| HS Code | 716754 |
| Product Name | Trastuzumab Injection Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable |
| Api Name | Trastuzumab |
| Api Type | Recombinant humanized IgG1 monoclonal antibody |
| Drug Class | HER2-directed monoclonal antibody |
| Target | Human epidermal growth factor receptor 2 (HER2) |
| Mechanism Of Action | Binds HER2 extracellular domain, inhibits HER2-mediated signaling, and induces antibody-dependent cellular cytotoxicity |
| Cas Number | 180288-69-1 |
| Molecular Weight | Approximately 145 kDa |
| Grade | Pharma Grade / GMP |
| Appearance | White to off-white lyophilized powder or sterile solution |
| Solubility | Soluble in water; reconstituted for injection |
| Route Of Administration | Intravenous infusion and subcutaneous injection |
| Dosage Forms | Lyophilized powder for concentrate for solution for infusion; solution for injection |
| Prescription Status | Prescription only |
| Approval Status | FDA-approved and EMA-approved for HER2-positive breast and gastric cancers |
| Manufacturing Method | Recombinant DNA technology in mammalian cell culture |
| Atc Code | L01XC03 |
As an accredited Trastuzumab Injection 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.
| Packing | Supplied in 100 mg sterile, single-use glass vials sealed with rubber stopper and aluminum crimp, labeled Pharma Grade API. |
| Container Loading (20′ FCL) | GMP-compliant, securely palletized, temperature-controlled, moisture-protected loading into a 20-foot FCL container for pharmaceutical-grade Trastuzumab API oral/injectable formulations. |
| Shipping | Trastuzumab Injection Pharma Grade API is shipped via validated cold chain at 2–8°C using insulated, leak-proof, tamper-evident packaging with temperature monitors and phase-change packs. Shipments follow GDP, IATA/UN dangerous goods, and customs documentation to preserve stability, sterility, and potency. |
| Storage | Store Trastuzumab Injection API in a tightly closed, light-resistant container at 2–8°C (36–46°F). Keep upright in original carton; do not freeze or shake. Protect from heat, moisture, and direct sunlight. Maintain in a clean, secure, temperature-monitored, pharmaceutical-grade area separated from incompatible materials. For reconstituted or diluted product, follow manufacturer instructions and use within the specified stability period. |
| Shelf Life | Trastuzumab shelf life: typically 24–36 months refrigerated at 2–8°C, protected from light; do not freeze. Confirm exact expiry with supplier. |
Trastuzumab in its 150 mg single-dose lyophilized presentation is not processed into tablet, capsule, or granule dosage forms; no pharmacopoeial monograph supports oral solid administration because the intact IgG1 is denatured and cleaved by gastric acid and pepsin before reaching systemic circulation. The injectable route is therefore the only validated downstream format at this strength. The formulation composition recorded in the approved product documentation combines 150 mg trastuzumab with 136.2 mg α,α-trehalose dihydrate, 3.36 mg L-histidine hydrochloride monohydrate, 2.16 mg L-histidine, and 0.60 mg polysorbate 20; reconstitution with 7.2 mL Sterile Water for Injection yields a nominal 21 mg/mL solution at a pH of approximately 6.0. Compliance for this presentation includes sterility testing under USP <71> and Ph. Eur. 2.6.1, bacterial endotoxin testing under USP <85> and Ph. Eur. 2.6.14, subvisible particulate testing under USP <787> and Ph. Eur. 2.9.19, visible particulate inspection under USP <790>, and parenteral quality testing under USP <1>. Batch-to-batch variability in the CHO-derived glycan profile is controlled under ICH Q6B release specifications and ICH Q5E comparability when a manufacturing change is introduced; the release panel also includes size-exclusion chromatography for aggregate content, capillary electrophoresis for purity, and cell-based potency testing calibrated against the international reference standard. The manufacturing sequence begins with CHO-derived bulk drug substance that is buffer-exchanged by tangential flow filtration into a histidine-trehalose formulation buffer, passed through a 0.22 μm sterilizing-grade filter, aseptically filled into Type I glass vials, partially stoppered, and lyophilized. The lyophilization cycle is product-specific: the amorphous trehalose matrix suppresses crystallization and maintains the protein’s native structure, while the primary-drying shelf temperature is governed by the collapse temperature of the formulation; full chamber-pressure and shelf-temperature ramps are not public for commercial product, but the cycle is validated against residual moisture by Karl Fischer titration and against cake appearance by visual inspection. The terminal dosage form is a white to pale yellow lyophilized powder for concentrate for solution for infusion. The reconstituted single-dose vial contains no preservative, and the approved in-use statement limits storage to 24 hours at 2–8 °C; from a microbiological standpoint it is therefore expected to be transferred directly to an infusion bag without intermediate pooling. Refreezing the reconstituted solution is not supported by stability data.
