| HS Code | 523752 |
| Productname | Recombinant Human Chymotrypsin Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable |
| Api | Recombinant Human Chymotrypsin |
| Productcategory | Proteolytic Enzyme |
| Grade | Pharma Grade |
| Expressionsystem | Recombinant DNA technology |
| Dosageforms | Tablet, Capsule, Granule, Injection |
| Routesofadministration | Oral, Injectable |
| Appearance | White to off-white lyophilized powder or sterile solution |
| Molecularweight | Approximately 25 kDa |
| Isoelectricpoint | Approximately 8.5 |
| Purity | ≥95% by SDS-PAGE and HPLC |
| Specificactivity | ≥1000 USP units/mg (typical) |
| Solubility | Soluble in water and aqueous buffers |
| Phoptimum | 7.5 to 8.5 |
| Storageconditions | Store at -20°C or 2-8°C, protect from light and moisture |
| Shelflife | 24 months when stored as directed |
| Endotoxin | ≤10 EU/mg |
| Heavymetals | ≤10 ppm |
| Residualhostcellprotein | ≤100 ppm |
| Residualhostcelldna | ≤10 ng/mg |
| Microbiallimits | TAMC ≤10^2 CFU/g; TYMC ≤10^2 CFU/g |
| Qualitystandards | cGMP, ISO, USP/EP/JP |
| Inhibitors | Serine protease inhibitors such as PMSF, TLCK, aprotinin |
| Formulation | Lyophilized powder or sterile injectable solution |
| Packaging | Sterile vial, sealed container, or bulk API container |
As an accredited Recombinant Human Chymotrypsin Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
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Recombinant human chymotrypsin is incorporated into oral anti-oedema and anti-inflammatory tablet cores by dry granulation or direct compression because the enzyme undergoes autocatalytic degradation in aqueous wet granulation at water activity above 0.6 and process temperatures above 45°C. A non-steroidal anti-inflammatory adjunct tablet is formulated at 5,000 USP units of chymotrypsin per 120 mg target core, with microcrystalline cellulose adjusted to final core mass, crospovidone at 5.0% w/w, sodium starch glycolate at 2.0% w/w, colloidal silicon dioxide at 0.5% w/w, and magnesium stearate at 1.0% w/w. The API is pre-blended geometrically with 20 parts of microcrystalline cellulose to reduce assay variability in low active fraction formulations; loss on drying is maintained below 2.0% w/w by Ph. Eur. 2.2.32 before compression. Industry compliance includes USP <905> for content uniformity with acceptance value ≤ 15.0, USP <711> for delayed-release dissolution after a 2 h acid stage in 0.1 N HCl followed by phosphate buffer at pH 6.8 with Q≥80% at 45 min, ICH Q3D for elemental impurities, and 21 CFR 210/211 for finished pharmaceutical cGMP. Downstream production employs a 16-station rotary tablet press with 8.0 mm round B tooling, precompression at 4 kN, main compression at 10–14 kN, target hardness 70–90 N, and friability ≤ 0.5% by USP <1216>. The compressed cores are top-spray coated with Eudragit L 30 D-55 in a fully perforated side-vented pan coater at inlet air 40–50°C, spray rate 4–8 g/min per kg tablet bed, and exhaust humidity 20–30% RH; enteric coating weight gain is fixed at 8.0–10.0% w/w to resist gastric pepsin and acid-mediated proteolytic loss. Terminal packaging uses cold-form Alu-Alu blisters with moisture vapour transmission rate below 0.3 g/m²/day or HDPE bottles with silica gel desiccant; the finished product type is enteric-coated oral tablets indicated for post-surgical oedema and soft tissue inflammation.
