formulation |
| Active Components | Ephedra, bitter apricot seed, gypsum, and licorice extracts with standardized marker compounds |
| Primary Indications | Relief of cough, wheezing, dyspnea, lung-heat respiratory infections, bronchitis, and pneumonia in animals |
| Target Species | Poultry, swine, cattle, sheep, goats, rabbits, and other veterinary animals |
| Supported Dosage Forms | Tablets, injections, capsules, powders, granules, premix, and oral solutions |
| Solubility | Partially soluble in water with dispersibility dependent on excipient blend |
| Storage Conditions | Store in tightly sealed containers in a cool, dry, dark place; protect from moisture and heat |
| Shelf Life | 24 months when stored under recommended conditions |
| Packaging | Sealed double-layer polyethylene bags or sealed drums, commonly 1 kg or 25 kg net weight |
| Regulatory Status | Suitable as veterinary-grade API and intended for use in compliance with applicable veterinary drug pharmacopoeia and GMP standards |
As an accredited Maxingshigan Tablets 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.
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Direct-compression tableting of a standardized Maxingshigan dry extract for oral administration in growing pigs is bounded by the powder’s rheological response when calcium sulfate dihydrate particles from the gypsum fraction interact with hygroscopic glycyrrhizic acid during blending at relative humidity above 55%. Production-scale rotary presses with 12–16 stations routinely record ejection force excursions if the extract is not pre-dried to moisture below 5.0%; a fluid-bed dryer set to inlet air 60°C and exhaust air 35–40°C is generally specified before weigh-up. The loss on drying is verified with a halogen moisture analyzer at 105°C, because free moisture above the limit increases die-wall friction and causes picking on embossed punch faces.
A typical direct-compression formulation for a 300 mg target tablet weight contains 25–40 wt% spray-dried Maxingshigan extract, 35–50 wt% microcrystalline cellulose PH-102, 10–20 wt% lactose monohydrate, 2–4 wt% croscarmellose sodium, 0.5–1.0 wt% magnesium stearate, and 1–2 wt% colloidal silicon dioxide. Sodium starch glycolate is substituted for croscarmellose sodium when rapid disintegration is required in porcine gastric fluid at pH 2.5–4.5. After final blending in a 600 L bin blender at 12 rpm for 20–30 min, samples taken from 10 positions are analyzed by HPLC for ephedrine alkaloid content; acceptance is set at 95–105% of label claim with RSD ≤ 5.0%. In-process tablet hardness is maintained at 6–8 kp, friability ≤ 1.0%, and disintegration time in purified water at 37±2°C is controlled to not more than 15 min according to USP <701>.
Wet granulation becomes necessary when the direct-compression API particle size distribution contains more than 30% fines caused by repeated milling, because segregation in the tablet press feed frame leads to weight variation exceeding ±3% and corresponding potency drift in the finished tablet. A high-shear mixer-granulator with an impeller speed of 200–300 rpm, chopper speed of 1500–2500 rpm, and bowl temperature 20–25°C is charged with extract, microcrystalline cellulose, and a portion of crospovidone; purified water containing povidone K30 at 3–5% w/w is sprayed at 2–3 kg/min until the torque endpoint reaches 20–25 Nm on a 65 L vertical granulator.
The wet mass is discharged, wet-milled through a 2.0 mm screen, and dried in a fluid-bed dryer to a final moisture of 1.5–2.5%. Dry granule sieving retains 40–60% on 0.25 mm and ≤ 10% below 0.15 mm. These fractions are blended with extra-granular disintegrant after granulation because intra-granular crospovidone at 2% combined with extra-granular crospovidone at 3% improves disintegration without retarding dissolution of amygdalin. For piglet oral granules, the finished product is filled into foil-lined sachets at 100 g or 500 g; uniformity of mass follows EP 2.9.5, and marker assay by HPLC with UV detection at 210 nm is performed against ephedrine hydrochloride reference standard.
