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Maxingshigan Injection Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions

    • Product Name: Maxingshigan Injection Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 103419
    Product Name Maxingshigan Injection Veterinary Grade API
    Active Ingredients Ephedrine, amygdalin, glycyrrhizin, and gypsum extract
    Physical Form Fine crystalline powder or liquid concentrate
    Solubility Soluble in water and dilute ethanol
    Ph Range 4.5 to 6.5
    Assay Purity ≥98.5%
    Heavy Metals Content ≤10 ppm
    Microbial Purity Total viable count ≤1000 CFU/g
    Loss On Drying ≤5.0%
    Storage Condition Store in a cool, dry, well-ventilated area
    Shelf Life 24 months
    Veterinary Indications Relieves cough, asthma, and fever in livestock and poultry

    As an accredited Maxingshigan Injection 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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    Application of Maxingshigan Injection Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions

    What Processing Parameters Govern Sterile Parenteral Formulation of Maxingshigan Extract?

    Maxingshigan Injection Veterinary Grade API is supplied as an injection-grade aqueous concentrate of Ephedrae Herba, Gypsum Fibrosum, Armeniacae Semen Amarum, and Glycyrrhizae Radix et Rhizoma, standardized to ephedrine alkaloid and amygdalin marker content. The concentrate is not a direct injectable; downstream sterile formulation requires dilution to 20–30% v/v in Water for Injections at 45–55°C. The pH is adjusted with 0.1 M sodium hydroxide or citric acid to a narrow window of pH 5.0–5.5. This window is a process determinant rather than a formulation preference: below pH 4.5, glycyrrhizic acid precipitates as a viscous sediment, while above pH 6.5, the cyanogenic glycoside fraction and amygdalin hydrolysis accelerate, increasing benzaldehyde and hydrogen cyanide degradation markers. Calcium sulfate from Gypsum Fibrosum saturates the solution, so processing water must not introduce bicarbonate alkalinity above 50 mg/L CaCO₃ to avoid calcium carbonate nucleation. Compliance for the sterile route is anchored to the relevant pharmacopoeial general chapters, including Ph. Eur. 2.6.1 for sterility and Ph. Eur. 2.6.14 for bacterial endotoxins; fill operations follow EU GMP Annex 1 with Grade B background and Grade A LAF. The diluted solution is treated with 0.1% w/v activated carbon at 60°C for 30 minutes, passed through a depth filter, and then through 0.45 µm/0.22 µm polyethersulfone capsule filters. Terminal steam sterilization at 121°C for 15 minutes is used only when the batch-scale validation confirms ephedrine HCl recovery ≥ 95%; otherwise aseptic filtration is specified. Production-scale fill lines record that hold times beyond 8 hours before filtration can produce visible calcium sulfate crystal growth, so preparation lots are generally split at 500 L. Terminal presentations are 10 mL, 20 mL, and 100 mL neutral borosilicate vials or ampoules for porcine and bovine respiratory indications. The injection is incompatible with sulfonamide sodium parenteral fluids because co-administration produces precipitate; ephedrine content also requires import documentation under controlled precursor rules in multiple jurisdictions.

    In broiler and layer integrations that administer respiratory support through closed nipple-drinker systems, the limiting unit operation is not the marker content of the API but the rate and completeness of solubilization in hard water at ambient temperature. Maxingshigan dry extract API for water-soluble powder is spray-dried onto maltodextrin or soluble starch, with loss on drying ≤ 4%. The formulation input range is 4–8% w/w of the finished powder, with anhydrous dextrose q.s. to 100%, PVP K30 at 1–2%, and fumed silica at 0.5–1% as flow control. If the dry extract particle fraction above 150 µm exceeds 10%, pre-milling on a pin mill fitted with a 0.5 mm screen is required before blending. Compliance is typically demonstrated against the Chinese Veterinary Pharmacopoeia soluble powder monograph for content uniformity and against VICH GL18 for residual solvent testing. The blend is mixed in a horizontal ribbon mixer at 60–70% fill volume for 10–12 minutes, discharged at ≤ 40% RH, and packed into 100 g, 500 g, or 1 kg foil-lined pouches. For farms with water hardness above 300 mg/L CaCO₃, the formula includes citric acid at 1–2% to reduce drinker-water pH to 5.5–6.0; without acidification, calcium sulfate fines from the herbal extract can deposit in pressure regulators and nipple drinkers. Sodium bicarbonate-buffered house water is a documented incompatibility because it precipitates calcium carbonate from the gypsum fraction and blocks drinker lines. Terminal products are 100 g, 500 g, and 1 kg water-soluble powder sachets; the same API grade can be converted into 1 L and 5 L oral solutions using a sorbitol-glycerin vehicle, but pH must remain below 6.0 at use dilution to limit amygdalin hydrolysis.

