| HS Code | 515823 |
| Product Identifier | Zhusha Powder Veterinary Grade API |
| Active Ingredient | Cinnabar (Mercuric sulfide, HgS) |
| Grade | Veterinary Grade |
| Dosage Form Compatibility | Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions |
| Cas Number | 1344-48-5 |
| Chemical Formula | HgS |
| Molecular Weight | 232.66 g/mol |
| Physical Form | Fine crystalline powder |
| Color | Bright red to dark red |
| Odor | Odorless |
| Solubility Profile | Insoluble in water and ethanol; soluble in aqua regia and alkali sulfide solutions |
| Storage Conditions | Keep in tightly closed container, protected from light and moisture, in a cool dry place |
| Shelf Life | 36 months from manufacturing date |
As an accredited Zhusha Powder 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 | Sealed double-layer polyethylene bags inside fiber drums, 25 kg net weight, tamper-evident, labeled for veterinary use. |
| Container Loading (20′ FCL) | One 20′ FCL contains Zhusha Powder Veterinary Grade API, securely packed in sealed drums, palletized and containerized for safe transport. |
| Shipping | Zhusha Powder (Veterinary Grade API) ships in sealed, moisture-proof containers with tamper-evident labeling. Ensure cool, dry storage away from light and incompatible materials. Transport via ground or air with proper hazardous-material documentation, if applicable. Include Certificate of Analysis and Safety Data Sheet with every consignment. |
| Storage | Store in a tightly sealed, opaque container in a cool, dry, well-ventilated area. Protect from light, moisture, and high temperatures. Keep away from incompatible substances and foodstuffs. Ensure container remains closed when not in use. Follow veterinary pharmacopoeia guidelines and use within stated shelf life. |
| Shelf Life | Shelf life is 24 months when stored in a cool, dry, sealed container away from light and moisture. |
Where the destination market applies the Cinnabaris monograph of the Chinese Pharmacopoeia 2020, the material is expected to meet an assay limit of not less than 96.0% HgS. In tablet manufacture for non-food companion animals, the first processing obstacle is not chemical incompatibility but density-driven segregation of the red α-HgS particles. The true density of cinnabar lies near 8.10 g/cm³, while common tableting carriers such as microcrystalline cellulose and lactose monohydrate remain in the 1.5–1.6 g/cm³ range. A wet-granulation route is therefore used when the dose requires greater than approximately 2.0% w/w HgS in the core. The API is first triturated with an equal mass of lactose monohydrate through a 300 µm sieve, then mixed stepwise with the remaining diluent in a pilot-scale high-shear granulator. The granulating fluid is purified water containing 2–5% w/w povidone K30; acidic granulating fluids are avoided because the resulting granule environment may generate localized low-pH regions that complicate mercury release testing, even though cinnabar is practically insoluble in dilute hydrochloric acid.
Drying is capped at 60°C and continued until loss on drying is not more than 2.0% w/w according to USP <731>. The upper temperature boundary is conservative because published decomposition data for this specific veterinary-grade HgS under forced-air drying is limited; the red α-form can convert to black metacinnabar under certain thermal and light conditions. The dried granulate is passed through an oscillating granulator fitted with a 1.0 mm screen. A low-shear tumble blender then receives the external phase, which includes crospovidone at 2–4% w/w, colloidal silicon dioxide at 0.5–1.0% w/w, and magnesium stearate at 0.25–0.75% w/w. Compression is monitored by weight variation, friability per USP <1216>, and content uniformity per USP <905>; an acceptance value of not more than 15.0 in Stage 1 is applied unless the batch is justified by Stage 2 testing. Film coating uses an opaque HPMC-based dispersion to reduce light exposure because the red cinnabar surface can darken during storage in clear packaging.
Direct compression trials with HgS loadings up to 2.0% w/w usually begin with a coarse lactose carrier fraction in the 100–200 µm sieve cut because ordered mixing requires the fine API to adhere to a coarser carrier surface. The fine fraction of Zhusha powder is preferably jet-milled to a laser diffraction D90 below 10 µm, measured by ISO 13320:2020, but excessive micronization increases the electrostatically active surface area and promotes detachment from the carrier during tablet press feed frame shear. Process failure is observed when the relative standard deviation of blend samples exceeds 5.0% before any tablet is compressed; this commonly occurs in low-humidity rooms below 30% RH or when the feed frame paddle speed is high enough to separate the attached fines from the lactose carrier. A conservative direct-compression window is achieved by maintaining processing humidity at 40–60% RH, reducing the feed frame paddle speed, and limiting turret speed until tablet weight variation remains within ±3.0% for a 200 mg core containing less than 2.0% w/w HgS.