Manufacture of an injectable solution from a multi-component botanical extract requires a solvent system that differs fundamentally from oral-grade aqueous dispersion. The extract obtained by water decoction and ethanol precipitation is not directly injectable; it must be subjected to ultrafiltration through a 10 kDa polyethersulfone membrane followed by terminal sterilization at 121°C for 15 min only after compatibility of marker stability is demonstrated. Published data for this specific configuration is limited. The presence of calcium sulfate and high-molecular-weight licorice polysaccharides can produce visible particles above USP <788> limits; pre-filtration through 0.45 µm polypropylene cartridges is required to prevent rapid blocking of a subsequent 0.22 µm sterilizing-grade filter. Bacterial endotoxin control is performed according to USP <85>; because the extraction process can introduce endotoxin loads from botanical starting materials, depyrogenation by activated carbon or ion-exchange resin is validated before membrane processing. Injectable dosage forms based on this botanical extract have narrow regulatory acceptance in multiple jurisdictions due to the variability of ephedra alkaloid content and the anaphylactic potential of high-molecular-weight polysaccharides; any parenteral application requires batch-wise marker quantification and safety data that exceed oral-grade requirements.
Soluble powder production from Maxingshigan extract is constrained by the limited cold-water solubility of resinous ephedra fractions and the gelling tendency of pectin-like licorice polysaccharides. To achieve a visually clear or opalescent solution at a use rate of 1–2 g/L in drinking water, the extract is often co-processed with anhydrous lactose or mannitol in a hammer mill fitted with a 0.5 mm screen. A spray-dried carrier system containing 20–30% extract and 70–80% maltodextrin DE 10–15 improves wetting; reconstitution testing at 25°C in standard hard water with hardness 340 mg/L CaCO3 indicates complete dispersion within 5 min under mechanical stirring at 100 rpm. The resulting solution is drawn through a 50 µm in-line filter in automatic dosing equipment to prevent nozzle fouling.
Stock solutions for drinking water medication are diluted 1:50 to 1:100 by proportioner pumps. Compatibility with acidifiers such as citric acid at 0.1–0.2% is generally acceptable when solution pH remains between 4.0 and 6.5; alkaline hypochlorite sanitizers should not be introduced simultaneously because ephedrine alkaloids are oxidized to inactive quinoid products and glycyrrhizic acid may precipitate as the free acid below pH 3.0. The powder is packaged in aluminum-laminated pouches with desiccant to keep moisture below 3.0% and is used within 24 h after reconstitution in farm water lines.
| Parameter | Direct-compression tablet | High-shear granule | Soluble powder |
|---|---|---|---|
| API loading | 25–40 wt% spray-dried extract | 60–75 wt% dry granule basis | 20–30 wt% extract on maltodextrin carrier |
| Primary moisture target | ≤5.0% LOD | 1.5–2.5% LOD | ≤3.0% LOD |
| Disintegration or dispersion criticality | Croscarmellose sodium 2–4% | Intra- and extra-granular crospovidone 2% + 3% | Dispersion at 100 rpm in ≤5 min |
| Process control | Hardness 6–8 kp, friability ≤ 1.0% | Granule sieve retention 40–60% on 0.25 mm | Reconstituted pH 4.0–6.5 |
| Analytical marker | Ephedrine alkaloid HPLC 95–105% label claim | Ephedrine HCl HPLC at 210 nm | Amygdalin and ephedrine marker dispersion in hard water |
At feed mill scale, the inclusion of a Maxingshigan premix into complete swine or poultry feed is usually executed through a 2–5% carrier premix rather than direct API addition. Ribbon mixers with working capacity 1–2 tonnes and mixing time 8–12 min achieve a coefficient of variation for ephedrine marker below 10% when the API is pre-blended with rice husk powder or calcium carbonate. Pelletizing at conditioner discharge temperature 75–80°C with steam pressure 2.0–2.5 bar is the upper validated boundary for most batches; higher temperatures accelerate loss of volatile ephedrine and reduce marker assay below label claim. Post-pellet liquid application of a protected extract onto cooled pellets at ≤40°C may be used when thermal degradation is a concern. After a medicated batch, a validated flush with ground corn at 5–10% of mixer capacity is run; carryover acceptance is usually set at ≤ 0.5% of the previous batch.
