| HS Code | 407500 |
| Product Name | Rivanol Solution Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions |
| Veterinary Grade | Yes, API intended for veterinary pharmaceutical manufacturing |
| Api Name | Ethacridine lactate monohydrate (Rivanol) |
| Chemical Name | 6,9-Diamino-2-ethoxyacridine lactate monohydrate |
| Cas Number | 1837-57-6 |
| Molecular Formula | C18H21N3O4·H2O |
| Molecular Weight | 361.39 g/mol |
| Appearance | Yellow crystalline powder; when prepared as a solution it forms a clear yellow to amber liquid with fluorescence |
| Solubility | Soluble in hot water; sparingly soluble in ethanol; practically insoluble in ether; freely soluble in aqueous acidic media |
| Ph | 5.5 - 6.5 for a 1% w/v aqueous solution |
| Assay | 98.0% - 101.0% on dried basis |
| Loss On Drying | 4.0% - 6.0% (corresponding to monohydrate) |
| Storage | Store in tightly closed, light-resistant containers in a cool, dry place; protect from heat and moisture |
| Applicable Dosage Forms | Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions |
As an accredited Rivanol Solution 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-protected, tamper-proof containers. Quantity: 25 kg per drum. Suitable for veterinary API formulations including tablets, injections, capsules, powders, granules, premix, solutions. |
| Container Loading (20′ FCL) | 20′ FCL: Drums/pails on pallets, secured, labeled, segregated. Ventilated, dry container; no contamination. UV-protected packaging. |
| Shipping | Rivanol Solution (Ethacridine Lactate) is a veterinary-grade active pharmaceutical ingredient supplied in liquid form. It is used for manufacturing tablets, injections, capsules, powders, granules, premixes, and solutions. Shipped in sealed, leak-proof containers under controlled conditions; store away from sunlight, heat, and incompatible materials. Transport requires compliance with chemical safety regulations. |
| Storage | Store in tightly sealed, light-resistant containers in a cool, dry, well-ventilated area. Protect from direct sunlight, moisture, and excessive heat. Keep away from oxidizing agents and incompatible materials. Maintain temperatures between 15–25°C unless otherwise specified. Ensure container integrity to prevent contamination, and follow all applicable veterinary pharmaceutical regulations for safe handling and storage. |
| Shelf Life | Shelf life is 24 months from manufacture when stored in airtight, light-resistant containers below 25°C, protected from moisture. |
In the high-shear granulation suite, Rivanol Solution Veterinary Grade API is introduced as the active granulating liquid for bovine intrauterine tablets and boluses. A dry premix of microcrystalline cellulose, lactose monohydrate, croscarmellose sodium, and povidone K 30 is charged into a 600 L top-driven high-shear mixer equipped with a bottom impeller and side chopper. The concentrated ethacridine lactate solution is diluted with purified water to a working concentration of 0.5–2.0% w/v and buffered to pH 4.0–5.0 with citric acid/sodium citrate before it is metered through a peristaltic pump at 0.4–0.8 kg/min per 100 kg dry mass. Addition rate is constrained by local overwetting; if the wet mass exceeds 12% w/w moisture, screen blinding and erratic tablet weight occur. Wet mass moisture is held at 8–12% w/w by Ph. Eur. 2.2.32, after which the mass is wet-milled through an oscillating granulator with a 2.0 mm square mesh. Fluid-bed drying at inlet air temperature 55–65°C reduces residual moisture to 1.0–2.0% w/w. Dry granules are screened through 1.0 mm, lubricated with magnesium stearate 1.0% w/w in a bin blender at 12 rpm for 5 min, and compressed on a rotary tablet press at 12–20 kN. Tablet hardness is controlled at 80–120 N, friability below 1.0% by Ph. Eur. 2.9.7, and disintegration below 15 min in water at 37±2°C by Ph. Eur. 2.9.1. Large-animal boluses use 25 mm flat-faced concave tooling and 3–5 g target mass. The compressed unit is administered by sterile catheter into the uterine lumen; published dissolution data in bovine uterine fluid are limited, so release-rate claims require a veterinary bioequivalence study. Granulation must avoid alkaline buffers, soap residues, and chloride concentrations above physiological isotonicity because free-base precipitation at pH above 6.0 produces yellow particulates and causes dose-uniformity failure.