    Conditional formulation input ranges for Maxingshigan veterinary-grade API
    Dosage-form pathwayAPI input rangeCritical process limitTerminal presentations
    Parenteral injection20–30% v/v aqueous concentratepH 5.0–5.5; 0.22 µm filtration10/20/100 mL vials, ampoules
    Water-soluble powder4–8% w/w dry extractLoss on drying ≤ 4%; hardness ≤ 300 mg/L CaCO₃100/500/1 kg sachets
    Feed premix5–10 kg/t final feedMixer CV ≤ 5%; pelleting ≤ 65°C5%/10% premix, 25 kg sacks
    Oral granules15–25% w/w granule massLoss on drying ≤ 3%; torque rise 8–12%10 g stick packs; 100 g jars
    Tablet/capsule10–20% w/w granulateHardness 60–80 N; disintegration ≤ 30 min300/500/750 mg tablets; 200/400 mg capsules
    Oral solution20–30% v/v liquid APIpH 4.8–5.5; Ph. Eur. 5.1.3 preservation1/5/25 L amber packs

    With a Direct Compression Route Skipped, What Happens Inside a 2-Ton Ribbon Mixer During Dry Premix Dilution?

    Feed premix intermediates containing Maxingshigan dry extract at 5–10 kg/t final feed are produced by progressive geometric dilution through a two-stage system. Stage one compacts the API with rice hulls, microcrystalline cellulose, and calcium silicate at 1:10 before introduction to a 2-ton horizontal ribbon mixer operating at 18 rpm and 60–70% fill volume. The critical acceptance criterion is coefficient of variation ≤ 5% for marker ephedrine across 10 sampling points. Single-stage mixing is not sufficient because the dry extract has bulk density 0.45–0.55 g/cm³, whereas soybean meal carriers are 0.62–0.68 g/cm³; density mismatch causes stratification after discharge. Compliance for EU medicated feed is under Regulation (EU) 2019/4, including homogeneous incorporation and carryover controls, rather than feed additive rules; the material is not a zootechnical feed additive. Moisture at mixer discharge is kept ≤ 12% for mash and ≤ 10% before pelleting, with moisture determined per ISO 6496. Pelleting is run at a conditioning temperature of ≤ 65°C and retention time of 45 seconds; temperatures above 70°C produce measurable amygdalin loss and darkening of the pellet surface. In high-humidity zones above 60% RH, uncoated API forms a hard layer on mixer shafts within 6 hours; this is an observed production bottleneck requiring line stoppage and steam-cleaning of the shaft. Terminal products are 5% and 10% premixes in 25 kg paper sacks with PE liner for nursery and grower pigs. In jurisdictions where ephedra-containing botanical preparations are not registered veterinary medicines, medicated feed use is not permitted; formulators must verify national controls before shipment.

    For pre-ruminant calves with enzootic pneumonia, the dry extract is formulated into granules because this route avoids the inhalable dust fraction generated by water-soluble powders while permitting direct oral drenching or top dressing onto starter feed. Maxingshigan granule API input is 15–25% w/w of the finished granule mass. The powder blend consists of lactose monohydrate 35–45%, microcrystalline cellulose 20–25%, sodium starch glycolate 2–4%, and povidone K30 as binder at 1–2%. Wet granulation is performed in a high-shear granulator with impeller speed 300–400 rpm and chopper 1500–2000 rpm; purified water is added at 18–20% w/w, with endpoint determined by torque rise 8–12% above the dry blend baseline. Drying in a fluid-bed dryer at 50°C inlet air to loss on drying ≤ 3% protects the amygdalin fraction from thermal degradation. The dried granules are sized through 12/20 mesh and packed as 10 g triple-foil stick packs, 100 g HDPE jars, or 1 kg pouches. Compliance is assessed by the Chinese Veterinary Pharmacopoeia granule monograph for moisture, content uniformity, and microbial limits, with USP 711 dissolution used for marker release where the importing jurisdiction follows USP general chapters. This section is shorter than the injectable route because the technical path is well-established and the only critical transfer point is moisture ingress during stick-pack filling below 35% RH. Prolonged oral administration of glycyrrhizin is recognized to cause sodium retention in calves, so treatment duration is ordinarily limited to 7 days and serum sodium is monitored when administration exceeds 5 days.

