| HS Code | 881530 |
| Product Name | Egg Hydrolytic Enzyme Veterinary Grade API |
| Synonyms | Egg white lysozyme; muramidase; N-acetylmuramide glycanohydrolase |
| Cas Number | 9001-63-2 |
| Ec Number | 3.2.1.17 |
| Source | Hen egg white |
| Grade | Veterinary grade API |
| Appearance | White to off-white crystalline powder or lyophilized powder |
| Solubility | Freely soluble in water; insoluble in organic solvents |
| Ph Stability | Stable over pH 3.0–7.0; optimum pH 6.0–7.0 |
| Thermal Stability | Stable below 60°C; activity decreases at higher temperatures |
| Enzyme Activity | Typically ≥20,000 U/mg; higher activities available |
| Moisture Content | ≤5.0% |
| Heavy Metals | ≤10 ppm |
| Arsenic | ≤2 ppm |
| Microbial Limits | Total aerobic count ≤1000 CFU/g; yeast and mold ≤100 CFU/g; E. coli absent; Salmonella absent |
| Storage Conditions | Store cool, dry, protected from light; keep tightly closed |
| Shelf Life | 24 months when stored as directed |
| Packaging | 25 kg drum, 1 kg foil bag, or customized packaging |
| Dosage Forms | Tablets, injections, capsules, powders, granules, premix, solutions |
| Target Species | Poultry, swine, ruminants, companion animals, aquatic animals |
| Route Of Administration | Oral, injection, topical, or as directed by veterinarian |
| Regulatory Standard | Veterinary grade; GMP-manufactured |
As an accredited Egg Hydrolytic Enzyme 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 | Egg Hydrolytic Enzyme Veterinary Grade API packaged in 25 kg double-lined fiber drums, sealed for tablets, injections, capsules, powders, granules, premix, and solutions. |
| Container Loading (20′ FCL) | 20′ FCL loading: palletized/drummed Egg Hydrolytic Enzyme Veterinary Grade API, securely braced, moisture-protected, for tablets, injections, capsules, powders, granules, premix, solutions. |
| Shipping | Egg Hydrolytic Enzyme Veterinary Grade API is shipped in sealed, light-resistant, moisture-barrier containers under temperature-controlled conditions, typically 2–8°C or as specified. Packaging prevents contamination and degradation, with complete documentation, labels, and MSDS/COA included. Handle as a sensitive biological enzyme; avoid excessive heat, moisture, and temperature fluctuations during transit. |
| Storage | Store in tightly closed, light-resistant, original containers in a cool, dry, well-ventilated area, away from sunlight, heat, moisture, and incompatible materials. Refrigerate at 2–8°C for prolonged storage; avoid freezing and temperature fluctuations unless supplier-validated. Protect from microbial contamination. For injectable use, maintain sterile handling and follow the manufacturer’s SDS/COA storage instructions. Keep containers sealed and use first-in, first-out stock rotation. |
| Shelf Life | Shelf life typically 24–36 months when stored sealed, dry, protected from light at controlled room temperature; verify exact expiry with supplier. |
The egg hydrolytic enzyme raw material is supplied as a white to faintly yellow lyophilised or crystalline powder with muramidase activity assigned to hen egg-white lysozyme hydrochloride, E.C. 3.2.1.17. The enzyme catalyses the hydrolysis of the β-(1→4) glycosidic linkage between N-acetylmuramic acid and N-acetylglucosamine in Gram-positive bacterial peptidoglycan. This specificity creates a narrow veterinary application window: staphylococcal and streptococcal presentations are appropriate, whereas Gram-negative organisms remain intrinsically resistant unless an outer-membrane permeabiliser such as EDTA or lactoferrin is co-formulated. Activity is normally determined by the turbidimetric method using a washed suspension of Micrococcus lysodeikticus ATCC 4698 at 25 °C to 37 °C in phosphate buffer pH 6.2, with results expressed in FIP lysozyme units per milligram against the Ph. Eur. lysozyme hydrochloride chemical reference substance. The veterinary API is handled as a non-sterile starting material for oral and feed applications, with acceptance criteria for loss on drying below 5.0% w/w, total aerobic microbial count below 103 CFU/g, and Escherichia coli absence in 1 g as described in Ph. Eur. 2.6.13. For sterile parenteral presentations, the API is reconstituted, sterile-filtered, and lyophilised in the finished dosage form; the raw powder is not terminally autoclaved. The material is hygroscopic and should be pre-dried before direct compression or dry blending when ambient relative humidity exceeds 60%.
