| HS Code | 759306 |
| Product Name | Isophane Insulin Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions |
| Api Name | Isophane Insulin |
| Synonyms | NPH Insulin; Neutral Protamine Hagedorn Insulin; Insulin Isophane |
| Cas Number | 53027-39-7 |
| Molecular Formula | C257H383N65O77S6 (insulin component) |
| Molecular Weight | 5807.57 g/mol (insulin component) |
| Grade | Veterinary Grade |
| Appearance | White to off-white powder or sterile suspension |
| Solubility | Practically insoluble in water; soluble in dilute acids and alkalis |
| Shelf Life | 24 to 36 months when stored as directed |
| Packaging | Sterile vials, ampoules, pre-filled syringes, bulk containers |
| Dosage Forms | Tablets, Injections, Capsules, Powders, Granules, Premix, Solutions |
| Target Species | Dogs, cats, and other veterinary species as prescribed |
| Therapeutic Category | Antidiabetic hormone; intermediate-acting insulin |
| Prescription Status | Veterinary prescription only |
| Purity | ≥95% (typical API specification) |
| Hs Code | 29371900 |
As an accredited Isophane Insulin 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 | Packaging: 25 kg sealed fiber drums with moisture-resistant double polyethylene liners, clearly labeled, for Isophane Insulin Veterinary Grade API. |
| Container Loading (20′ FCL) | Container loading (20′ FCL): Isophane Insulin Veterinary Grade API for tablets, injections, capsules, powders, granules, premix, solutions; palletized, labeled, sealed, dry-stored. |
| Shipping | Isophane Insulin Veterinary Grade API ships via qualified cold-chain couriers, generally at 2–8°C for injections/solutions, with form-specific conditions for tablets, capsules, powders, granules, and premix. Use sealed, tamper-evident, UN-compliant insulated packaging with temperature monitors, desiccants, and SDS/CoA documentation. Avoid freezing, heat, light, and delays. Secure handling per applicable regulations. |
| Storage | Store Isophane Insulin Veterinary Grade API in tightly sealed, light-resistant containers under refrigeration at 2–8°C. Protect from freezing, heat, and direct sunlight. Keep powders and granules dry; keep solutions, suspensions, and premixes sterile, upright, and avoid vigorous shaking. Maintain controlled inventory, segregate from incompatible substances, and follow the manufacturer’s SDS. |
| Shelf Life | Veterinary isophane insulin API: typically 24–36 months refrigerated (2–8°C), protected from light; reconstituted/diluted forms have shorter shelf life. |
In sterile injectable contract manufacturing for companion animal diabetes therapy, isophane insulin veterinary grade API is quarantined under 21 CFR 211.80 until identity, purity, and potency release against a qualified reference standard are completed using USP <121> insulin bioassay plus a validated reversed-phase HPLC method under USP <621>. The API is not processed into tablet, capsule, granule, powder, or premix formats because the peptide undergoes rapid acid hydrolysis in gastric fluid and intestinal peptidase clearance before reaching systemic circulation; those oral routes have no current veterinary insulin product recognized in dog or cat populations. Formulation addition ratio is stated in international units per millilitre rather than weight percent because the active entity is the isophane crystalline complex, not soluble insulin alone: a 100 IU/mL suspension contains approximately 3.5 mg/mL insulin, with protamine sulfate addition in the range of 0.30–0.40 mg per 100 IU and zinc chloride adjusted from 0.20–0.50 mg per 100 IU depending on crystal aspect ratio response. Downstream production begins with dissolution of the API in acidified water at pH 2.5–3.0 containing zinc, sterile filtration through a 0.22 µm PVDF sterilizing-grade filter, and aseptic precipitation via controlled mixing with sterile protamine sulfate and phosphate buffer at 12–18 °C, final pH 7.2–7.4. The crystal slurry is passed through a rotor-stator homogenizer until laser diffraction D50 is within 2–6 µm, held in a jacketed vessel at 2–8 °C, and filled aseptically into Type I glass vials or cartridges under EU GMP Annex 1 and 21 CFR 210/211. Terminal finished dosage forms include 40 IU/mL and 100 IU/mL sterile injectable suspensions for multi-dose vials and 3 mL cartridge systems intended for veterinary prescription administration.