When content uniformity per USP <905> fails at Stage 1, re-blending is rarely effective because the segregation mechanism is density-driven and electrostatic rather than purely geometric. The accepted control therefore relies on sealed transfer bins, minimal drop height into the tablet press hopper, and periodic sampling from the press discharge. No additional wet granulation should be imposed as a retroactive correction without repeating compatibility testing because the granulation binders may alter the ordered mixing architecture.
Because dosator-type capsule machines compact the powder bed to form a slug, the pre-blend must possess sufficient cohesion to remain intact during transfer but not so much that the slug breaks unevenly when ejected into the capsule body. The standard trituration uses lactose monohydrate as the diluent and a geometric dilution sequence of at least four steps, starting with a 1:1 mixture of HgS and lactose passed through a 300 µm screen. A low-shear tumble blender operated at 40–60% fill depth is preferred to a high-shear mixer because high-shear mixing of dense HgS can produce a fine dust fraction that adheres to the blender walls. The finished triturate is sampled at top, middle, and bottom locations with a thief sampler; a relative standard deviation of not more than 5.0% is applied before capsule filling. Capsule shells are opaque gelatin or HPMC to limit photodarkening of the red polymorph.
Dissolution testing is not used as a release-specifying surrogate for immediate drug release because cinnabar is practically insoluble in aqueous gastrointestinal media. Instead, finished capsule content uniformity is confirmed by USP <905>, and capsule disintegration is evaluated according to USP <701>. Capsule weight and lock length are recorded during the filling run; dosator height and tamping pin force are adjusted when the coefficient of variation of filled capsule mass exceeds 2.0% over 20 consecutive capsules. The major operational boundary is dust generation from the dosator station; the filling area must operate under local exhaust with mercury exposure control at the 0.025 mg/m³ 8-hour TLV-TWA for inorganic mercury as Hg.
Premix dilution follows a geometric sequence because the API is dense and the target concentration in the finished carrier feed can be less than 0.1% w/w. The first dilution is usually 1:10 or 1:20 with ground corn, wheat middlings, or calcium carbonate as carrier; each step is mixed for at least 10 minutes in a horizontal ribbon mixer equipped with a variable-speed drive. The selection of a carrier with a bulk density above 0.6 g/cm³ reduces segregation after transfer, but no carrier fully cancels the density mismatch with 8.10 g/cm³ HgS, so post-mix bin samples are taken before discharge to confirm a coefficient of variation below 5.0%. Vegetable oil is added at 0.5–1.0% w/w of the premix to reduce dust, provided that the oil does not compromise flow into downstream feed mill hoppers. The resulting premix is transferred in closed containers and labeled for restricted use in non-food-producing animals unless regional medicinal feed legislation explicitly permits a derogation.
In the EU, mercury compounds are not listed in Table 1 of Commission Regulation (EU) No 37/2010 as allowed substances for food-producing species; therefore a medicated premix containing HgS cannot be placed on the market for food-producing animals. In feed mills that handle multiple species, the cleaning validation protocol must include mercury-specific rinse or swab limits developed from the final line usage and regional feed safety requirements. Shared equipment is a carryover risk because HgS particles lodged in dead legs, rotary valve pockets, or bucket elevator seams are poorly removed by dry flushes; a wet clean followed by a verified dry flush is preferred, but published carryover data for this specific veterinary-grade HgS in feed mill lines is limited.
| Premix processing step | Critical control | Boundary condition | Test or equipment |
|---|---|---|---|
| First geometric dilution | Carrier ratio | 1:10 to 1:20 | Ribbon mixer, coefficient of variation <5.0% |
| Mixing time | Homogeneity | 10 min minimum per dilution step | Stratified sampling, ANOVA |
| Dust control | Vegetable oil addition | 0.5–1.0% w/w | Dust meter, local exhaust |
| Mercury exposure | Inorganic Hg TLV-TWA | 0.025 mg/m³ | ACGIH occupational exposure limit |
Granule and powder sachet operations require local exhaust ventilation at the bag dump station and the sieve transfer point because the fine fraction of cinnabar becomes airborne more readily than organic APIs of lower density. The granulation is typically prepared by fluid-bed top-spray granulation with a binder solution of povidone K30 at 2–3% w/w and purified water. The inlet air temperature is capped at 60°C and the product moisture is controlled to a loss-on-drying value below 2.0% w/w to reduce mold growth in sachets. After drying, the granulate is screened to a 355–1000 µm fraction; fines below 150 µm are recycled to the next granulation batch because their high specific surface area contributes to dust formation and poor flow. The finished sachet fill weight is verified by weight variation, and the sachet material is selected from aluminum foil laminate with a light barrier layer.