Injectable lysozyme presentations are built around the narrow pH and temperature window of the enzyme in aqueous solution. The bulk solution is prepared in Water for Injection at 10–50 mg/mL lysozyme hydrochloride, adjusted with 0.1 M hydrochloric acid or sodium hydroxide to pH 5.0–6.5, and filtered through a 0.22 µm PVDF or PES membrane into Type I borosilicate vials. Terminal steam sterilisation is not used because the aqueous enzyme loses more than 50% of its turbidimetric activity after 30 min at 65 °C; aseptic filling followed by lyophilisation is therefore the standard route for bovine, porcine, and companion-animal injectables. The lyophilised cake is reconstituted with Water for Injection to the original volume, and the preservative-free reconstituted product should be used within 24 h when stored at 2–8 °C. If a multi-dose vial is formulated with benzyl alcohol at 1.0% v/v, the finished product must be tested for activity and subvisible particles under Ph. Eur. 5.1.3 and Ph. Eur. 2.9.19, because benzyl alcohol has been reported to interfere with lysozyme conformational stability in some buffer systems; published data for this specific veterinary dosage form is limited. Use of phosphate-buffered saline is accepted, but phosphate concentration above 100 mM can salt out the enzyme and produce visible flocculation. The injection is not suitable for combination with anionic surfactants or with strong oxidising agents, and it should not be mixed with tetracycline hydrochloride in the same syringe because complexation and precipitate formation have been observed in aqueous solution.
For compressed oral solid dosage forms, lysozyme hydrochloride is not subjected to wet granulation unless the granulation fluid is water and the product temperature remains below 50 °C. Direct compression is the preferred process because the enzyme is water-soluble and has good compactability when blended with mannitol and microcrystalline cellulose; lactose monohydrate is used only when the water activity of the finished tablet is maintained below 0.60, because reducing sugar impurities can accelerate Maillard browning and reduce assay potency under long-term storage. A representative direct-compression blend contains lysozyme hydrochloride equivalent to 20–50 mg of lysozyme chloride per tablet, microcrystalline cellulose, mannitol, crospovidone at 2.0–4.0% w/w, and magnesium stearate at 0.5–1.0% w/w. The powder is pre-dried at 40–45 °C for 2–4 h when relative humidity exceeds 60% in the granulation suite. Tablets are compressed on a rotary press to hardness 70–120 N, friability below 0.8% w/w, and disintegration within 15 min in purified water at 37 °C per Ph. Eur. 2.9.1. Dissolution testing is performed in 900 mL of phosphate buffer pH 6.2 using USP Apparatus 2 at 50 rpm; acceptance criteria are product-specific because no harmonised veterinary monograph fixes a universal Q value, and published data for this exact grade is limited. Capsules are filled with a dry blend after sieving through 250 µm mesh to remove agglomerates. The fill weight is adjusted for tapped density between 0.45 g/mL and 0.65 g/mL to prevent dosator fill-weight drift on high-speed encapsulation machines. Hard gelatin capsules size 2 or 3 are used when the powder does not exceed 40 °C during filling; HPMC capsules are selected when moisture-sensitive fill formulations or specific regulatory market requirements exclude gelatin.
Water-soluble powders and oral solutions are prepared by dry blending lysozyme hydrochloride with dextrose monohydrate, citric acid, and sodium chloride. The sodium chloride level is maintained to provide an ionic strength of 0.05–0.10 M after dilution, which is the optimum range for muramidase activity against Micrococcus lysodeikticus. Citric acid is added to ensure the finished stock solution pH remains between 5.5 and 6.0. For mass medication in poultry and swine, the dry powder is diluted in a stock tank and delivered through in-line proportioners at 0.5–2.0% stock solution. Free chlorine in the drinking water is a critical process parameter because hypochlorous acid oxidises methionine residues in the enzyme, and residual free chlorine above 1.0 mg/L can reduce activity by more than 20% after 60 min of contact. Water lines should be flushed and, if necessary, dechlorinated with ascorbic acid at 20–50 mg/L before the medicated solution is introduced. The proportioner should be calibrated to deliver the intended dose per litre of drinking water, and direct recirculation through return lines should be avoided because the enzyme is not a self-preserving solution. Stagnant solutions in PVC header tanks for more than 12 h at ambient temperatures above 30 °C may develop microbial growth and should not be used. The dry powder should remain free-flowing after storage in foil-lined 25 kg bags; caking is avoided by maintaining loss on drying below 5.0% w/w and storage relative humidity below 60%.