| Release check | Standard or regulation | Boundary |
|---|---|---|
| Sterility | USP <71> | No growth after 14 days |
| Bacterial endotoxins | USP <85> | Limit derived per maximum veterinary dose/kg |
| Particulate matter | USP <788> | Light obscuration count per SVI |
| Visible particles | USP <790> | Essentially free |
| pH | USP <791> | 7.0–7.5 |
| Uniformity of dosage units | USP <905> | Acceptance value ≤ 15.0 |
The protamine-to-insulin ratio in development batches does not act as a simple mass percentage; it changes the crystal habit of the isophane precipitate by shifting the balance between basal plane growth and prismatic face growth. In pilot-scale crystallisation, protamine sulfate is added in dose-response series of 0.25 mg, 0.35 mg, and 0.50 mg per 100 IU insulin while zinc chloride is fixed at 0.30 mg per 100 IU; the resulting suspensions show measurable differences in aspect ratio and sedimentation volume under ISO 13320:2020 laser diffraction and static image analysis. The applicable development standards are USP <621> for related proteins, USP <121> for biological activity, and ICH Q1A(R2) for stress study design; when the target species-specific bioequivalence model is not yet validated in a regulatory dossier, published data for this specific configuration is limited and the batch record should be treated as the primary process definition. Downstream production for these experimental systems uses a jacketed crystalliser with pH-stat control at 12–18 °C, a peristaltic addition pump delivering protamine sulfate at 0.5–2.0 mL/min, and an aseptic rotor-stator shear pass at 10,000–15,000 rpm for 30–60 seconds before transfer to a holding vessel at 2–8 °C. Terminal output types are not commercial finished preparations; they are pilot-scale crystal suspensions, formulation development stability batches, and photo-resuspension evaluation samples used to set the final particle size specification for sterile injectable manufacture.
Veterinary compounding pharmacies prepare patient-specific isophane insulin suspensions from bulk API under FDA CPG Sec. 608.400 Compounding of Drugs for Use in Animals, with state board of pharmacy sterile compounding rules and, where adopted, USP <797> aseptic technique benchmarks for injectable preparations. The formula addition ratio for compounded preparations is not increased linearly with body weight; a 100 IU/mL master suspension is diluted with sterile isotonic vehicle to concentrations such as 1 IU/mL or 10 IU/mL, and the prescribed dosing volume is calculated from the target dose of 0.25–0.5 IU/kg body weight administered twice daily in dogs, with cat doses adjusted from 0.25 IU/kg every 12 hours under serial blood glucose monitoring. Downstream production occurs in an ISO Class 5 laminar airflow hood using vented vial adapters, swabbed rubber stoppers, and low-protein-binding polypropylene syringes; the precipitated crystal cake is resuspended by rolling the vial between palms 20–30 times without shaking, because shaking introduces air and shears the isophane crystal lattice into aggregates that can fail USP <790> visible particulate inspection. Terminal output types are amber glass vials or sterile polypropylene syringes containing patient-specific concentrations, labeled with beyond-use dates derived from USP <797> risk levels, and intended for immediate or short-term veterinary administration.
For quality control laboratories that release imported veterinary insulin API, the compound is used as a secondary reference standard and system suitability material rather than as a formulation input. The applicable quality system is ISO/IEC 17025:2017, with clause 7.2 governing method validation and clause 6.2 governing staff competence, while ISO 17034:2016 governs the production of certified reference materials. The addition ratio for standard preparation is based on gravimetric dissolution of a pre-dried sample in 0.01 M hydrochloric acid at approximately 1.0 mg/mL protein, followed by quantitative dilution to 0.1 mg/mL for reversed-phase system suitability; each standard is potency-assigned against a compendial isophane insulin standard under USP <121> and stored in low-protein-binding polypropylene vials at 2–8 °C. Downstream analytical production includes RP-HPLC on a C18 column with detection at 214 nm, size-exclusion HPLC for high-molecular-weight proteins, and capillary electrophoresis for desamido and other related protein impurities; the chromatographic system is qualified under USP <621> with tailing factor from 0.8 to 1.5 and resolution not less than 2.0 from the nearest related impurity. Terminal output types include certified reference standards, impurity marker solutions for high-molecular-weight protein and desamido insulin, and system suitability mixtures used for injectable product release testing across multi-day analytical sequences.