When granules are intended for reconstitution before animal dosing, the formulation includes a suspending agent such as microcrystalline cellulose/carboxymethyl cellulose sodium at 1–2% w/w and sorbitol as a density-modifying vehicle component. The suspension is not a solution; the label and the stability protocol must evaluate redispersibility rather than clarity. Redispersibility is tested by manual inversion of the closed container for 30 seconds followed by visual inspection for caked sediment. Published data for oral granule reconstitution containing this specific veterinary-grade HgS is limited, so a 24-hour sedimentation volume test is used to define the acceptable suspending agent concentration for each batch.
For parenteral dosage forms, the first decision gate is residue status rather than particle size reduction capability. An injectable preparation of Zhusha powder would necessarily be a suspension because HgS is practically insoluble in water and common parenteral co-solvents. The formulator would be expected to reduce the particle size to a parenteral suspension specification, typically a D90 below 10 µm for intramammary or intramuscular suspensions, and to evaluate sub-visible particles according to USP <788> or Ph. Eur. 2.9.19. Terminal steam sterilization at 121°C for 15 minutes cannot be validated unless the chemical stability program demonstrates no decomposition, polymorph conversion, or release of mercury species under those conditions; published data for this specific veterinary-grade HgS in the injectable configuration is limited. Sterile filtration is not possible, and aseptic processing of an insoluble mineral suspension introduces additional contamination risk from the particle matrix itself.
The controlling boundary in major regulated markets is not viscosity or sterility but the absence of a maximum residue limit for mercury in food-producing species. Under Commission Regulation (EU) No 37/2010, mercury compounds are not included in the allowed substances table for food-producing animals, and therefore no injectable HgS product can be authorized for food-producing species in the EU. For companion animals, an injectable suspension would need to overcome the local depot issue: injected HgS particles can persist at the injection site and produce long-term chronic exposure, inflammation, and systemic accumulation. Published toxicokinetic data for such local retention in cats, dogs, or horses exposed to this specific powder is limited; therefore, formulation development cannot rely on a generic soluble drug modeling package.
When a liquid oral dosage form is requested, the formulator must distinguish a true solution from a structured suspension; HgS is practically insoluble in aqueous buffers, ethanol, and glycerin, so the product is a suspension regardless of the label word solution. The vehicle is built around a high-viscosity suspending network, commonly xanthan gum at 0.2–0.5% w/v or sodium carboxymethyl cellulose at 0.5–1.5% w/v. Stokes settling calculations for a 5 µm diameter HgS particle in water indicate a settling velocity near 97 µm s⁻¹, which is rapid enough to produce a hard cake within minutes; increasing the continuous phase viscosity to 20 mPa·s reduces the settling rate proportionally and extends redispersion intervals. The pH is maintained in the neutral range because low-pH vehicles can shift the surface charge of the suspending polymer and alter flocculation behavior; the specific interaction with cinnabar in this particular veterinary grade has limited published data.
Preservation of an oral suspension for multi-dose use requires sodium benzoate at 0.1% w/v or potassium sorbate at 0.1% w/v, subject to dose-volume and animal species acceptability. The finished product is tested for sedimentation volume, redispersibility, viscosity, and content uniformity of the redispersed suspension; filtration assay is not acceptable because the API is predominantly in the solid phase. The container is light-resistant glass or high-density polyethylene with an aluminum foil induction seal to limit photodarkening of the red polymorph. The product is labeled for non-food-producing companion animals only unless the relevant regional regulation provides an explicit authorization. No true solution can be prepared from Zhusha powder without digestion that would destroy the HgS structure and generate soluble mercury species; such processing is outside the intended application of the veterinary-grade API.
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Zhusha Powder Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions is a mineral-derived active pharmaceutical ingredient consisting predominantly of mercuric sulfide, HgS, prepared from cinnabar ore by elutriation or wet grinding and dried to controlled moisture. The product is supplied under material code ZS-VET-API-96/98, with the numerical suffix identifying the minimum HgS assay: the 98 grade is normally reserved for injectable and liquid-suspension development, and the 96 grade is used for solid oral dosage forms and premix lines. The powder is red to dark red, practically insoluble in water, and is identified by the Cinnabaris monograph of the Chinese Pharmacopoeia 2020, which sets HgS content at not less than 96.0%. It differs from crude cinnabar ore by the removal of coarse gangue and from synthetic precipitated mercuric sulfide by its natural trace-mineral signature and trigonal crystal form.