| Product presentation | Standard / regulation | Test or process requirement |
|---|---|---|
| Lyophilized IV vial | USP <71>, Ph. Eur. 2.6.1 | Sterility after incubation; membrane filtration method |
| Lyophilized IV vial | USP <85>, Ph. Eur. 2.6.14 | Bacterial endotoxin limit according to maximum bolus dose |
| Subcutaneous solution | USP <787>, Ph. Eur. 2.9.19 | Subvisible particle limits for ≥10 μm and ≥25 μm |
| Multi-dose vial | USP <51> | Antimicrobial effectiveness of benzyl alcohol-containing diluent |
| ADC intermediate | ICH Q6B, ICH Q3D | Conjugated protein specifications and elemental impurity control |
At the 440 mg strength, the multi-dose lyophilized vial achieves the same nominal 21 mg/mL reconstituted protein concentration but differs in preservative-containing diluent and excipient mass ratios. The dry formulation combines 440 mg trastuzumab with 400 mg α,α-trehalose dihydrate, 9.9 mg L-histidine hydrochloride monohydrate, 6.4 mg L-histidine, and 1.8 mg polysorbate 20. Reconstitution with 20 mL Bacteriostatic Water for Injection containing 1.1% benzyl alcohol yields 21 mg/mL trastuzumab. The preserved system is qualified for antimicrobial effectiveness under USP <51>; the benzyl alcohol content triggers a label contraindication for use in neonates, infants, and populations with known benzyl alcohol toxicity risk. The filling line for the multi-dose format is configured to maintain a headspace and closure geometry that tolerates repeated needle puncture without loss of container closure integrity, and closure integrity is validated according to USP <1207> or an equivalent deterministic package integrity method. In manufacturing, the bulk formulation process remains aseptic: buffer exchange into the histidine-trehalose-polysorbate 20 matrix, 0.22 μm filtration, aseptic filling, and lyophilization; the multi-dose container requires additional stability and integrity studies because the in-use period extends to 28 days at 2–8 °C after reconstitution. The terminal presentation is a 440 mg lyophilized powder for concentrate for solution for infusion, intended for repeated withdrawal from a single vial in a controlled oncology pharmacy setting. Withdrawal precision is governed by the nominal 21 mg/mL concentration; institutional dose rounding is an in-use policy decision outside the API manufacturer’s control.
Subcutaneous administration requires a formulation distinct from the intravenous lyophilized presentations: a ready-to-use solution containing 600 mg trastuzumab and 10,000 U hyaluronidase-oysk in 5 mL, corresponding to 120 mg/mL antibody and 2,000 U/mL hyaluronidase. The excipient system includes L-histidine, L-histidine hydrochloride monohydrate, α,α-trehalose dihydrate, L-methionine, and polysorbate 20; the formulation is filled as a single-dose vial without preservative. The approved dosing schedule is 600 mg injected subcutaneously over 2–5 minutes every 3 weeks, and the label warns that this product must not be administered intravenously. The applicable compliance framework includes USP <1>, USP <71>, USP <85>, USP <787>, USP <790>, Ph. Eur. 2.6.1, Ph. Eur. 2.6.14, and Ph. Eur. 2.9.19. The downstream manufacturing route concentrates the CHO-derived bulk drug substance by ultrafiltration/diafiltration to 120 mg/mL, introduces polysorbate 20 and methionine as stabilizers, and then mixes the solution with hyaluronidase-oysk under low-shear conditions; the order of excipient addition is controlled because the enzyme is less robust than the antibody and can be damaged by high interfacial stress. The fill line uses positive-displacement piston pumps and larger-diameter fluid paths to limit shear-induced aggregation and subvisible particle formation at high protein concentration. The finished article is a 5 mL single-dose vial containing a clear to opalescent solution for subcutaneous injection; because no preservative is present, any unused portion is discarded, and the vial is not suitable for multi-dose withdrawal.
If the intent is maytansinoid antibody-drug conjugate production, trastuzumab API is first buffer-exchanged into a conjugation buffer and then partially reduced at interchain disulfide bonds using tris(2-carboxyethyl)phosphine or dithiothreitol under controlled pH and temperature; the number of generated free sulfhydryls determines the final conjugation stoichiometry. The reduced antibody is reacted with a molar excess of the SMCC-DM1 reagent, then the conjugate is purified by tangential flow filtration and size-exclusion chromatography to remove unconjugated linker-payload, organic solvent, and high-molecular-weight aggregate. The drug-to-antibody ratio is quantified by ultraviolet/visible absorbance deconvolution and orthogonal chromatography; the approved conjugate product documentation reports a target average DAR of approximately 3.5, while the precise lot-release interval is proprietary. Batch-to-batch variability in the conjugation reaction is controlled by in-process DAR and residual free payload limits, typically measured by reversed-phase HPLC. After conjugation, the bulk is buffer-exchanged into sodium succinate buffer with sucrose and polysorbate 20, aseptically filtered through a 0.22 μm membrane, filled, and lyophilized. Compliance for this route must include ICH Q6B for conjugated protein specifications, ICH Q3D for elemental impurities because residual metals from the reduction or conjugation step may be present, ICH Q3C for residual solvents from the linker-payload preparation, and ICH Q5A(R2) for viral safety of the biological intermediate. The finished conjugate is a 100 mg or 160 mg single-dose lyophilized powder; after reconstitution with Sterile Water for Injection the nominal concentration is 20 mg/mL ado-trastuzumab emtansine. This product is not considered equivalent to unconjugated trastuzumab; dose conversion, infusion rate, and toxicity monitoring follow the conjugate label, not the unconjugated antibody label.