Terminal sterilisation of ethacridine lactate injection fluids is constrained by pH-dependent hydrolytic degradation and light sensitivity. The injectable solution is prepared by diluting the API concentrate to 0.1% w/v in water for injection, with pH adjusted to 3.5–5.0 using acetic acid or citrate buffer. The solution is filtered through a 0.22 μm PVDF membrane, filled into Type I borosilicate glass ampoules or polypropylene vials under Grade A laminar airflow, and sealed under nitrogen purging so that headspace oxygen remains below 0.5% v/v. If terminal sterilisation is selected, filled containers are autoclaved at 121°C for 15 min with F0 ≥ 8 min. Published forced-degradation data for this specific veterinary-grade solution are limited; a candidate sterilisation cycle must therefore be confirmed by acid/base hydrolysis studies at pH 3.0, 5.0, and 7.0. Visual inspection of yellow colour intensity at 420 nm is used as a screening indicator, while assay is performed by liquid chromatography according to Ph. Eur. 2.2.29. Sterility testing follows Ph. Eur. 2.6.1; for intrauterine instillation in cattle, endotoxin is controlled at ≤ 0.5 EU/mL. This injectable solution is intended for local uterine lavage or wound irrigation, not for systemic intravenous administration. Containers are stored below 25°C and protected from light because acridine derivatives degrade under UV-A exposure. Contact surfaces are 316L stainless steel or borosilicate glass; copper, iron, and chlorine-releasing disinfectants must be excluded from the filling line.
On farms where clean water is not available, field reconstitution of wound irrigation powders requires low-dust granule morphology and rapid cold-water solubility. Concentrated Rivanol Solution Veterinary Grade API is sprayed onto a preheated carrier of maltodextrin, mannitol, or lactose monohydrate in a fluid-bed granulator. The carrier is pre-sieved through 0.45 mm mesh before loading. Inlet air temperature is maintained at 45–55°C; product temperature remains below 42°C to avoid caramelisation of maltodextrin and thermal degradation of ethacridine lactate. Spray rate is set at 6–10 g/min/kg carrier. Final granules contain 0.05–0.2% w/w ethacridine lactate, with bulk density 0.55–0.75 g/mL and tapped density 0.70–0.90 g/mL. Dissolution time in water at 20±2°C is below 60 s. Sachets are filled under low-humidity conditions; residual moisture is ≤ 1.5% w/w by Ph. Eur. 2.2.32. Sodium chloride is omitted from the formulation because chloride concentrations above 0.9% w/v can reduce solubility. The finished powder is intended for dilution to 0.05–0.1% w/v before irrigation of contaminated wounds, umbilicus, or post-surgical cavities in cattle, horses, and companion animals. Hard water with calcium or magnesium hardness above 250 ppm as CaCO₃ should be replaced with purified water; polyvalent cations can promote precipitation. Metallised sachets protect the granulate from light, and storage at 15–25°C supports the assigned shelf life, with accelerated stability evaluated at 40°C/75% RH for 6 months per VICH GL3.
Medicated drinking water premix lines in swine and poultry operations introduce particulate segregation risks that require geometric dilution of the API solution onto a soluble or dispersible carrier. The concentrate is first adsorbed onto dextrose monohydrate or lactose in a 500 kg double-cone blender; a 1:10 premix is prepared by spraying 50 kg of diluted API solution onto 450 kg carrier with drum rotation at 8–12 rpm and spray-bar pressure 1.0–2.0 bar. After 20 min blending, the 1:10 intermediate is discharged through a 0.5 mm screener and diluted 1:10 again to obtain a target ethacridine lactate concentration of 0.1–0.25% w/w in the final premix. Content uniformity is controlled below 5.0% RSD using HPLC per Ph. Eur. 2.2.29 on 10 sampling points. In drinking water, the final premix is dissolved at 0.5–1.0 kg per 1000 L to deliver 0.5–2.5 mg/L ethacridine lactate. Turbidity, pH 3.5–5.5, and absence of foam are inline control parameters. The medicated water system must not contain chlorine-based disinfectants at concentrations above 0.2 mg/L free chlorine because acridine dyes undergo oxidative bleaching and assay loss. Administration is restricted to the prescribed veterinary indication; published pharmacokinetic data for oral ethacridine lactate in food-producing species are limited, so withdrawal periods must be established in accordance with Regulation (EU) 2019/6 and Commission Regulation (EU) 37/2010 where applicable. The blend is packaged in HDPE drums with polyethylene liners and stored below 25°C; moisture pickup during storage is controlled below 0.5% w/w per Ph. Eur. 2.2.32.