Release testing is governed by the intended dosage form rather than by a single uniform specification. Non-sterile oral and premix applications are controlled for appearance, assay, loss on drying, acid-insoluble residue, particle size, and elemental impurities. Injectable and liquid-suspension lines add particulate-size reduction, endotoxin, and leachable-mercury testing to the finished vehicle. The values in the following table are representative release criteria for the 98-grade material; natural mineral variability prevents a fixed universal specification, and each batch must be read against its certificate of analysis.
| Parameter | Representative criterion | Method / reference |
|---|---|---|
| Assay as HgS | ≥ 98.0% for the 98 grade; ≥ 96.0% for the 96 grade | Chinese Pharmacopoeia 2020 Cinnabaris |
| Loss on drying | ≤ 1.0% | USP <731> |
| Acid-insoluble residue | ≤ 1.0% for air-milled lots; report basis may vary by ore lot | Gravimetric after hydrochloric acid digestion |
| Particle size, oral solid | D90 ≤ 75 µm | ISO 13320:2020 laser diffraction |
| Particle size, injectable | D90 ≤ 15 µm | ISO 13320:2020 laser diffraction |
| Lead | ≤ 5 mg/kg | USP <233> |
| Arsenic | ≤ 2 mg/kg | USP <233> |
| Microbial enumeration, non-sterile | Total aerobic count ≤ 103 CFU/g; yeast and mould ≤ 102 CFU/g | USP <61>, USP <62> |
| Endotoxin, injectable development | ≤ 0.5 EU/mg when specified | Ph. Eur. 2.6.14 |
| Sterility of finished injectable | Conforms after terminal sterilization | USP <71> |
Because the single-crystal density of cinnabar is approximately 8.1 g/cm³, the milled powder segregates rapidly when dry-blended with lactose, cellulose, or cereal premix carriers having bulk densities below 0.6 g/cm³. Tapped density and flow measurements according to USP <616> and USP <1174> are therefore treated as lot-release parameters for solid dosage work, not as routine descriptive data. The red colour is an effective visual marker for blend homogeneity, but visual inspection cannot replace quantitative HgS assay because fines and coarse fractions can display identical colour intensity. Air-jet milling reduces primary particle size without necessarily normalizing the trace quartz and pyrite fractions that alter cohesion and ejection force; this is the principal reason that two natural ore lots with the same assay can exhibit different tablet hardness and granulation behaviour.
In production-scale spiral-jet milling aimed at D90 ≤ 15 µm, the main bottleneck is not particle-size reduction but the retention of dense cinnabar fines in the classifier circuit. Dense particles are retained longer than low-density excipients at the same aerodynamic diameter, leading to over-milling and a broadening of the particle-size distribution tail below 1 µm. That over-milled fraction increases poured-to-tapped density ratio and can produce stable agglomerates in suspension. Operators typically reduce feed rate relative to organic APIs of similar nominal particle size and increase grinding-gas pressure to hold the target D90. The process window is narrow because too much pressure raises the sub-1 µm fraction, while too little pressure leaves coarse cinnabar particles that accelerate sedimentation in injectable suspensions.
Injectable development imposes a different control envelope. The API is not inherently sterile; terminal sterilization of the finished suspension is required unless aseptic processing is justified by thermal instability of the vehicle. The particle-size target for suspension injectables is typically D90 ≤ 15 µm to preserve syringeability and reduce the risk of capillary occlusion. That additional milling raises specific surface area and can increase the extractable mercury concentration in the aqueous vehicle, so the finished liquid is tested for soluble mercury by membrane filtration and ICP-MS rather than only for total HgS assay. Bacterial endotoxin limits are negotiated with the finished-product manufacturer; a typical injectable-grade release includes endotoxin ≤ 0.5 EU/mg after depyrogenation. Because HgS is practically insoluble in water, injectable presentations are suspensions or colloids, not true solutions, and label text should not imply dissolution of the API.