| Release control | Method designation | Acceptance criterion |
|---|---|---|
| Content uniformity | USP <905>, Ph. Eur. 2.9.40 | Acceptance value ≤ 15.0 |
| Delayed-release dissolution | USP <711>, Ph. Eur. 2.9.3 | Q≥80% at 45 min in pH 6.8 after acid stage |
| Moisture content | USP <921>, Ph. Eur. 2.2.32 | NMT 2.0% w/w |
| Friability | USP <1216> | NMT 0.5% |
| Elemental impurities | ICH Q3D | Permitted daily exposure-based control |
Chymotrypsin injection cannot be sterilized by saturated steam autoclave at 121°C because activity loss exceeds 50% within 15 min; therefore aseptic filtration through a 0.22 µm PVDF membrane followed by lyophilization is the only route compatible with the thermolability of the recombinant enzyme. The liquid pre-lyophilization bulk is compounded at 5,000 USP units per mL in 10 mM sodium citrate buffer at pH 6.5, containing mannitol 25 mg/mL as cryoprotectant and polysorbate 80 0.1 mg/mL for interfacial protection. After 0.22 µm PVDF filtration, the solution is filled into 5 mL USP Type I borosilicate glass vials at 1.0 mL per vial, then lyophilized in a freeze dryer with shelf cooling to -45°C at 0.5°C/min, primary drying at -25°C and 80–100 µbar for 18–24 h, and secondary drying at 25°C for 6–8 h; residual moisture is controlled by coulometric Karl Fischer titration per USP <921> with limit NMT 1.0% w/w. Compliance includes USP <71> sterility, USP <85> bacterial endotoxin with a dose-based limit calculated from the 5 EU/kg/hr threshold, ICH Q5A(R1) for recombinant viral safety, and 21 CFR 610 for biological product general safety. Production-scale failure modes include incomplete cake collapse when primary drying is initiated above -20°C, and visible particle formation when polysorbate 80 is omitted from the formulation. The terminal finished product is a lyophilized powder for intramuscular or subcutaneous injection after reconstitution with 2 mL sterile water for injection, used where an injectable anti-inflammatory enzyme preparation is authorized.
For capsule-based oral systemic enzyme therapy, a multiparticulate enteric-coated pellet system is required rather than simple powder filling because the enzyme is pH-sensitive and powder-filled capsules can exhibit variable gastric transit and premature release. Chymotrypsin is layered onto 250–355 µm sugar spheres in a fluid bed rotor granulator using a binder solution of hypromellose 5 mPa·s at 3.0% w/w; the drug layer is applied to achieve 5,000 USP units per 200 mg capsule fill. A separating layer of hypromellose 6.0% w/w is applied before enteric coating with Eudragit L 100-55 and triethyl citrate at 10% w/w of polymer, talc at 40% w/w of polymer, and polysorbate 80 at 0.2% w/w of polymer, to a coating weight gain of 15–18% w/w. The coating process is performed in a bottom-spray fluid bed with inlet air 55–65°C, product temperature 32–38°C, spray rate 5–10 g/min per kg pellet bed, and final loss on drying NMT 2.0% w/w by Ph. Eur. 2.2.32. Production-scale observation indicates that pellet agglomeration increases sharply when spray rate exceeds 10 g/min/kg or product temperature falls below 30°C; this requires sieve fractionation and can reduce yield by 5–8%. Compliance for this oral capsule form includes USP <711> delayed-release dissolution in pH 6.8 phosphate buffer, USP <905> content uniformity, Ph. Eur. 2.9.40, Ph. Eur. 2.9.3, and ICH Q3D elemental impurity control. The terminal finished product is size 1 hard gelatin or hypromellose capsules in PVC/PVDC or Alu-Alu blister, indicated for systemic enzyme therapy in patients requiring a capsule dosage form.
A granule dosage form is prepared for patients who cannot swallow tablets or capsules; the formulation is dispensed as 2,500 USP units of chymotrypsin per 1,000 mg sachet, built on a sorbitol-mannitol excipient base to provide a pharmaceutically acceptable oral bulk. The granulation process is a fluid bed top-spray granulation using a 6% w/w povidone K30 aqueous binder, but the binder volume is limited to 60–80 mL per kg dry charge to keep final granule moisture below 2.0% w/w. Inlet air temperature is 60–70°C, product temperature 34–38°C, and spray rate 6–10 g/min; after drying, granules are sieved through 1.0 mm and 0.25 mm screens to control size distribution and improve reconstitution behaviour. Compliance includes Ph. Eur. 2.9.40 for uniformity of dosage units, Ph. Eur. 2.9.5 for uniformity of mass, USP <711> dissolution using phosphate buffer at pH 6.8 with Q≥80% at 30 min, and Ph. Eur. 5.1.4 for microbiological quality of non-sterile oral preparations. The terminal product is sealed in a paper/aluminium/polyethylene laminate sachet with water vapour transmission rate below 0.5 g/m²/day; the finished product type is a single-dose oral granule for post-traumatic oedema and inflammatory swelling.
