| HS Code | 230382 |
| Product Name | Protamine Zinc Insulin Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions |
| Synonyms | PZI, Protamine Zinc Insulin, Insulin Protamine Zinc |
| Molecular Weight | Variable; insulin approx. 5808 Da, protamine approx. 4000-6000 Da, zinc 65.38 Da |
| Appearance | White to off-white powder or sterile suspension |
| Solubility | Sparingly soluble in water; forms suspension; insulin component soluble at appropriate pH |
| Grade | Veterinary Grade API |
| Purity | Typically ≥95% for insulin component; confirm actual value via CoA |
| Dosage Forms | Tablets, Injections, Capsules, Powders, Granules, Premix, Solutions |
| Route Of Administration | Subcutaneous injection is typical for insulin; other listed forms are for veterinary compounding or supply |
| Target Species | Dogs, cats, and other veterinary species as directed |
| Mechanism Of Action | Long-acting insulin; protamine and zinc delay absorption and prolong hypoglycemic effect |
| Therapeutic Class | Antidiabetic; long-acting insulin |
| Shelf Life | Typically 24 months when stored properly |
| Packaging | Amber glass vials, ampoules, sealed containers, or bulk API containers |
| Hs Code | 2937.12 for insulin hormones or 3004.90 for veterinary medicaments depending on form |
| Manufacturer | Various veterinary API suppliers |
| Country Of Origin | Varies by supplier |
| Ph | 7.0-7.5 for typical suspension |
As an accredited Protamine Zinc 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 | Protamine Zinc Insulin Veterinary Grade API: 1 kg, 5 kg, and 25 kg double polyethylene-lined, moisture-resistant fiber drums for all forms. |
| Container Loading (20′ FCL) | 20′ FCL container loading: Protamine Zinc Insulin Veterinary Grade API for tablets, injections, capsules, powders, granules, premix, solutions; palletized, sealed, secured. |
| Shipping | Ship Protamine Zinc Insulin Veterinary Grade API for tablets, injections, capsules, powders, granules, premix, and solutions via validated cold chain at 2–8°C. Use insulated shippers, gel packs, temperature loggers, and secure labeling. Do not freeze; protect from light. Follow IATA/ADR, GDP, and local veterinary transport regulations. |
| Storage | Store Protamine Zinc Insulin Veterinary Grade API in tightly sealed, light-resistant containers under refrigeration at 2–8°C (36–46°F). Protect from freezing, heat, moisture, and light. Keep away from oxidizing agents and contamination. For solutions, premixes, or reconstituted forms, follow manufacturer instructions and use aseptic handling. Maintain secure, labeled inventory with temperature monitoring. Do not exceed stability limits; rotate stock. |
| Shelf Life | Shelf Life: Typically 24–36 months when stored sealed, cool, dry, protected from light; reconstituted or injectable forms require label-specific refrigeration. |
In feline diabetic management, the manufacture of a 40 IU/mL protamine zinc insulin suspension is performed as an aseptic crystallization process rather than as a sterile-fill solution, because the final dosage form is a crystalline suspension that cannot be passed through a 0.22 µm sterilizing filter after the insulin-protamine-zinc complex is formed. The API addition ratio on a dried basis corresponds to 40 IU/mL, equivalent to approximately 1.45 mg/mL of insulin substance when calculated with a nominal potency of 27.5 IU/mg. In the downstream production sequence, bulk veterinary-grade PZI API is first dissolved in an acidic aqueous phase at pH 2.5–3.0, combined with protamine sulfate and zinc chloride, and then neutralized with a buffered phosphate system to pH 6.9–7.4 to induce formation of protamine-zinc-insulin crystals with the slow dissolution profile required for feline glycemic control. The buffer components are sterilized by 0.22 µm polyethersulfone filtration before crystal formation, and the finished suspension is held under low-shear agitation at 100–200 rpm to prevent flocculation without fracturing crystals. Filling is conducted under ISO Class 5 aseptic conditions into depyrogenated 10 mL Type I flint glass multi-dose vials with chlorobutyl rubber stoppers and aluminium seals; container preparation follows 21 CFR 211.94, equipment cleaning is validated under 21 CFR 211.67, and in-process checks are executed per 21 CFR 211.110. Terminal batch release includes sterility testing to USP <71>, bacterial endotoxins to USP <85>, sub-visible particulate matter to USP <788>, visible particulates to USP <790>, and pH to USP <791>. The terminal finished product is a 10 mL U-40 veterinary multi-dose injection refrigerated at 2–8 °C and labelled for subcutaneous administration in cats.