Compatibility with free calcium carbonate and magnesium oxide in mineral premixes requires adjustment of the extract addition method because direct contact between acidic glycyrrhizic acid and alkaline mineral carriers reduces ephedrine marker recovery after 4 weeks at 40°C/75% RH. In top-dressing granules for cattle or buffalo, the extract is often protected by a 5–10% w/w coating of hydrogenated vegetable oil applied in a bottom-spray fluid-bed coater at product temperature 35–40°C and atomizing air pressure 1.5–2.0 bar. The granule core is first built by rotor granulation with microcrystalline cellulose spheres of diameter 0.8–1.2 mm; the extract is layered as a 15–25% w/w suspension containing 5% povidone K30 as binder. Dosing through a top-dressing applicator calibrated at 10–20 g per animal per day requires granule density 0.85–1.05 g/cm³ to prevent segregation in the hopper; a sieve cut of 0.5–1.6 mm is maintained by mechanical classification.
Because maximal marker retention in capsules requires filling under low-humidity conditions, hard gelatin capsule production for companion animals is usually scheduled when ambient relative humidity remains below 40%. An automatic tamping-pin capsule filler with size 1 or 0 shells achieves a fill weight of 300–500 mg when the extract is granulated to a Hausner ratio below 1.25. At moisture below 12%, gelatin shells can become brittle and split, so shell conditioning at 45–55% RH for 4–6 h is used for powders with low moisture content. HPMC capsules are preferred when the extract contains residual aldehyde impurities that can cross-link gelatin over time. Dissolution testing per USP <711> Apparatus II at 50 rpm in 900 mL of 0.1 N hydrochloric acid with pepsin is specified for batch release, and the finished capsules are inspected for leakage through vacuum dye testing at 0.6 bar negative pressure.
| Verification point | Standard or reference | Application |
|---|---|---|
| Uniformity of dosage units | USP <905> | tablets, capsules |
| Disintegration | USP <701> | tablets |
| Bacterial endotoxins | USP <85> | injectable solution |
| Uniformity of mass of single-dose preparations | EP 2.9.5 | granules, powders |
| Extractable volume and particulate matter | USP <788> | injectable solution |
| Residual solvents in botanical extracts | VICH GL18, EP 5.4 | all extraction-derived API |
| Heavy metals | EP 2.4.8 | API |
| Veterinary medicinal product placing on market | EU 2019/6 | finished dosage forms |
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Maxingshigan Tablets Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions is a multi-marker botanical active pharmaceutical intermediate intended for further manufacture rather than direct administration to animals. The material is prepared from a fixed-ratio botanical formula containing Ephedra Herba, Gypsum Fibrosum, Armeniacae Semen Amarum, and Glycyrrhizae Radix et Rhizoma. Identity and assay markers therefore include ephedrine hydrochloride, pseudoephedrine hydrochloride, amygdalin, glycyrrhizic acid, and calcium sulfate dihydrate. No single harmonized monograph exists under the exact product name; the receiving jurisdiction establishes acceptance criteria through the finished-product applicant’s registration file. The model designation is therefore a grade matrix rather than a single model number. That matrix separates spray-dried extract for tablets, purified clarified extract for injections, sieved powder for capsules, milled material for granules, flowable dry-mix powder for premix use, and dissolved or suspended extract for oral solutions.
Specifications are batch-specific and dosage-form-specific. A tablet-grade API may be released with particle-size distribution measured by laser diffraction according to ISO 13320, while an injection-grade API is released with additional bacterial endotoxin and bioburden limits. Marker content alone is not sufficient for release. The supplier certificate of analysis typically includes total ephedrine alkaloids, pseudoephedrine content, amygdalin, glycyrrhizic acid, loss on drying, residue on ignition, heavy metals, pesticide residues, residual solvents, total plate count, yeast and mold, and specified organisms. Quantification is performed by HPLC or UHPLC with photodiode array detection because no single ultraviolet-visible absorbance method separates all marker classes. The lower marker concentration of Ephedra Herba in ChP 2020 is 0.8% combined ephedrine hydrochloride and pseudoephedrine hydrochloride; the final extract ratio may concentrate these alkaloids but must not concentrate heavy metals or pesticide residues beyond the registration limit.