| Dosage-route conversion | Critical process step | Process limit | Reference method |
|---|---|---|---|
| Intrauterine tablet/bolus | High-shear wet granulation and fluid-bed drying | LOD 1.0–2.0% w/w; hardness 80–120 N | Ph. Eur. 2.2.32, 2.9.7 |
| Injectable solution | Sterile filtration and terminal sterilisation | pH 3.5–5.0; F0 ≥ 8 min | Ph. Eur. 2.6.1 |
| Wound irrigation powder/granulate | Fluid-bed spray adsorption | Product temperature ≤ 42°C; dissolution <60 s | Ph. Eur. 2.2.32 |
| Medicated drinking water premix | Geometric dilution in double-cone blender | Content uniformity ≤ 5.0% RSD | Ph. Eur. 2.2.29 |
| Capsule/pellet | Wurster spray layering and capsule filling | Product temperature 38–42°C; fill weight ≤ 3.0% RSD | Ph. Eur. 2.9.1 |
For dose banding and bitter-taste masking in companion animal and calf therapy, capsule filling of low-dose ethacridine lactate formulations is governed by the flow function coefficient of spray-layered sugar spheres. Concentrated API solution is diluted to 1.0–2.0% w/v and sprayed onto 500–600 μm microcrystalline cellulose spheres in a Wurster fluid-bed coater. Product temperature is held at 38–42°C, spray rate at 8–12 g/min/kg core material, and atomising air pressure at 1.5–2.5 bar. A 10% w/w ethacridine lactate layer is built up in successive spray cycles, followed by a protective hydroxypropyl methylcellulose seal coat of 1.0–2.0% w/w weight gain. The dried pellets are filled into hard gelatin or hydroxypropyl methylcellulose capsules on a dosing-disc capsule filler at 30,000–60,000 capsules/h. Flow function coefficient of the pellet bed should exceed 4.0 to avoid rat-holing and fill-weight variation above 3.0% RSD. Capsule disintegration time is tested at 37±2°C by Ph. Eur. 2.9.1; enteric-coated pellets, if used, must meet the acid stage of Ph. Eur. 2.9.1 for 2 h in 0.1 M HCl without release, followed by buffer-stage release at pH 6.8. Taste masking is confirmed by an in vitro release test; because the bitter free base is less soluble at pH above 6.0, release in saliva should be below 10% within 5 min. Published data for oral absorption of ethacridine lactate in target species are limited; the capsule formulation is generally intended for local gastrointestinal antiseptic action rather than systemic therapy. Finished capsules are stored below 25°C in amber glass or alu-alu blister packaging.
During transfer of concentrated API solution from 200 L stainless steel drums to aseptic filling lines, a series of pressure and filtration controls is applied in veterinary solution manufacturing. The concentrate is received with assay 10–20% w/v ethacridine lactate, pH 3.0–5.0, and bioburden ≤ 100 CFU/mL. Transfer uses positive-displacement pumps with EPDM or PTFE diaphragms; centrifugal pumps are avoided to minimise shear-induced foaming. Filtration through 0.45 μm prefilter and 0.22 μm sterile-grade cartridge is performed under nitrogen pressure 0.5–1.0 bar. Filling lines use 316L stainless steel with surface roughness Ra ≤ 0.8 μm; all fittings are polished. The diluted solution is filled into LDPE or HDPE bottles at 100 mL, 250 mL, 500 mL, and 1000 mL volumes. Inline UV absorbance at 420 nm monitors concentration; absorbance variation exceeding ±5% triggers automatic diversion. Container closure integrity is tested by vacuum decay per ASTM F2338-09. The label includes species-specific directions for dilution to 0.05–0.1% w/v before instillation, irrigation, or wound flushing. Avoid contact with hypochlorite, iodine-based disinfectants, and strong alkalis; line cleaning after use is performed with 0.1 M citric acid solution followed by purified water. Because ethacridine lactate binds to glass and some plastics, dedicated transfer lines are recommended; batch-to-batch carryover is assessed by swab recovery studies with acceptance ≤ 10 ppm residual API.
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Rivanol Solution Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions is the compendial active pharmaceutical ingredient ethacridine lactate monohydrate, 6,9-diamino-2-ethoxyacridine lactate monohydrate, CAS 6402-23-9, molecular formula C18H23N3O5 and relative molecular mass 361.39 g/mol. The material is released as a yellow crystalline powder with the acridine chromophore responsible for visible absorption in the 400–450 nm region. Unlike a finished antiseptic solution, the veterinary-grade API is supplied as a solid monohydrate for downstream formulation into the dosage forms named in the product description; the term “Solution” refers to the intended aqueous administration form and to the API’s primary use as a water-soluble active. Specification alignment with the Ph. Eur. monograph 1507 for ethacridine lactate monohydrate and current ICH Q7 good manufacturing practice are standard for bulk release.