The re-suspendability of protamine zinc insulin in a multi-dose vial is governed by the stoichiometric excess of protamine and zinc relative to insulin, the crystal habit formed during neutralization, and the ionic strength of the aqueous phase. A 40 IU/mL batch is prepared with the same nominal API loading as the feline suspension, but the process window is narrower because excessive zinc addition produces dense, rapidly settling crystals, while insufficient protamine produces fine amorphous aggregates that adhere to vial walls and stopper surfaces. The formulation addition ratio therefore includes a compendially bounded protamine sulfate and zinc chloride input, with final zinc content controlled by a validated atomic absorption or inductively coupled plasma procedure; the API addition remains 40 IU/mL, equivalent to approximately 1.45 mg/mL of insulin substance. Downstream manufacturing after crystallization includes cooling to 2–8 °C with continuous low-shear agitation, followed by aseptic transfer to a jacketed holding vessel equipped with a magnetic stir bar operating at 100–200 rpm to maintain homogeneous crystal distribution without generating fines. Vacuum-stoppered vials are filled under nitrogen or filtered dry air to limit oxidation of the peptide, and fill volume is controlled within ±0.2 mL of the declared volume. Production-scale equipment for this suspension typically includes a rotary piston filler with side-sweep agitation, a dual-head stoppering station, and a modified vial washer capable of handling Type I glass containers without introducing residual alkaline detergent that would alter pH. Release testing for this presentation includes sterility to USP <71>, bacterial endotoxins to USP <85>, resuspendability by a standardized manual inversion cycle, zinc and protamine assays, and sub-visible particulate matter to USP <788>; compendial monographs or marketing authorizations may also require in vivo bioidentity testing by rabbit blood glucose depression. The terminal finished product is a 10 mL U-40 multi-dose PZI injection intended for subcutaneous use in dogs and cats where a longer duration of insulin action is clinically indicated.
| Presentation | Downstream operation | Typical API addition | Critical operational boundary | Relevant standard designation |
|---|---|---|---|---|
| U-40 aqueous suspension injection | Aseptic crystallization and vial filling | 40 IU/mL (1.45 mg/mL insulin equivalent) | No terminal filtration after crystal formation; settling control required | 21 CFR 211.110, USP <71>, USP <85>, USP <788> |
| Lyophilized powder for reconstitution | Freeze-drying and vacuum stopper sealing | 40 IU/mL before drying; reconstitute to 40 IU/mL | Residual moisture control below 2.5%; reconstituted suspension not filterable | ICH Q7, USP <921>, 21 CFR 211.111 |
| Pen cartridge suspension | Cartridge filling with glass bead insertion | 40 IU/mL in 3 mL cartridge | Plunger glide force and dose accuracy at 0.5 U increments | ISO 11608-1:2022, USP <790> |
Aseptic powder dispensing of lyophilized PZI API for veterinary hospital compounding presents a different operational boundary than suspension filling because the dry powder is hygroscopic and electrostatically charged, which creates batch-to-batch variance in gravimetric transfer if relative humidity exceeds 60%. Compounding facilities handling this API operate under USP <797> for sterile preparations, and outsourcing facilities performing batch-scale patient-specific or office-use distribution follow 21 CFR 211 requirements for finished pharmaceuticals. The addition ratio after reconstitution is calculated from the lot-specific API potency; for example, to prepare 10 mL of 40 IU/mL PZI suspension, 400 IU of API is required, which corresponds to 14.5 mg of powder when the lot assay is 27.5 IU/mg. For a lower clinical concentration of 20 IU/mL, the calculated mass is 7.3 mg per 10 mL, but such dilution is accepted only when the chosen vehicle has documented physical stability for the protamine-zinc crystal system. The downstream process is performed in an ISO Class 5 laminar flow hood within an ISO Class 7 buffer room; sterile diluent is added using an 18–21 gauge needle without filtering the reconstituted suspension, and the vial is mixed by gentle rolling rather than shaking to prevent foaming and peptide aggregation. The finished product is a patient-specific or office-use multiple-dose PZI injection, typically dispensed in a 3 mL or 10 mL sterile vial with a client-specific label stating the concentration, beyond-use date, refrigeration requirement at 2–8 °C, and the instruction that the product must be resuspended prior to dose withdrawal.