Because zinc-m-cresol partitioning between the aqueous continuous phase and the isophane crystal surface controls both preservation and crystal solubility, accelerated stability protocols for veterinary isophane insulin suspensions must be designed as chemical kinetic studies rather than simple storage hold checks. The applicable stability framework is ICH Q1A(R2) and VICH GL3 for veterinary drug substances, with photostability evaluated under ICH Q1B and antimicrobial effectiveness under USP <51>. The formula addition ratio for preservative in the continuous phase is set at total phenol plus m-cresol in the range 2.0–2.5 mg/mL; if m-cresol drops below 1.8 mg/mL because of adsorptive loss onto hydrophobic vial closures or partition into the crystal phase, USP <51> challenge organisms may exceed acceptance criteria. Downstream production for stability batches includes aseptic filling into Type I glass vials with halobutyl stoppers, storage at 5 ± 3 °C for long-term, 25 ± 2 °C/60% RH for accelerated, and 30 ± 2 °C/65% RH for intermediate conditions, with pull points at 0, 3, 6, 9, 12, 18, and 24 months; forced degradation samples are exposed to 40 °C/75% RH and pH extremes to identify desamido insulin and high-molecular-weight protein formation. Terminal output types are stability-labeled injectable suspensions, unstressed control vials, and forced-degradation reference lots used to validate the release and shelf-life specification under real-time veterinary distribution conditions.
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Isophane insulin veterinary grade is an intermediate-acting crystalline insulin API manufactured by co-crystallization of insulin with protamine sulfate and zinc chloride in a phosphate-buffered aqueous system. The product model is the NPH-type suspension intermediate, supplied as a concentrated slurry, a compacted solid, or a spray-dried/lyophilized intermediate for subsequent formulation into injections, powders, granules, premix, tablets, capsules, and solutions. The NPH crystal lattice moderates subcutaneous dissolution after injection; however, tablet and capsule presentations require additional peptide-stability engineering because native insulin is degraded by gastric pepsin and intestinal brush-border proteases before pharmacologically relevant absorption can occur. The API release specification includes a potency window of 95.0%–105.0% of label claim determined by liquid chromatography, with related-protein and protamine-zinc stoichiometry controls aligned to current veterinary pharmacopoeial expectations and VICH GL18 residual-solvent limits. Registered veterinary injections are commonly presented at 40 IU/mL for companion-animal dosing or 100 IU/mL for multi-species use, while the API itself is supplied at higher solids content for further compounding.
Production-scale filling of NPH-type suspensions uses positive-displacement recirculation rather than high-shear rotor-stator mixers. Batches filled from unrecirculated tanks exhibit potency stratification because protamine-zinc crystals settle at a rate governed by crystal size distribution and vehicle viscosity. The filling-line headspace is kept under nitrogen, and dissolved oxygen is monitored by polarographic probe as an oxidation-control parameter for labile amino-acid side chains. Subvisible particles are measured by light obscuration per Ph. Eur. 2.9.19 and USP <788>, and crystal morphology is checked by light microscopy because high-shear processing can fragment the NPH lattice and increase supernatant protamine. Multi-dose vial preservative systems, typically phenol or m-cresol, are validated by preservative efficacy testing per Ph. Eur. 5.1.3 and USP <51> to ensure that preservative partitioning into the crystal surface does not strip protamine from the lattice.
At release, crystal size distribution is measured by laser diffraction per Ph. Eur. 2.9.31; the acceptable span is justified by syringeability and sedimentation rate. X-ray powder diffraction is used to differentiate the NPH crystalline phase from amorphous insulin and zinc-only crystals because the crystal form affects dissolution and protamine retention. These controls are included in the master batch record to reduce batch-to-batch variance in veterinary injection resuspendability. Published data for oral solid dosage forms of isophane insulin in veterinary species is limited, so powder, granule, tablet, capsule, and premix claims require product-specific stability and bioavailability justification.
The defining difference is the presence of protamine. In NPH systems, protamine and zinc form a poorly soluble insulin complex at physiological pH, prolonging release after subcutaneous injection without reliance on the acetate-buffered zinc equilibrium used in lente formulations. This chemical distinction has a compounding consequence: NPH suspension can be drawn into the same syringe as soluble insulin for pre-mixed doses, subject to gentle inversion and immediate administration. Lente suspensions are less tolerant of this practice because the excess zinc can bind soluble insulin and shift the intended time-action profile. The phosphate buffer capacity of the NPH vehicle is therefore specified and controlled; deviation outside the monograph pH range accelerates dissolution of the protamine-zinc lattice or promotes aggregation of insulin fibrils. The pH acceptance range is checked on each batch per Ph. Eur. 2.2.3 and USP <791>.