When chymotrypsin is indicated for intracameral zonulolysis during lens extraction, the API is not tableted or encapsulated but is supplied as a sterile lyophilized powder for reconstitution. The formulation ratio in this surgical niche is conventionally 150 USP units per single-use vial, reconstituted with 5 mL sterile balanced salt solution to a nominal concentration of 30 USP units/mL; the surgical team then dilutes this solution 1:5,000 into the irrigation fluid used for zonular fibre cleavage. The manufacturing process is aseptic: chymotrypsin is dissolved in 10 mM sodium acetate buffer at pH 5.5, filtered through a 0.22 µm PVDF membrane, filled into 5 mL USP Type I glass vials under Grade A unidirectional airflow within an isolator, and lyophilized with primary drying at -30°C and 90 µbar for 20 h. Compliance anchors include USP <71>, USP <85> with endotoxin acceptance calculated from the intended intraocular dose, Ph. Eur. 2.6.1, ICH Q5A(R1) for viral safety, 21 CFR 211 subpart C for aseptic processing, and 21 CFR 610 for biological product lot release. The proteolytic action is not selective for zonular fibres; prolonged irrigation beyond 2 min can weaken the lens capsule, so surgical protocols restrict contact time and irrigation volume. The finished product type is a sterile lyophilized powder for ophthalmic irrigation after reconstitution, used strictly as a surgical aid rather than a systemic anti-inflammatory.
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Recombinant Human Chymotrypsin Pharma Grade API, model rHC-01, is produced by submerged fermentation of a non-pathogenic Escherichia coli K-12 strain carrying a codon-optimized synthetic gene encoding the human chymotrypsin B sequence. Fermentation is performed in a 200 L fed-batch stainless-steel bioreactor at 37 °C ± 0.5 °C, dissolved oxygen 30% ± 5%, and pH 6.8–7.2. The cell paste is harvested by continuous disc-stack centrifugation, resuspended in lysis buffer, and disrupted by high-pressure homogenization at 800–1000 bar. Inclusion bodies are washed, solubilized in 6 M guanidine hydrochloride with 10 mM dithiothreitol, and refolded by 20-fold dilution into a redox buffer containing 2 M urea, 0.2 M arginine, 3 mM reduced glutathione, and 0.6 mM oxidized glutathione at pH 8.5. The active enzyme is purified by hydrophobic interaction chromatography, cation-exchange chromatography, and size-exclusion chromatography. The cation-exchange step is operated at pH 5.5 with 50 mM sodium acetate, and the elution gradient from 0.0 M to 0.3 M sodium chloride is applied over 10 column volumes. The size-exclusion step removes high-molecular-weight aggregates and clipped species, with aggregate content controlled to ≤ 2.0% by SEC-HPLC. The purified bulk is concentrated by tangential-flow ultrafiltration with a 10 kDa cutoff membrane, dialyzed against 5 mM sodium acetate pH 5.0, and lyophilized. Model rHC-01 oral grade and injectable grade are differentiated by residual endotoxin, bioburden, and particulate-matter acceptance limits, not by active enzyme identity.
Release testing follows the USP Chymotrypsin monograph for enzyme activity and the relevant general chapters for impurity, water, and microbiological control. Table 1 lists the typical release profile. Each batch is also tested for identity by peptide mapping using trypsin digestion and RP-HPLC; the peptide map must match the reference standard at a similarity score of ≥ 0.85. The residual moisture specification is critical because water content above 3.0% increases solid-state autolysis and reduces tablet stability. The bacterial endotoxin limit for the injectable grade is ≤ 0.10 EU/mg, which is consistent with a maximum dose of 10 mg and the Ph. Eur. 2.6.14 threshold for parenteral products. The oral grade permits ≤ 100 CFU/g by Ph. Eur. 2.6.12, while the injectable grade is terminally sterile-filtered and filled under Grade A laminar airflow. Host-cell protein and DNA limits are set according to ICH Q11 residual DNA guidance, with residual DNA ≤ 10 pg/mg and host-cell protein ≤ 50 ppm.