Release testing includes assay by anhydrous titration with perchloric acid, with a typical acceptance range of 98.5–101.0% on the dried basis. Loss on drying is controlled within 4.0–5.5% to maintain the monohydrate crystal lattice; sulfated ash does not exceed 0.1% under Ph. Eur. 2.4.14, and related substances by liquid chromatography are limited to total impurities not more than 1.0%. Elemental impurities follow ICH Q3D with parenteral routes triggering lower permitted daily exposures for cadmium, lead and arsenic than oral or topical routes. Residual solvents, where ethanol may be present from recrystallisation, are controlled under ICH Q3C with ethanol as a Class 3 solvent at not more than 5000 ppm. The powder should be stored at 15–25°C in tight, light-resistant containers; the monohydrate is stable for 24 months when protected from moisture excursions above 60% RH.
Because the product is an active pharmaceutical ingredient rather than a finished veterinary medicinal product, no single model number appears in pharmacopoeial monographs. Batch release is identified by the manufacturer’s lot number, the compendial designation and the country-specific veterinary drug approval file. Buyers should request a certificate of analysis and material safety data sheet before use.
Ethacridine lactate monohydrate differs from halogenated and biguanide antiseptics because its activity is not based on free halogen release or general membrane lysis but on planar acridine intercalation into microbial nucleic acid. Published comparative data indicate that this mechanism gives more selective coverage than chlorhexidine digluconate, with higher activity against Gram-positive cocci and less robust activity against Pseudomonas and spore-forming organisms. The presence of the lactate counterion provides a pH range in aqueous solution of 4.5–6.5 at 0.1% w/v, which is compatible with many veterinary irrigation protocols but insufficiently acidic to prevent hydrolysis of the acridine ring under terminal heat.
The light sensitivity of the acridine chromophore is a critical operational boundary. Aqueous solutions exposed to unfiltered daylight in clear glass develop measurable photodegradation within 12–24 h; amber glass or opaque fill lines are required for bulk solution holding. The compound is also sensitive to strong oxidising agents; hydrogen peroxide and sodium hypochlorite destroy the yellow chromophore and should not be used for sanitising equipment holding ethacridine lactate. In compounding, the API should not be triturated with strong alkalis because the free base precipitates and the lactate salt is neutralised.
| Property | Ethacridine lactate monohydrate | Chlorhexidine digluconate | Povidone-iodine |
|---|---|---|---|
| Primary mechanism | Acridine DNA intercalation | Membrane disruption | Oxidative halogenation |
| Antimicrobial spectrum | Gram-positive bacteria, some fungi; weaker against Gram-negative bacteria and spores | Bacteria, yeasts; limited sporicidal activity | Bacteria, fungi, viruses, spores |
| Activity in presence of serum or organic soil | Moderate retention | Reduced activity | Markedly reduced activity |
| Staining propensity | Yellow to orange on skin and instruments | Minimal | Transient iodine colour |
| Thermal stability in aqueous solution | pH-dependent hydrolysis; protect from light | Stable at acidic pH | Unstable at alkaline pH and elevated temperature |
Within the acridine family, ethacridine lactate monohydrate is a single defined entity, unlike acriflavine, which is a mixture of 3,6-diamino-10-methylacridinium chloride and proflavine. The 2-ethoxy substituent in ethacridine raises lipid solubility relative to proflavine and reduces the irritancy observed with simple aminoacridines; the lactate salt avoids the chloride counterion, which can promote corrosion in stainless steel. These differences matter in formulation because ethacridine lactate monohydrate can be incorporated into aqueous vehicles without the precipitation that occurs when proflavine salts are mixed with chloride-rich buffers.
Manufacture of tablets and capsules is limited by the crystal habit of ethacridine lactate monohydrate. The plate-like crystals flow poorly through gravity-driven feeds, so direct compression requires a force-feeder equipped with rotating stirrer bars and an acceptably low lubricant concentration. Magnesium stearate above 0.5% w/w delays disintegration beyond 15 min in the disintegration apparatus and reduces tensile strength, while colloidal silicon dioxide at 0.2–0.5% w/w improves flow without excessive particle-size interference.