Canine use of PZI in a pen injector platform requires cartridge filling with a suspended solid, not a true solution, and the 3 mL cartridge must include a glass or stainless steel bead of 2–3 mm diameter to facilitate re-suspension ahead of dose setting. The API addition ratio remains 40 IU/mL, but the fill volume is set at approximately 3.15 mL to permit stopper insertion and the required headspace without trapping air bubbles that affect dose accuracy. Downstream production involves filling Type I clear borosilicate cartridges in an aseptic line, inserting bromobutyl plungers and aluminium seal caps, and loading the finished cartridges into pen injector devices that meet ISO 11608-1:2022 requirements for needle-based injection systems. In-process checks include extractable volume, dose accuracy at 0.5 U increments across a U-40 pen, and plunger glide force measured at a travel speed of 100 mm/min; excessive glide force above the device limit indicates crystal agglomeration at the barrel wall or insufficient siliconization. Release testing includes sterility to USP <71>, bacterial endotoxins to USP <85>, and visible particulates to USP <790>. The terminal finished product is a 3 mL U-40 PZI cartridge for a veterinary reusable pen, intended for dogs receiving twice-daily subcutaneous injections.
Shifting from a liquid suspension to a freeze-dried powder is considered when distribution through regions with unreliable cold-chain infrastructure requires a dosage form that is less sensitive to transient temperature excursion during transport. The API is lyophilized with a matrix of trehalose or mannitol at a solids ratio of API to bulking agent from 1:10 to 1:20, with residual moisture controlled below 2.5% as determined by Karl Fischer titration. Before drying, the liquid blend contains 40 IU/mL PZI; after reconstitution with sterile water for injection, the target potency returns to 40 IU/mL, and the reconstituted suspension is subject to the same settle-and-resuspend behavior as a natively manufactured liquid PZI injection. Downstream production uses 10 mL Type I tubing vials with a liquid fill volume of 2 mL before freeze-drying, and cycle parameters include primary drying at a shelf temperature of −20 °C under chamber pressure of 100–150 mTorr, followed by secondary drying at 25 °C until moisture release meets specification. Compliance includes ICH Q7 for good manufacturing practice for active pharmaceutical ingredients, 21 CFR 211.111 for time limits on production, and residual solvent limits under ICH Q3C. The finished product is a lyophilized PZI veterinary injection that is reconstituted immediately prior to subcutaneous use in client-owned diabetic cats or dogs.
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Protamine Zinc Insulin Veterinary Grade API is supplied as a sterile white to off-white crystalline suspension or lyophilised intermediate. Product designations PZI-VG-40 and PZI-VG-100 denote the nominal insulin activity after reconstitution: 40 IU/mL and 100 IU/mL, respectively. The material is released against potency, protamine-to-insulin molar ratio, zinc-to-insulin molar ratio, pH, particle size distribution after resuspension, bacterial endotoxin, sterility, and subvisible particulate matter. It is intended for processing into injectable suspensions and, with appropriate stabilisation and enteric protection, into solid dosage intermediates such as tablets, capsules, powders, granules, and premixes for veterinary use. The API is not interchangeable with regular insulin, NPH, or lente products without a revised bioequivalence assessment.
PZI-VG-100 is filled into Type I borosilicate glass vials of 10 mL nominal fill. The closure is a chlorobutyl rubber stopper with an aluminium flip-off seal. Unopened vials are stored at 2–8°C protected from light. In-use vials may be held at controlled room temperature for up to 28 days, but repeated temperature cycling above 25°C increases free insulin in the supernatant and alters the depot profile. Before dose withdrawal, the vial is resuspended by gentle inversion 10–20 times. Vigorous shaking introduces air and shears the crystalline particles; this can narrow the particle size distribution and produce faster dissolution after injection.
Protamine zinc insulin contains an excess of protamine sulfate and zinc chloride relative to neutral protamine Hagedorn isophane. This excess stabilises a slowly dissociating crystal lattice with reduced dissolution rate in subcutaneous tissue. In NPH, insulin and protamine are combined at an isophane ratio, yielding intermediate-acting particles; in PZI, the higher zinc content prolongs dissociation and delays release. Lente and ultralente preparations lack protamine and rely on zinc-acetate crystallinity, producing a different dissolution profile and particle morphology. Regular soluble insulin remains in solution and has an immediate time-action profile. The consequence is that PZI has a slower onset and a longer duration than NPH or lente in veterinary patients, but the profile shifts with particle size distribution, crystal form, injection site vascularity, and species-specific subcutaneous pH and temperature.