| Attribute | Limit | Test procedure |
|---|---|---|
| Appearance | White to off-white lyophilized cake or powder | Visual |
| Specific activity | ≥ 1000 USP units/mg | USP Chymotrypsin monograph |
| Purity by RP-HPLC | ≥ 97.0% | Ph. Eur. 2.2.29 |
| Aggregate content | ≤ 2.0% | SEC-HPLC |
| Residual moisture | ≤ 3.0% | USP <921> / Ph. Eur. 2.5.12 |
| pH of 1% solution | 5.0–7.0 | Potentiometric |
| Bulk density | 0.35–0.55 g/mL | Graduated cylinder tap density |
| Particle size | D50 80–150 μm, D90 ≤ 250 μm | Laser diffraction |
| Bacterial endotoxins, injectable | ≤ 0.10 EU/mg | Ph. Eur. 2.6.14 / USP <85> |
| Microbial enumeration, oral | ≤ 100 CFU/g | Ph. Eur. 2.6.12 |
| Sterility, injectable | Sterile | Ph. Eur. 2.6.1 / USP <71> |
| Host-cell protein | ≤ 50 ppm | ELISA |
| Residual host-cell DNA | ≤ 10 pg/mg | qPCR |
| Residual trypsin activity | ≤ 0.10 USP units/mg | USP trypsin substrate assay |
Manufacture is conducted under ICH Q7 and 21 CFR 211 for APIs. Process validation comprises three consecutive batches with critical process parameters monitored in real time by distributed control system. Column resin lifetime is validated for 20 cycles; cleaning validation by total organic carbon and protein swab confirms residual carryover below 1 ppm. The lyophilized cake may vary from cracked to uniform; this is not a failure criterion because it does not affect reconstitution time.
For tablet and capsule manufacturing, rHC-01 is preblended with microcrystalline cellulose and sodium starch glycolate in a bin blender at 15 rpm for 10 minutes. Magnesium stearate is added as a lubricant at 0.5% w/w and mixed for 3 minutes to avoid excessive shear. Dry granulation by roller compaction is preferred for tablet formulations requiring particle size enlargement; the roller pressure is maintained at 6–8 kN/cm, and the compact is milled through a 1.0 mm screen. Aqueous wet granulation is not recommended because the enzyme is sensitive to heat and hydrolysis. If wet granulation is unavoidable, the drying step must maintain product temperature below 30 °C and the granulate moisture below 2.5%. Capsule filling is performed at relative humidity below 35% RH and temperature 20–25 °C. Dissolution testing by USP <711> uses 900 mL of 50 mM phosphate buffer pH 6.8 at 37 °C with paddle speed 50 rpm; the release criterion is not less than 80% of label activity at 30 minutes.
Granule presentations are prepared by blending the API with pregelatinized starch and sorbitol, filling into aluminum foil sachets under nitrogen. The sachet headspace oxygen is controlled below 2.0% v/v to limit oxidation of methionine residues. The blend is passed through a 500 μm sieve prior to filling to ensure content uniformity according to USP <905>.
Injectable formulations are prepared by reconstituting rHC-01 in Water for Injection at 2–10 mg/mL under Grade A laminar airflow in a 316L stainless steel jacketed vessel. The solution is adjusted to pH 5.5–6.5 with 0.1 M hydrochloric acid or 0.1 M sodium hydroxide, and stirred at 100–150 rpm with a bottom-mounted magnetic mixer. Tonicity is adjusted with sodium chloride 0.9% w/v. The solution is prefiltered through a 0.45 μm PVDF membrane and sterile-filtered through a 0.22 μm PES membrane. A minimum filtrate flux of 50 L/m²/h is maintained to limit shear-induced aggregation; the transmembrane pressure should not exceed 0.5 bar during the final sterile filtration.