    Tablet and Capsule Compression Without Exceeding the Hygroscopicity Limit of Spray-Dried Botanical Extract

    Direct compression of Maxingshigan dry extract above 20% w/w is not recommended because the extract acts as a self-binder and picks up moisture within 15 minutes at 50% RH, causing capping on rotary presses. Tablet and capsule formulations therefore use slugging or dry granulation: API input is 10–20% w/w, dibasic calcium phosphate dihydrate 40–55%, microcrystalline cellulose 20–30%, croscarmellose sodium 2–5%, colloidal silicon dioxide 0.5–1.0%, and magnesium stearate 0.5–1.0%. Compression is run at 12–18 kN on a 12-station rotary press to target hardness 60–80 N, thickness 3.5–4.5 mm, and friability ≤ 0.8% per USP 1216. Disintegration is controlled by USP 701 and is specified as ≤ 30 minutes in water at 37°C. For capsules, the granulate is filled into size 3 or size 1 hard gelatin or HPMC capsules at 60–70% of maximum fill volume; low-fill capsules generate dust and electrostatic adherence on high-speed dosator machines. Compliance for non-food-producing equine and companion animal applications follows current veterinary GMP and the relevant national pharmacopoeial general chapters, with certificates of analysis stating microbial limits, heavy metals, and residual solvent profile according to VICH GL18. Terminal products are 300 mg, 500 mg, and 750 mg tablets in aluminum/PVC cold-form blisters, and 200 mg and 400 mg hard capsules in HDPE bottles with 1 g silica gel desiccant. Magnesium stearate above 1.0% is a documented compression failure mode because it combines with the extract’s free calcium to form hydrophobic agglomerates that slow disintegration beyond specification.

    Oral Solution pH Windows and the Preservative Partitioning Behaviour of Maxingshigan Liquid API

    Maxingshigan liquid API in oral solutions is maintained at 20–30% v/v in a co-solvent system of sorbitol 40–55%, glycerin 5–10%, and purified water q.s. to 100%. The solution pH is adjusted to 4.8–5.5 with citric acid; this range keeps glycyrrhizic acid soluble while suppressing benzaldehyde and hydrogen cyanide development from the cyanogenic glycoside fraction. Preservative selection is constrained because polysorbate 80 above 0.1% inactivates methylparaben; the standard system uses methylparaben 0.08% and propylparaben 0.02%, with preservative challenge testing per Ph. Eur. 5.1.3. The liquid is compounded in a jacketed stainless mixing vessel at 55–60°C, cooled to 25°C before final pH adjustment, and passed through a 10 µm cartridge filter to remove particulate calcium sulfate without removing active markers. Filling is into 1 L, 5 L, and 25 L amber polyethylene terephthalate or HDPE jerrycans with induction-sealed closures; the light-protective container is required because ephedrine alkaloids in aqueous solution are susceptible to photodegradation under ICH Q1B conditions. The terminal products are oral dosing solutions for calves, lambs, foals, and pigs when individual animal administration is preferred over drinking-water mass medication. Sodium bicarbonate buffer should not be substituted for citric acid; bicarbonates reduce the solution’s pH-buffering capacity at use dilution and permit visible precipitation at >500 mg/L CaCO₃ equivalent. Published data for this specific liquid configuration is limited outside Chinese-language technical bulletins; batch-specific validation is required for the pH and preservative levels stated here.

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    Certification & Compliance
    More Introduction

    Maxingshigan Injection Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions is a standardised multi-component botanical active pharmaceutical ingredient rather than a single chemical entity. The source material corresponds to the Maxing Shigan composition of Ephedra sinica aerial parts, Prunus armeniaca seed, Gypsum fibrosum, and Glycyrrhiza uralensis root. No unified pharmacopoeial model number exists for this combination; therefore, batch-specific internal codes should be assigned by the receiving site and linked to the extraction lot under ICH Q7 documentation. Published monographs for this exact API as an injectable veterinary raw material are limited, so release specifications must be derived from the target dosage form, process validation, and pharmacopoeial general chapters.