Wet granulation with aqueous binders is generally avoided because partial dissolution and drying produce needle-like recrystallised material that increases punch-filling variability and causes picking. Dry granulation by roller compaction is preferred for ethacridine lactate tablets; ribbon density is maintained between 1.10 and 1.25 g/cm³, and milled granules are screened through a 0.8 mm sieve. Hardness of the final tablet is typically specified between 60 and 80 N for intrauterine administration, but veterinary product developers must confirm disintegration in the target environment because compendial disintegration in water does not predict behaviour in viscous uterine fluid.
For oral powders, granules and premixes, stepwise geometric dilution is mandatory because the API is active at low concentrations and segregation occurs if coarse crystalline material is added directly to feed. A first preblend at 10% w/w API on lactose monohydrate is prepared by tumble blending for 20 min, followed by a second preblend at 1% w/w and final feed with a coefficient of variation not exceeding 5.0%. The final premix should be tested for uniform distribution according to the medicated feed sampling scheme adopted by the relevant Veterinary Good Manufacturing Practice guideline.
Hard gelatin capsule filling is performed with dry-granulated material with a particle size d90 below 180 µm to avoid bridging in the dosator. The monohydrate is hygroscopic above 60% RH; open handling in uncontrolled humidity should be limited to 8 h or less. Capsule content uniformity is evaluated by USP chapter 905, with the acceptance value determined by the labelled dose and batch size; segregation during capsule filling is monitored by sampling at 10 evenly spaced intervals across the run.
On production-scale rotary presses equipped with paddle force-feeders, ethacridine lactate monohydrate tablets containing high lactose loads show a tendency to cap when turret speed exceeds 30 rpm and pre-compression force is below 5 kN. The failure mode is attributed to air entrapment between the plate-like crystals. Raising the pre-compression force to 5–8 kN and reducing turret speed to 20–25 rpm improves tablet hardness and lowers friability below 0.8% after 100 revolutions in the friabilator. Batch-to-batch variance in particle-size distribution from different recrystallisation lots can shift the required compaction force, so roller-compacted granules are preferred when the API fraction exceeds 20% w/w.
| Dosage form | Critical parameter | Control range | Reference method |
|---|---|---|---|
| Tablets | Magnesium stearate | ≤ 0.5% w/w | Disintegration apparatus, USP chapter 701 |
| Tablets | Hardness | 60–80 N | Radial crushing force |
| Capsules | Particle size d90 | ≤ 180 µm | Laser diffraction |
| Injectable solution | pH | 5.0–6.5 | Potentiometric |
| Premix or medicated feed | Blend uniformity RSD | ≤ 5.0% | Near-infrared or HPLC assay |
Injectable solutions are prepared by dissolving ethacridine lactate monohydrate in Water for Injections at 45–55°C with moderate agitation at 150–200 rpm. The solution is cooled to 20–25°C before pH adjustment to 5.0–6.5 with dilute sodium hydroxide or hydrochloric acid. Sterilising filtration through a 0.22 µm polyethersulfone membrane is the preferred method because terminal autoclaving accelerates hydrolytic and oxidative degradation; nylon membranes should be avoided because the planar acridine moiety binds to the membrane and reduces yield.
If terminal sterilisation is unavoidable, the solution is packed in amber Type I glass under a nitrogen headspace and autoclaved at 121°C for 15 min. The pH before autoclaving must remain below 6.5; higher pH values produce rapid colour darkening and visible particulate formation. Post-sterilisation absorbance at 450 nm is monitored as a stability indicator. Published data for terminal sterilisation of ethacridine lactate at concentrations above 0.2% w/v is limited, and aseptic filtration remains the default route for higher-strength injectable products.
Membrane flux decline during sterilising filtration has been observed when the solution is cooled too rapidly below 25°C or when the pH is adjusted above 6.5. The acridine base aggregates as fine needle clusters that deposit on the upstream side of the 0.22 µm membrane and restrict flow. A controlled cooling ramp of 0.5–1.0°C/min and filtration at 25–30°C maintains the monomer-dimer equilibrium in solution and allows 50–70 L/m² throughput before change-out of the membrane cartridge. These values are process guidance from pilot-scale batches and should be qualified for each membrane vendor.
For topical and cavity irrigation, the veterinary API is diluted to 0.05–0.1% w/v in sterile water or normal saline. Solutions should be prepared immediately before use where possible, or stored in amber glass for no more than 24 h. The product is not a high-level sterilant for surgical instruments and should not be used as a substitute for autoclaving or glutaraldehyde-based disinfection. It is incompatible with anionic surfactants, strong oxidisers, and concentrated halide solutions. When these solution formulations are filled into plastic containers, low-density polyethylene and polypropylene are acceptable after extraction testing according to the relevant veterinary drug registration requirements.