| Parameter | Acceptable range | Reference method |
|---|---|---|
| Free chlorine | < 1.0 mg/L | ISO 7393-2 |
| pH after dilution | 5.5–6.0 | Potentiometric method |
| Water temperature | < 30 °C | Process measurement |
| Total hardness | < 200 mg/L as CaCO3 | ISO 6059:1984 |
Feed granules and antibacterial premixes present the most demanding thermal and moisture environment for egg hydrolytic enzyme. Direct incorporation into the meal before pelleting is rarely used because the steam conditioner operates at 75–85 °C for 30–60 s, and aqueous lysozyme activity begins to decline sharply above 65 °C. Instead, the enzyme is applied as a post-pelleting coating or is incorporated as a microgranule after the pellet cooler. The premix is prepared by dry blending lysozyme hydrochloride with calcium carbonate, sodium sulphate, or ground wheat middlings to a standardised activity of 1×106 FIP units per kg, then granulated in a high-shear mixer with water as binder and dried in a fluid-bed dryer at inlet air temperature 40–50 °C. The target particle size after dry sieving is 250–500 µm. This range supports uniform distribution in complete feed at inclusion rates of 500–2,000 g/tonne with a coefficient of variation below 5.0% after 2–3 min in a horizontal ribbon mixer, as verified by sampling according to ISO 6497:2002. The finished premix should have a loss on drying below 5.0% w/w and should be packed in foil-lined 25 kg bags; bags exposed to relative humidity above 65% for more than 48 h may cake and should be re-tested before use. Do not blend this premix with acidogenic mineral premixes containing citric acid or phosphoric acid, because low pH below 4.5 and high hydrogen-ion activity can destabilise the enzyme during prolonged storage. Published data for this specific post-pelleting enzyme configuration is limited, so activity recovery should be verified on the actual pellet mill and coating line before routine production.
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Egg Hydrolytic Enzyme Veterinary Grade API is a purified peptidoglycan N-acetylmuramoylhydrolase (EC 3.2.1.17; CAS 12650-88-3) obtained from hen egg white and standardised for veterinary pharmaceutical processing into tablets, injections, capsules, powders, granules, premix, and oral solutions. The enzyme consists of a single polypeptide chain of approximately 129 amino acid residues with a molecular mass of 14.3 kDa and an isoelectric point near 11. It catalyses hydrolysis of the β-1,4-glycosidic linkage between N-acetylmuramic acid and N-acetyl-D-glucosamine residues in bacterial peptidoglycan, a mechanism that does not target host cell membranes. Manufacturer release codes for veterinary-grade material typically incorporate dosage-form compatibility and assay tier: EHE-VG/DT for direct-tablet powder, EHE-VG/INJ for low-endotoxin lyophilised injection powder, EHE-VG/PRM for granular premix, and EHE-VG/SOL for drinking water or solution formulations. The code suffix is not a pharmacopoeial descriptor but a supplier-specific model identifier that is mapped to the batch certificate of analysis.
Specification differentiation begins with route of administration. Oral tablet, capsule, and powder grades are released with a minimum activity of 20,000 FIP units/mg on the dried substance, loss on drying no greater than 5.0%, and total aerobic microbial count no greater than 10^3 CFU/g. Parenteral solution grade is manufactured from the same active substance but is additionally processed through chromatographic purification and aseptic lyophilisation to achieve a bacterial endotoxin limit of 0.05 EU/mg by Ph. Eur. 2.6.14, a loss on drying no greater than 2.0%, and total aerobic microbial count no greater than 10^1 CFU/g by Ph. Eur. 2.6.12. Residual moisture is controlled because water uptake above the specified limit reduces chemical stability and interferes with dry powder flow and tablet hardness.