    Across the dosage form range specified, the physical grade must be deliberately partitioned. A single extraction lot can be air-jet milled to D90 ≤75 µm for direct compression and capsule fill operations, or sieved to a granular cut between 180 µm and 850 µm for premix and granule blending. Injection-grade material is not simply the same powder with reduced particle size; it requires separate depyrogenation, bioburden control, and particulate reduction operations. A failure to separate these grades at the receiving site commonly produces cross-contamination from oral-grade corn starch or lactose carriers into parenteral lines, which is a batch rejection risk under sterility and particulate requirements.

    What conditions force a choice between direct compression and high-shear granulation?

    Direct compression is only feasible when the API fraction has a Hausner ratio ≤1.25 and a Carr index ≤20%; above these boundaries, flow segregation produces weight variability outside USP <905> uniformity limits. The standardised extract may retain polysaccharide fractions from Glycyrrhiza uralensis, which increase cohesiveness at relative humidity above 60%. In high-shear granulation, binder addition is stopped before impeller torque exceeds 30 N·m because overwetting creates a paste that stalls the chopper. A production-scale high-shear mixer operating at impeller speed 200 rpm and chopper speed 1500 rpm can form granules of acceptable density in 120 s, but this window must be revalidated for each extraction lot because the polysaccharide-to-marker ratio is not fixed.

    Fluid-bed drying after granulation should maintain inlet air temperature at 45°C to 55°C and product temperature below 40°C; ephedrine alkaloid loss can exceed 5% when the bed remains above 45°C under high moisture. Residual moisture is controlled to ≤5.0% w/w by USP <731>. At storage relative humidity above 60%, caking becomes irreversible if the API is not packed with desiccant. Tablet compression on 9 mm round tooling is typically targeted to hardness 60 N to 80 N and friability ≤1.0% under USP <1216>.

    When a low endotoxin burden becomes the primary release criterion for injectable veterinary lines

    When the API is intended for injectable veterinary products, the bacterial endotoxin limit should be set at ≤0.5 EU/mg; for large-volume parenteral preparations the tighter limit of ≤0.25 EU/mg is used. Endotoxin is quantified using USP <85> chromogenic LAL at 37°C ± 0.5°C with a validated lysate sensitivity of 0.06 EU/mL. Because plant-derived extracts carry lipopolysaccharide from rhizosphere bacteria, oral-grade lots routinely exceed these limits and cannot be reworked into injectable grade by sterilisation alone: moist-heat sterilisation at 121°C for 15 min reduces viable bioburden but does not remove pre-existing endotoxin. Depyrogenation by tangential-flow filtration, activated carbon, or chromatographic capture must be applied before terminal filtration. Marker recovery after depyrogenation is not guaranteed; ephedrine alkaloid loss may exceed 10% on carbon-based depyrogenation, and the process therefore requires re-assay.

    Parenteral processing of this API creates a specific membrane-fouling failure mode. If the reconstituted or purified concentrate is filtered directly through 0.45 µm and 0.22 µm polyvinylidene difluoride membranes without clarification, residual colloids can raise membrane loading above 10 g/m² and reduce flux to 50 L/m²/h or lower. The corrective sequence is chilled centrifugation at 10°C to 15°C, prefiltration through 5 µm cellulose acetate, and then the final sterilising-grade membrane. Insoluble particulate matter in the finished injection is measured by light obscuration under USP <788>; acceptance for small-volume parenterals is not more than 6000 particles per container at ≥10 µm and not more than 600 particles per container at ≥25 µm. pH of the final solution is controlled to 5.0 to 7.0 under USP <791>, because alkaline conditions destabilise the solution and can precipitate residual saccharides.

    Dosage form Primary process risk Critical API control Reference method
    Tablets by direct compression Capping and lamination under high compression force Hausner ratio ≤1.25; D90 ≤150 µm USP <1174>; USP <616>
    Capsules Powder bridging and fill weight variability Bulk density 0.35–0.65 g/mL; moisture ≤5.0% w/w USP <616>; USP <731>
    Injections Endotoxin burden and subvisible particulate formation Endotoxin ≤0.5 EU/mg; pH 5.0–7.0 USP <85>; USP <788>
    Powders and granules Segregation during transfer Particle-size ratio to carrier 1:0.6–1:1.4 ISO 13320:2020
    Premix Blend non-uniformity in feed matrix Assay relative standard deviation ≤5.0% USP <905>
    Solutions pH drift and precipitation Solution clarity at pH 5.0–7.0 USP <791>

    Capsule filling on dosator machines is sensitive to powder bridging when bulk density falls below 0.35 g/mL; if tapping raises density by more than 20%, the blend is considered floodable and requires precompaction or slugging. The API's residual moisture interacts with gelatin capsules; moisture transfer above 5% w/w can embrittle capsule shells. Therefore, desiccant loading in high-density polyethylene bottles is calculated from the moisture vapour transmission rate of the closure.