Powder and granule intermediates for tablet, capsule, premix, and oral-powder applications are milled and sieved under controlled humidity. Reducing sugars are avoided in direct compression because the primary amino groups of insulin and protamine can form Maillard adducts under compaction heat; microcrystalline cellulose and dicalcium phosphate dihydrate are used as diluents in compatibility screens. Residual moisture is determined by Ph. Eur. 2.5.32, with the acceptance limit established from stability data. Tablet and capsule presentations are not the primary route of veterinary glycaemic control; peptide bioavailability across the intestinal mucosa is low and inconsistent without specialised permeation or enteric-coating systems.
The certificate of analysis contains the following release attributes. Acceptance limits follow the current monograph for isophane insulin suspension unless otherwise justified by veterinary product registration. Potency is expressed in international units per millilitre or per milligram of dried substance, with liquid chromatography validated for specificity against desamido and high-molecular-weight impurities. Elemental impurity control follows ICH Q3D; residual solvent control follows VICH GL18; and TSE risk control follows Ph. Eur. 5.2.8.
| Attribute | Method/standard | Acceptance basis |
|---|---|---|
| Identification | Ph. Eur. 2.2.29/USP <621> | Retention time congruence with insulin isophane reference standard |
| Potency | Ph. Eur. 2.2.29 | 95.0%–105.0% label claim |
| Related proteins | Size-exclusion HPLC | High-molecular-weight fraction within monograph limit |
| Protamine content | Reverse-phase HPLC | Reportable against approved stoichiometric window |
| Zinc content | ICP-OES, USP <233> | Reportable against approved stoichiometric window |
| pH | Ph. Eur. 2.2.3/USP <791> | Suspension pH within monograph range |
| Sterility | Ph. Eur. 2.6.1/USP <71> | No microbial growth after incubation |
| Bacterial endotoxins | Ph. Eur. 2.6.14/USP <85> | Endotoxin limit defined by route and dose |
| Particulate matter | Ph. Eur. 2.9.19/USP <788> | Subvisible particle criteria for injections |
| Residual moisture | Ph. Eur. 2.5.32 | Validated limit from stability data |
Because the NPH crystal lattice contains protamine, release assays include protamine integrity and binding capacity. A shift in supernatant protamine after centrifugation indicates crystal weakening and predicts accelerated sedimentation; this is monitored during storage at 2°C–8°C and during short-term excursions at 25°C. Stability data are generated under VICH GL3 and include potency, pH, related proteins, zinc-protamine binding, and resuspendability. If an oral solid dose or premix is requested, stability protocols add moisture uptake, compaction-induced crystal changes, and dissolution in physiologically relevant buffers. Published data for oral isophane insulin in veterinary species is limited.
Insulin suspensions cannot be autoclaved without loss of potency and protamine release; therefore sterile injection manufacture uses aseptic crystallisation and filling. The API slurry is passed through a 0.22 μm sterilising-grade filter only when the crystal size is below the filter challenge threshold; otherwise, the sterile crystalline intermediate is prepared by aseptic co-precipitation from filtered insulin and protamine solutions. Aseptic processing environments are qualified according to Ph. Eur. 5.1.1 and USP <1116>, with media-fill verification of filling-line interventions and glove integrity. Gamma irradiation of dried NPH solid at sterilising doses is expected to produce radiolytic aggregates and reduce potency; published data for this specific configuration is limited, but radiation sensitivity is documented for peptide APIs. Dry-heat and autoclave cycles are incompatible with peptide stability. Aseptic processing therefore remains the only established sterilisation route for this veterinary peptide API.
Isophane insulin NPH is an intermediate-acting suspension, whereas insulin glargine is a soluble acidic solution that precipitates after subcutaneous injection and insulin detemir is a soluble acylated insulin analogue with albumin binding. These products are not directly substitutable; the API physical form, pH, and dilution requirements differ. For veterinary grade isophane, the suspension is drawn from the vial and gently resuspended before administration; syringe-to-syringe transfer into saline or other diluents is not permitted unless validated by compatibility studies. Glargine and detemir protocols are supported by separate veterinary pharmacokinetic data and are not interchangeable with NPH in the same dosing regimen. Published veterinary pharmacokinetic comparisons show inter-animal variability in duration; no single NPH time-action curve is representative across canine and feline populations. The veterinary API is also distinguished from human-recombinant insulin APIs by the need to control species-specific TSE raw-material sources and by the frequent use of 40 IU/mL companion-animal presentations rather than the 100 IU/mL human diabetes convention.