Tablet formulations require wet granulation or high-shear dispersion because the high-density API does not remain uniformly distributed in direct-compression blends. A two-stage granulation with a binder solution such as povidone at 2–5% w/w is often specified; the exact level is adjusted after measuring granule bulk density and loss on drying. During high-shear wet granulation, the dense API tends to concentrate in the lower impeller zone after binder addition. If impeller tip speed is insufficient to lift the cinnabar fraction, the batch can stratify and produce out-of-specification assay values at the end of discharge; if the speed is excessive, the dense particles can compact and raise granule hardness. Capsule filling demands weight-fill compensation because the high true density can overload small capsule bodies at low apparent volume; filled mass must be verified against assayed HgS content rather than visual fill level. Powders and granules for premix use are usually milled through an 80-mesh sieve and blended with a carrier such as calcium carbonate or cereal hulls. Blend uniformity is confirmed by sampling at the beginning, middle, and end of blender discharge according to USP <905>.
| Dosage form | Critical API property | Process control / standard |
|---|---|---|
| Tablets | D90 ≤ 75 µm; bulk density | Wet granulation; friability per USP <1216> |
| Injections | D90 ≤ 15 µm; sterility; endotoxin | Terminal sterilization; USP <71> |
| Capsules | Flowability; fill weight | Weight-fill compensation; assay on filled capsules |
| Powders / granules | Sieve pass 80 mesh | Blender discharge sampling; USP <905> |
| Premix | Carrier density match | Ribbon or paddle blending; low-shear dust control |
| Solutions / suspensions | Particle size; leachable Hg | High-shear homogenization; leachable mercury test |
Zhusha Powder Veterinary Grade API is practically insoluble in water and in most pharmaceutical solvents; a true solution is not obtained without chemical modification that changes the active species from cinnabar to a soluble mercury salt. Liquid dosage forms labelled “solutions” therefore require either a suspension stabilizer or a non-aqueous vehicle that maintains HgS particles in a uniformly dispersed state. For an aqueous vehicle at 25 °C, the Stokes settling velocity of a 5 µm cinnabar particle is approximately 0.097 mm/s, or 5.8 mm/min; a 75 µm particle settles at approximately 21.8 mm/s, or 1.3 m/min, because settling velocity scales with the square of particle diameter. These velocities explain why oral suspensions and injectable suspensions require both particle-size reduction and a structured vehicle with measurable yield stress; a vehicle yield stress below the buoyancy-corrected weight force of the largest particle is a formulation failure condition. The use of complexing agents or reducing agents in the vehicle is discouraged in early formulation because they can increase ionic mercury concentration and alter toxicokinetics. If a clear solution is mandatory, the formulation must be reclassified around a different mercury source and evaluated under a separate toxicological file.
Unlike synthetic precipitated mercuric sulfide, which is produced from mercury(II) salt solutions under controlled pH and frequently appears as a brighter, more uniform red powder, Zhusha Powder retains the trigonal cinnabar crystal habit and a small insoluble gangue fraction dominated by quartz, calcite, and pyrite. This gangue fraction is not inert in every dosage form; it raises acid-insoluble residue and can increase equipment wear in high-shear granulators and jet mills. Synthetic red HgS can be manufactured with lower trace-metal variability and tighter particle-size distribution, but it lacks the natural mineral signature and may not satisfy traditional veterinary monographs that require Cinnabaris identification. Compared with water-soluble mercury species such as mercuric chloride or organic mercury preservatives, the cinnabar form has markedly lower water solubility and therefore slower release of ionic mercury under gastric or environmental conditions; that difference does not eliminate toxicological caution, but it changes formulation handling and waste classification.
The trace-metal profile is a further differentiator. Natural cinnabar lots may contain detectable arsenic, lead, and selenium in the sulfide lattice or associated gangue; synthetic HgS made from purified mercury(II) nitrate or chloride can be expected to show lower arsenic and lead but may carry process-related anions such as chloride or nitrate if washing is incomplete. For this reason the veterinary-grade release file includes anion screening by ion chromatography when the API is intended for injectable development. The natural product also retains a weak acid-soluble carbonate fraction from calcite gangue that can raise the pH of unbuffered aqueous suspensions and should be neutralized or accounted for in stability protocols.
Quarantine and reject-stream control are mandatory for this material. The powder should be stored away from strong acids, oxidizing agents, and reducing atmospheres that could generate elemental mercury vapour. It should not be combined with metallic aluminium, magnesium, or zinc in acidic aqueous media, because reduction can liberate elemental mercury and create operator exposure risk. Milling and blending suites should operate under negative-pressure dust collection with HEPA filtration; dry sweeping should be replaced by wet vacuuming or disposable wipes. In food-producing species, regulatory acceptance is highly restricted because mercury residues are not assigned a routine maximum residue limit in edible tissues in major jurisdictions. Published data for this specific veterinary-grade configuration is limited; therefore each batch intended for a new species or route must be supported by route-specific toxicological review and residue-control documentation. Waste streams containing the powder or finished product must be classified as mercury-containing waste and managed under local hazardous-waste regulations.