| Parameter | Method or standard | Dosage-form-dependent note |
|---|---|---|
| Marker identity | HPTLC or HPLC-PDA; component monographs, ChP 2020 | Required for every grade |
| Total ephedrine alkaloids | HPLC; ChP 2020 Ephedra Herba monograph | Raw-herb lower bound 0.8%; concentrated according to extraction ratio |
| Amygdalin | HPLC-PDA | Set from formula ratio and extraction solvent |
| Glycyrrhizic acid | HPLC | Used as a ratio fingerprint marker |
| Elemental impurities | ICP-MS; USP <232>/<233> | Limits defined by target species and route |
| Bacterial endotoxin | LAL; USP <85>; Ph. Eur. 2.6.14 | Injection grade only; dose-based limit |
| Microbial enumeration | USP <2021>/<2022>/<62> | Non-sterile forms; pharmacopeial sample sizes apply |
| Particle size | Laser diffraction, ISO 13320 | D90 set by dry-mix, tableting, or filling need |
The use of this API is confined to further pharmaceutical processing. It is blended into tablet formulations by wet granulation or direct compression, filled into hard capsules, dispersed in dry premixes for feed, converted into granules by fluid-bed processing, or dissolved or suspended in solutions. Each route applies different pressure, heat, and shear histories. The tablet route requires compression at forces that do not induce lamination of the botanical extract. The injectable route requires a sterilizing filtration or terminal sterilization decision that tablet-grade material cannot satisfy. The premix route requires homogeneity testing at low inclusion. In all cases, the API is not a finished product and cannot be used as a replacement for a registered veterinary medicinal product. Each finished product must justify target species, dose, route, and withdrawal period through the applicable veterinary drug authority.
Matching marker content does not indicate interchangeability across dosage forms. Tablet-grade powder routinely contains calcium sulfate, insoluble cell wall fragments, and small quantities of flow-enhancing materials that are not acceptable in a clear injectable solution. A sterile filtration train with a 0.45 µm prefilter and a 0.22 µm sterilizing membrane will foul if calcium sulfate concentration exceeds the solution saturation limit or if the extract has a high colloid burden. Injection-grade API is therefore produced under a separate purification strategy, commonly involving centrifugation, ultrafiltration, or membrane clarification. The production area must meet EU GMP Annex 1 and ISO 14644-1. Endotoxin control is dose-based; passage through a 0.22 µm filter removes bacteria but not endotoxin. The maximum allowable endotoxin for an injectable is calculated from the intended dose volume and the target species sensitivity, and it cannot be copied from a tablet-grade certificate of analysis. The same concern applies to injection-grade stability: if the API is lyophilized, the residual moisture after freeze-drying must be low enough to prevent glass transition collapse and marker degradation, but the specific moisture target is product-dependent. Published data for this exact botanical injection-grade API is limited; each manufacturer must generate filter-flux, endotoxin-reduction, and stability data before release of a sterile finished product.
For oral powder and premix manufacturing, the dominant production bottleneck is segregation rather than solubility. A spray-dried multicomponent extract with a tapped bulk density below 0.40 g/cm³ can stratify in ribbon blenders, especially if the mixer is filled beyond its validated working volume. An angle of repose greater than 40° indicates that glidant addition is necessary before filling or dosing. Content uniformity testing on finished premix is mandatory when the API inclusion rate is below 1.0% by weight. Sampling from at least 10 locations per batch and HPLC marker assay provide evidence that the dry-mix form is suitable for field dilution. Increasing mixing time beyond the qualified range does not improve homogeneity; it may raise the powder-bed temperature and change the recovery of heat-sensitive markers. On production lines with high ambient humidity, the extract surface adsorbs moisture, and the powder transitions from free-flowing to cohesive at a threshold that must be established for the specific extract ratio. Pre-drying at low temperature is required when relative humidity exceeds 60%, and opened containers should be resealed under dry conditions to avoid batch-to-batch flow variation.