Extended liquid-state hold is a critical process point. At pH 6.0 and 25 °C, activity loss after 24 h is less than 5%; at pH 8.0 and 37 °C, activity loss exceeds 15% because of autolysis. Holding tanks are jacketed at 2–8 °C, and the total duration from reconstitution to filling should not exceed 8 h. Terminal sterilization by moist heat is contraindicated: exposure at 121 °C for 15 min reduces specific activity by more than 90%. Aseptic filtration is mandatory. The filling line is equipped with online particle monitoring to comply with USP <790> and Ph. Eur. 2.9.19. Glass vials are Type I borosilicate per USP <660> and Ph. Eur. 3.2.1, with chlorobutyl stoppers.
Freeze-thaw stability of the reconstituted solution is limited to three cycles at -20 °C ± 2 °C; activity loss per cycle is ≤ 5% and subvisible particle counts remain below the Ph. Eur. 2.9.19 limit for small-volume parenterals. The lyophilized powder is stored at -20 °C ± 5 °C. After reconstitution, solutions should be used within 8 h at 2–8 °C and must not be refrozen more than once.
Chymotrypsin from bovine pancreas is obtained as a mixture of chymotrypsin A and B along with variable amounts of trypsin, elastase, carboxypeptidase A, and undefined pancreatic lipids. Recombinant fermentation of the human chymotrypsin B sequence provides a single molecular species with a predictable disulfide bond pattern. Table 2 summarizes the main distinguishing attributes.
| Characteristic | rHC-01 | Bovine pancreatic chymotrypsin |
|---|---|---|
| Source | E. coli K-12 fermentation | Bovine pancreas extract |
| Animal-derived materials | None | Present |
| TSE/BSE risk | Absent | Requires country-of-origin certification |
| Trypsin activity | ≤ 0.10 USP units/mg | Often 0.5–1.5 USP units/mg without additional chromatography |
| Host-cell protein | ≤ 50 ppm | Not standardized |
| Residual host-cell DNA | ≤ 10 pg/mg | Not routinely tested |
| Specific activity | ≥ 1000 USP units/mg | ≥ 1000 USP units/mg after crystallisation |
| Preferred cleavage site | Carboxyl side of Tyr, Trp, Phe | Same |
The recombinant product is particularly suited to controlled-release dosage forms in which residual trypsin would otherwise alter the release-controlling polymer or prematurely degrade co-formulated peptide APIs. The absence of animal-derived proteases simplifies regulatory submissions under EMA/410/01 Rev. 3 and FDA 21 CFR 211.160. For oral granules, the API is blended with pregelatinized starch and filled into sachets under nitrogen purge; the headspace oxygen is controlled below 2.0% v/v to protect methionine residues from oxidation.
rHC-01 should not be combined with reducing sugars in aqueous granulating fluids because Maillard-type conjugation of lysine residues reduces activity. The product retains catalytic activity in the pH 6.0–8.5 range with an esterase optimum at pH 7.8–8.0; it is inactivated below pH 2.0 and above pH 10.0. In comparison with recombinant trypsin, rHC-01 cleaves after aromatic residues rather than after lysine or arginine, which modifies the peptide mapping profile and reduces the risk of activating certain precursor proteins during processing. Compared with porcine pepsin, rHC-01 operates at neutral to slightly alkaline pH and is not acid-stable. The product is not compatible with oxidizing agents, strong acids, acetone above 40% v/v, or heavy-metal ions such as Fe³⁺ and Cu²⁺.
The oral grade is not interchangeable with the injectable grade; oral material may exceed the injectable endotoxin limit and cannot be terminally sterilized. Injectable grade rHC-01 is supplied in sterile double-bagged containers with a documented sterility assurance level of ≤ 10⁻⁶. Packaging of rHC-01 bulk powder is performed in amber glass or HDPE containers with screw caps under argon, with desiccant. Storage at -20 °C ± 5 °C protects activity for 24 months from the date of manufacture. Once opened, the container should be re-purged with nitrogen and resealed; repeated warming to room temperature accelerates moisture uptake and should be avoided. When used in parenteral processing, the lyophilized powder is equilibrated to 15–25 °C in the unopened container before reconstitution to prevent condensation on the cake surface.