Release activity is expressed in FIP units per milligram against a Micrococcus lysodeikticus reference substrate under the turbidimetric method cited in compendial lysozyme monographs. The following table summarises the representative veterinary release specification across dosage-form grades.
| Parameter | Oral tablet/capsule/powder/granule/premix grade | Parenteral solution grade | Test designation |
|---|---|---|---|
| Appearance | White to off-white free-flowing powder | White to off-white lyophilised powder | Visual examination |
| Assay on dried substance | ≥ 20,000 FIP units/mg | ≥ 20,000 FIP units/mg | Turbidimetric FIP assay |
| Loss on drying | ≤ 5.0% | ≤ 2.0% | Ph. Eur. 2.2.32 |
| Sulphated ash | ≤ 1.0% | ≤ 0.5% | Ph. Eur. 2.4.14 |
| Bacterial endotoxins | ≤ 0.5 EU/mg | ≤ 0.05 EU/mg | Ph. Eur. 2.6.14 |
| Total aerobic microbial count | ≤ 10^3 CFU/g | ≤ 10^1 CFU/g | Ph. Eur. 2.6.12 |
| Total yeast and mould count | ≤ 10^2 CFU/g | ≤ 10^1 CFU/g | Ph. Eur. 2.6.12 |
| Particle size D90 | ≤ 150 µm | ≤ 75 µm | Laser diffraction / Ph. Eur. 2.9.31 |
| Residual solvents | Class 3 limits; ethanol ≤ 5000 ppm | Class 3 limits; ethanol ≤ 3000 ppm | Ph. Eur. 2.4.24 |
Identification is performed by peptide mapping against the reference standard and by an enzymatic activity overlay. Identity alone is not sufficient for veterinary API release; the batch certificate also includes residual protein profile, host allergen limits, and stability data generated under conditions appropriate to the dosage form. The presence of unhydrolysed egg protein species is controlled because residual ovalbumin and ovomucoid are relevant to hypersensitivity risk in target animals.
Veterinary formulations containing egg hydrolytic enzyme are administered orally as tablets, capsules, powders, granules, premixes, or solutions where enzymatic cleavage of bacterial peptidoglycan is intended to reduce Gram-positive bacterial load on mucosal surfaces or in the gastrointestinal tract. The enzyme is not absorbed systemically to a significant extent and does not act on Gram-negative organisms unless the outer membrane has been permeabilised; this narrow spectrum is a critical difference from broad-spectrum antimicrobial drugs and reduces selection pressure for plasmid-mediated resistance genes. Published field efficacy data for this specific configuration are limited, and product indications must be evaluated against the target species and the registered veterinary medicinal product dossier.
Direct-compression tablet formulations require particle size, bulk density, and moisture control because the enzyme has limited intrinsic compaction capacity unless preconditioned. The direct-tablet grade is blended with microcrystalline cellulose, lactose monohydrate, crospovidone, and sodium stearyl fumarate in a bin blender for 15–20 min at 60–70% fill volume. The blend is compressed on a rotary tablet press equipped with precompression rolls and a main compression force window of 15–25 kN; tablet hardness is maintained at 50–80 N, friability is below 1.0% after 100 revolutions by Ph. Eur. 2.9.7, and disintegration is under 15 min in water at 37°C by Ph. Eur. 2.9.1. Direct-compression formulations above 50 mg active per tablet tend to cap unless the API is dry-granulated by roller compaction at a gap of 1.0–1.5 mm and a roll pressure of 60–80 bar. Published data for direct-compression loading above 100 mg in large veterinary boluses is limited.
Capsule filling on dosator-type machines requires control of particle-size span and flow. The oral powder grade conditioned to a bulk density of 0.35–0.55 g/mL and tapped density of 0.55–0.75 g/mL produces fill-weight variability below 5% relative standard deviation when the D10 exceeds 20 µm and the D90 remains below 150 µm. Granular premix and powder formulations are buffered with sodium acetate to pH 4.0–5.0; solution preparations maintain activity above 95% for 24 h at 25°C under these conditions, while unpurified egg protein hydrolysates exhibit precipitation and variable enzymatic recovery in the same matrix.