    Premix dispersion, reconstitution pH, and water-medication compatibility constraints

    Premix formulations require active particle size to match the carrier within a particle-size ratio of 1:0.6 to 1:1.4; outside this window, vibration during transport stratifies the mixture. The API is usually loaded onto calcium carbonate, wheat middling, or lactose carriers at 5 kg to 25 kg active per tonne of final feed. Blend homogeneity is assessed by assay of at least 10 sampling points with relative standard deviation not exceeding 5.0%.

    In aqueous solution, reconstituted API from the liquid or powder formulation has a target pH of 5.0 to 7.0. Hard water containing calcium and magnesium above 200 mg/L as CaCO₃ may form insoluble complexes with residual organic acids from licorice and apricot kernel; therefore, water-medication lines with high hardness should be pre-mixed with a chelating agent or acidified to pH 5.5 before API addition. The solution should not be combined with cationic preservatives such as benzalkonium chloride without a visual precipitation study, because residual anionic polysaccharides can form insoluble ionic complexes. This incompatibility is not observed in all batches because the polysaccharide content depends on the extraction solvent and demineralisation variables.

    In solution, stability of the API is limited by hydrolysis of amygdalin under acidic and alkaline conditions. For oral solutions, buffering to pH 5.0–5.5 and storage at 25°C may hold marker content within ±5% for 12 months if the container is amber polyethylene terephthalate. For injection-grade liquids, sterility must be maintained concurrently with chemical stability, so aseptic filtration is followed by inert-gas overlay and closure in Type I borosilicate glass. Published data for this specific formulation at 40°C accelerated conditions are limited; therefore, pilot stability studies should be designed according to VICH GL3.

    The primary difference from other products is standardisation with a defined multi-marker ratio rather than a single assay or total solids claim. A synthetic single-marker active, such as ephedrine hydrochloride, is a chemically discrete substance with assay limits of 98.0% to 102.0%. This botanical API is defined by percentage contributions of ephedrine alkaloids, amygdalin, and glycyrrhizic acid, with each marker controlled to ±10% of the declared label. Non-standardised powders differ in that marker failures may appear as variation in colour, odour, and extract viscosity; these qualitative attributes are not acceptance criteria but can signal extraction deviation. The present API is therefore supplied with a certificate of analysis listing residual solvent, heavy metal, microbiological, and marker assay results, which is not uniformly provided for commodity plant powders.

    Characteristic Synthetic single-marker active Non-standardised botanical powder Standardised Maxingshigan API
    Analytical basis Single assay Total identity or coarse botanical microscopy Multi-marker HPLC profile
    Batch consistency 98.0–102.0% of single marker Lot-to-lot variance may exceed 30% Markers controlled to ±10% of label claim
    Endotoxin control Usually low; dilution may be required Uncontrolled Injection grade controlled to ≤0.5 EU/mg
    Solution behaviour Defined aqueous or organic solubility Variable extraction-dependent solubility Controlled pH range 5.0–7.0
    Documentation Drug master file or certificate of suitability Limited certificate of analysis Certificate of analysis with stability and residual solvent data

    Packaging for solid grades should use triple-layer aluminium foil or high-density polyethylene drums with desiccant when storage exceeds 6 months at 25°C and 60% RH. Liquid injection-grade concentrates require refrigerated storage at 2°C to 8°C under nitrogen or vacuum closure to reduce oxidation of residual phenols. Open handling of the material should be done in a downflow booth because fine fractions may become airborne and leave a persistent licorice-like residue on contact surfaces. The API is not intended for human use, and its acceptance for export requires supplier verification against the receiving country’s veterinary residue and heavy-metal regulations; lead, cadmium, arsenic, and mercury should be controlled to ≤10 ppm, ≤1 ppm, ≤3 ppm, and ≤0.1 ppm respectively by atomic absorption or inductively coupled plasma-mass spectrometry under USP <232>/<233>.

    Final formulation development should include extraction recovery studies under the actual granulation or sterilisation conditions, because marker loss is not linear across dosage forms. Published data for this specific configuration is limited, so each site should validate the analytical transfer using ICH Q2(R1) and maintain retention samples for at least 5 years under cGMP.

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