Because the unit activity is standardised by biological assay, a unit of PZI is not clinically interchangeable with a unit of NPH or lente without re-titration. Published veterinary pharmacokinetic data in diabetic cats document duration of action of 12–24 h after subcutaneous injection; however, the data are product-specific and should not be extrapolated to compounded formulations without validation by a qualified assay.
| Product class | Protamine present | Zinc binding mechanism | Typical in-use presentation |
|---|---|---|---|
| Regular insulin | No | Soluble hexamer | Solution |
| NPH/isophane | Yes, low ratio | Weak zinc-protamine complex | Intermediate suspension |
| PZI | Yes, high ratio | Excess zinc-protamine crystalline lattice | Long-acting suspension |
| Lente/ultralente | No | Zinc-acetate crystal fraction | Long-acting suspension |
The release specification for PZI-VG-100 sterile suspension requires resuspendability without irreversible agglomeration after storage at 2–8°C. The pH window is 7.0–7.4; outside this range, the crystalline fraction may dissolve or amorphous precipitate forms, shifting dissolution rate. Zinc and protamine ratios are monitored by inductively coupled plasma optical emission spectrometry and high-performance liquid chromatography, respectively. Batch-to-batch variation in particle size is controlled by laser diffraction: D50 is typically held between 8 µm and 25 µm after standardised resuspension in the finished suspension. Smaller D50 values increase surface area and shorten the profile; larger D50 values reduce injectability through 29-gauge needles. These parameters are critical because the depot effect is a function of crystal dissolution kinetics, not only insulin potency.
| Test | Acceptance criterion | Method/Standard |
|---|---|---|
| Insulin potency | 95.0–105.0% label claim | HPLC per USP 121 |
| pH | 7.0–7.4 | USP 791 |
| Sterility | No growth | USP 71 |
| Bacterial endotoxins | ≤ 0.1 EU/mg or product-specific | USP 85 |
| Subvisible particulates | ≤ 6000/container ≥ 10 µm; ≤ 600/container ≥ 25 µm | USP 788 |
| Residual moisture, lyophilised API | ≤ 3.0% w/w | Karl Fischer USP 921 |
For lyophilised PZI, residual moisture is held at or below 3.0% w/w; higher moisture reduces storage stability. The powder is hygroscopic and is packaged under dry nitrogen. Supernatant insulin after 24 h of undisturbed settling is controlled below 2.0 IU/mL in the finished sterile suspension because elevated free insulin indicates premature crystal dissociation. The crystalline fraction is characterised by optical microscopy and laser diffraction at batch release; crystal habit should be predominantly rod-shaped. Equiaxed or fragmented particles are recorded as observation and may require additional resuspension studies if present above the acceptance threshold stated in the certificate of analysis.
In a 316L stainless steel jacketed vessel, sterile-filtered insulin solution is cooled to 2–4°C before the addition of sterile protamine sulfate and zinc chloride solutions. Crystal growth is conducted under low-shear impeller agitation at 30–60 rpm. Increasing agitation above 500 rpm during crystallisation increases fines and narrows the crystal size distribution but can generate amorphous fragments that dissolve too rapidly after injection. The final suspension is passed through a 150 µm screen to remove agglomerates, then filled aseptically in an ISO 5 environment. Terminal moist heat sterilisation is not used because insulin denatures above 55°C; all components are sterile-filtered or dry-heat sterilised before crystallisation. Sterile filtration of the finished suspension is not possible because the crystalline particles exceed 0.22 µm membrane pores. Filler and stopper preparation comply with ISO 14644 and EU GMP Annex 1 for aseptic processing. During scale-up from pilot to production, batch-to-batch variance is observed mainly in crystal aspect ratio and D50. Deviations in zinc addition of ±5% from the registered ratio can shift the dissolution time-action curve; therefore, the zinc stock solution is standardised by complexometric titration before use.
A clear injectable solution can be produced from the API only by dissociating the zinc-protamine complex under acidic conditions. This yields a regular insulin-like immediate-acting profile and is not the standard PZI presentation. Such processing is not recommended unless the formulation is re-established as a separate solution product and the protamine and zinc counterions are removed or neutralised in a controlled manner. The standard injectable presentation remains a suspension; it must not be injected intravenously.