For parenteral solutions, the lyophilised API is dissolved in water for injection at 10–20 mg/mL, and the solution is clarified through 0.22 µm polyethersulfone sterilising-grade filters before aseptic filling. Adsorption of the enzyme to container-closure elastomers at low protein concentration is mitigated by inclusion of 0.05% polysorbate 80 and 0.9% sodium chloride. Terminal steam sterilisation is not recommended because activity loss of 30–40% is observed after 121°C for 15 min; aseptic filtration is therefore the standard manufacturing route. The parenteral grade is controlled for subvisible particulate matter by Ph. Eur. 2.9.19 and for bacterial endotoxin as described. SDS-PAGE purity is not less than 95%, and residual ovalbumin is held below 0.1% w/w by ELISA; this threshold reduces but does not eliminate type I hypersensitivity risk in target species.
Compared with unstandardised egg protein hydrolysates sold as feed or food ingredients, the veterinary-grade API is not interchangeable because the latter lack batch activity standardisation and are not released against pharmacopoeial impurity limits. Food-grade lysozyme declared as additive E 1105 is suitable for food preservation but does not provide veterinary drug master file documentation, viral safety data, endotoxin recovery studies, or the stability commitment required for registered veterinary medicinal products. Recombinant lysozyme from microbial fermentation may contain host-cell proteins and endotoxin profiles that differ by strain; the egg-derived veterinary grade has a defined source and a single-band purity profile that simplifies pharmacopoeial identification. The hydrolytic activity of this API should not be confused with acid-hydrolysed egg protein powders intended as nutritional supplements, because the latter are valued for peptide content rather than enzymatic activity and contain no controlled peptidoglycan-hydrolysing titre.
| Characteristic | Veterinary Grade Egg Hydrolytic Enzyme API | Food-Grade Lysozyme E 1105 | Recombinant Lysozyme | Unstandardised Egg Hydrolysate Powder |
|---|---|---|---|---|
| Assay standardisation | Turbidimetric FIP units; batch certificate of analysis | Microbial inhibition titre; variable | Specific activity by fermentation strain | Total protein only; no enzyme assay |
| Bacterial endotoxin | ≤ 0.5 EU/mg oral; ≤ 0.05 EU/mg parenteral | Not routinely tested | Host-cell dependent | Not tested |
| Microbial limits | Ph. Eur. 2.6.12 | EU food hygiene criteria | ICH Q6A applies | Not specified for feed misuse |
| Residual solvents | Ph. Eur. 2.4.24 | Food safety solvent residues | Process-specific | Not controlled |
| Regulatory documentation | Veterinary drug master file; API GMP | Food additive specification only | Biologics dossier if therapeutic | Feed material declaration |
The premix grade is diluted onto lactose or corn cob carriers at 5–50 g/kg active enzyme and incorporated into complete feed at 1–5 kg/t. In a 500 L ribbon mixer, the carrier is charged first, then the premix grade is added and blended for 10 min at 20–30 rpm; addition of the enzyme before the carrier produces protein segregation and assay variability above 10% relative standard deviation. The feed pelleting step is the main thermal hazard: conditioning above 70°C results in activity losses of 10–20% per pass, and post-pelleting liquid application is specified when pellet die temperatures exceed 65°C.
Granules are produced by fluidised-bed spray granulation using maltodextrin as binder at inlet air 60–70°C and product temperature below 40°C; this route improves flow and reduces dust but requires moisture migration evaluation under 40°C/75% RH for 6 months. For drinking water medication, the solution-dedicated API is dissolved at 0.1% w/v in buffered water at pH 4.0–6.0; activity remains above 90% for 48 h at 25°C. Chlorinated municipal water at 2 ppm free chlorine reduces activity by more than 50% within 4 h due to oxidative inactivation of active-site residues; therefore, dechlorination or stabiliser addition is required before administration. Alkaline drinking water above pH 8.0 is not recommended because the enzyme undergoes time-dependent aggregation and partial denaturation; published data for continuous administration over 72 h in this specific matrix is limited.
All grades are stored in sealed aluminium-laminated pouches with desiccant at 2–8°C. Under these conditions, the manufacturer’s shelf-life specification is 24 months; opened containers for oral powder and premix grades are used within 30 days when stored below 25°C and 60% RH. Repeated freeze-thaw cycles of reconstituted injection solution are not permitted because activity loss after 3 cycles exceeds 10%.