| Dosage form | Equipment control point | Most common process failure | Control method |
|---|---|---|---|
| Tablets | Rotary press precompression force | Lamination from elastic recovery of botanical extract | Add precompression; control granule moisture |
| Capsules | Dosing disc and tamping pin speed | Poor flow and caking | Glidant addition; flow testing per USP <1216> |
| Powders and premixes | Ribbon blender fill level and mixing time | Marker segregation, poor content uniformity | Multi-point sampling; USP <905> or ChP uniformity method |
| Granules | Fluid-bed inlet airflow and spray rate | Overwetting and filter clogging | Monitor exhaust temperature; sieve analysis |
| Solutions | Vessel mixing and filtration | Precipitation of calcium sulfate | Clarify before filter; adjust pH strategy |
| Injections | Membrane cascade to 0.22 µm | Filter fouling and endotoxin breakthrough | Prefiltration at 0.45 µm; validated reduction factor |
Dry-mixing of the unprocessed extract is not equivalent to wet granulation. In wet granulation, the polysaccharides present in licorice root function as a natural binder and can reduce the amount of external binder needed. However, the same polysaccharides extend disintegration time in tablet forms. A disintegration limit in the finished product must be set according to USP <701> or the applicable ChP method. The calcium sulfate component acts as a filler and hardening agent in tablets, which is advantageous for hardness but creates a precipitation risk in solutions. If a clear oral solution is required, calcium sulfate must be removed or reduced, or the formulation must be designated as a suspension. For granules, fluid-bed spray rate and inlet air temperature must be validated because the extract is heat-sensitive; a high intake temperature can reduce marker recovery, but the threshold must be determined by forced degradation. In capsule filling, the API powder is combined with diluents and glidants; flow characterization follows USP <1216> and the filled capsule is tested for weight variation or uniformity of dosage units according to USP <905>.
Rotary tablet presses with a precompression stage are used to avoid lamination. The botanical extract exhibits elastic recovery after compaction; if precompression is missing, crown cracking appears on the tablet surface. Compression force and turret speed are set to maintain tablet hardness while ensuring disintegration. The tablet-grade API may contain residual moisture; if the moisture content is too low, the tablets undergo capping; if too high, sticking occurs. Batch-to-batch variation in loss on drying should be controlled within a range established by the manufacturer, and incoming API should be re-tested after storage above 60% relative humidity.
The product differs from synthetic respiratory agents such as ketoprofen, carprofen, bromhexine hydrochloride, or amoxicillin in that it has no single pharmacopeial potency unit. A synthetic API is one molecular entity with a single melting point, a single assay wavelength, and a defined impurity profile. This API has a minimum of four marker classes and requires a chromatographic fingerprint. Consequently, dissolution testing cannot be transferred from a single-entity product; it must track the marker or markers that are relevant to the intended formulation. If ephedrine is selected as the dissolution marker, its water-soluble salt form may mask formulation differences; if amygdalin is selected, temperature and pH stability of the sample must be controlled. Published data for this exact finished combination in veterinary species is limited, so therapeutic equivalence cannot be assumed from marker content alone.
Compared with a single-herb ephedra extract or a single-herb licorice extract, this product contains calcium sulfate from gypsum. That mineral component changes the density and tableting behavior of the dry extract and is a major reason that tablet-grade powder cannot be directly substituted into an injectable solution. The fixed formula ratio also creates an analytical constraint: if one raw herb lot has a low marker content, it cannot be corrected by simply adding isolated marker compounds. The botanical ratio must be maintained, and the extraction process must be adjusted against the formula. The product is therefore supplied to manufacturers as a standardized intermediate, not as a synthetic chemical whose impurity profile can be definitively indexed.
Regulatory handling differs as well. Ephedra-derived alkaloids are subject to precursor or controlled-substance controls in certain jurisdictions. Import, export, and inventory records may require a veterinary drug import permit, a good manufacturing practice certificate, and an end-use declaration. Unopened material should be stored in a cool, dry, controlled-access area. If storage is not under controlled access, supply-chain compliance rather than pharmacopeial chemistry may become the limiting specification.