Potency is determined by high-performance liquid chromatography using a reversed-phase C18 column and gradient elution with phosphate buffer and acetonitrile; the method is system suitability tested per USP 121. The assay must resolve insulin from desamido insulin and other related peptides. Size-exclusion HPLC monitors high-molecular-weight proteins and aggregates; the acceptance limit for high-molecular-weight species is product-specific but typically below 1.0% of total peak area. Deamido insulin is controlled as an impurity; the compendial monograph sets its limit below 3.0–4.0% for many insulin products, but the exact PZI limit is stated in the certificate of analysis. Peptide mapping after digestion with endoproteinase Glu-C confirms the primary structure, and mass spectrometry is used for identification. Dissolution testing of the final suspension is performed in a pH 7.4 phosphate-buffered saline medium at 37°C using a USP 711 apparatus 2 paddle at 50 rpm. The time to release 50% insulin is monitored as an in vitro indicator of depot duration; a shorter T50 indicates faster dissolution and potential loss of long-acting character.
Stability storage conditions follow ICH Q1A(R2) for refrigerated products: 5°C ± 3°C long-term, 25°C ± 2°C/60% RH ± 5% RH accelerated. Release and shelf-life acceptance criteria are product-specific and stated in the stability protocol. At 1–5°C, the sterile suspension retains potency within the specified range for the assigned shelf-life; stressed exposure to 40°C for 7 days reduces potency in representative samples because insulin deamidation and aggregation accelerate above refrigerated conditions. Published data for this specific accelerated configuration is limited; therefore, product-specific degradation rates are established from the manufacturer’s stability batches rather than from general protein literature.
Dry processing of protamine zinc insulin is constrained by moisture, temperature, and mechanical energy. Lyophilised PZI is milled under nitrogen with residual moisture below 3.0% w/w; milling above 40°C or at high relative humidity causes denaturation and loss of potency. Dry granulation by roller compaction is preferred over wet granulation because water exposure dissolves the zinc-protamine complex and promotes amorphous aggregation. If wet granulation is unavoidable, non-aqueous solvents such as anhydrous ethanol or isopropanol may be used, but the granulation endpoint must be validated by recovery of insulin potency above 90.0% label claim. Tablets and capsules containing PZI require an enteric coating. Gastric pepsin degrades insulin rapidly at pH 1.5–2.5; uncoated oral products exhibit negligible systemic absorption. Methacrylic acid–ethyl acrylate copolymer enteric coatings are commonly used, but dissolution at pH 5.5–6.5 must be confirmed for the target species intestinal environment. Premix and powder intermediates are dispersible in feed carriers such as lactose monohydrate and microcrystalline cellulose, but this does not confer oral bioavailability unless the final dosage form includes an absorption-enhancing system.
Published data for oral administration of intact protamine zinc insulin in dogs and cats is limited, and the oral route is not a standard approach. Compounded tablet and capsule preparations are therefore considered non-systemic unless bioavailability is demonstrated by a validated ELISA or HPLC-MS method. In solid dosage processing, the dry blend must be protected from atmospheric moisture; environmental relative humidity above 60% requires preconditioning of excipients and processing under dry nitrogen. Lubrication with magnesium stearate is limited to 0.5–1.0% w/w because extended mixing can shear the insulin particles and expose hydrophobic surfaces, reducing dissolution. Disintegration testing per USP 2040 is performed in simulated gastric fluid and simulated intestinal fluid to confirm enteric coat integrity. For granules and premixes, content uniformity is assessed by sampling at 10–15 points across the blender; acceptance is 90.0–110.0% label claim with relative standard deviation below 5.0%. These operations are common to low-dose protein APIs and require separate equipment or validated cleaning procedures compliant with 21 CFR 211 for veterinary drug products where applicable.
Cross-contamination control follows 21 CFR 211.67. Swab sampling after cleaning uses a limit of not more than 10 ppm in the next product unless a health-based limit is established. Dedicated equipment is preferred for veterinary insulin products; if shared, cleaning validation must include HPLC and ELISA to detect residual insulin and protamine in rinse water and surface swabs. These controls are necessary because protamine zinc insulin is active at microgram-level doses and residual crystalline material can produce measurable hypoglycaemic response if transferred to a subsequent batch.