Once the lyophilized or liquid drug product reaches a hospital or centralized oncology pharmacy, the final downstream operation is the preparation of the patient-specific infusion. The approved labeling instructs transfer of the calculated dose into a 250 mL 0.9% Sodium Chloride Injection, USP polyvinyl chloride or polyolefin infusion bag; dextrose 5% solution is specifically contraindicated because exposure to dextrose-containing diluents has been associated with increased protein aggregation and particle formation. The diluted admixture is not preserved and is assigned an in-use storage limit of 24 hours at 2–8 °C. Administration is by intravenous infusion over 30–90 minutes through a 0.22 μm inline filter; the label prohibits intravenous push or bolus injection. Compounding staff handle the admixture under USP <797> for sterile preparation and USP <800> for hazardous drug containment because trastuzumab carries embryo-fetal toxicity warnings; closed system transfer devices, negative-pressure compounding areas, and leak-tight containers are required by that hazard assessment. The dose schedule is weight-based: the approved label specifies a loading dose of 4 mg/kg followed by weekly 2 mg/kg for the weekly intravenous regimen, and a loading dose of 8 mg/kg followed by 6 mg/kg every 3 weeks for the three-weekly regimen in the approved metastatic gastric cancer indication. Terminal point of the admixture chain is a ready-to-infuse 250 mL sodium chloride bag containing a patient-specific trastuzumab dose; no other drug should be added to the same bag, and the final infusion must be visually inspected for particulates and discoloration before administration.
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Trastuzumab Injection Pharma Grade API is a recombinant humanized IgG1 monoclonal antibody produced in Chinese hamster ovary (CHO) cell culture and released as a biotechnology-derived active pharmaceutical ingredient. The descriptor “for Tablet / Capsule / Granule / Injection, Oral & Injectable” functions as an inventory-grade identifier rather than a regulatory authorization for all listed routes; the intact molecule has a molecular weight of approximately 145 500 Da and is subject to acid-catalyzed unfolding and pepsin-mediated fragmentation in the stomach. Published data for conventional oral solid dosage delivery of native trastuzumab is limited, and the native molecule is not absorbed intact across intestinal epithelium at therapeutically relevant fractions. The injection grade is therefore supplied as a sterile-filtered liquid or lyophilized powder intended for aseptic formulation into intravenous or other injectable presentations, while any use in tablet, capsule, or granule lines would require a separately qualified enteric or nanocarrier system. The “Pharma Grade” designation indicates manufacture under current good manufacturing practice as described in 21 CFR 210 and 21 CFR 211, viral safety evaluation according to ICH Q5A(R2), and product quality assessment aligned with ICH Q6B. A discrete catalog model number is not assigned; the grade descriptor itself functions as the model identifier in technical and regulatory documentation.
The injectable-grade material is released against a panel of compendial and product-specific methods that reflect the structural complexity of a 145 500 Da glycoprotein. Liquid presentations are typically controlled for pH 5.8–6.2 by USP <791>, osmolality 250–350 mOsm/kg by USP <785>, and protein concentration by ultraviolet absorbance at 280 nm using the product-specific extinction coefficient. Bacterial endotoxin is controlled by USP <85> with a typical limit of ≤0.5 EU/mg; sterility is confirmed by USP <71>; subvisible particulate matter is controlled by USP <787> or USP <788> as appropriate. Size-exclusion high-performance liquid chromatography separates monomer, high-molecular-weight aggregate, and low-molecular-weight fragment species; a representative release target for monomer is ≥95.0% with high-molecular-weight species ≤5.0%. Host cell protein by enzyme-linked immunosorbent assay is typically controlled at ≤100 ng/mg, and residual Protein A leached from affinity capture is typically controlled at ≤20 ng/mg. Charge variant distribution by ion-exchange chromatography and N-linked glycan profiling by hydrophilic interaction chromatography are product-specific and are set according to ICH Q6B comparability rather than fixed small-molecule impurity thresholds. Where the product is supplied as a lyophilized powder, residual moisture is controlled by Karl Fischer titration, typically ≤3.0%; the powder is reconstituted only with the designated diluent to avoid pH shift and aggregation.
| Attribute | Method or standard | Representative release criterion |
|---|---|---|
| Identity | Peptide mapping, LC-MS/MS | Concordant with reference standard; ICH Q6B |
| Purity | SEC-HPLC | Monomer ≥95.0%; high-molecular-weight species ≤5.0% |
| Potency | Receptor-binding or cell-based assay | 80–125% relative to reference standard |
| Bacterial endotoxin | USP <85> | ≤0.5 EU/mg |
| Sterility | USP <71> | No growth |
| pH | USP <791> | 5.8–6.2 |
| Water content (lyophilized) | Karl Fischer titration | ≤3.0% |
In aseptic filling suites, the API is typically received as a sterile-filtered frozen liquid or lyophilized powder. Frozen liquid is thawed under controlled conditions at 2–8 °C for 24–48 h; uncontrolled thawing at room temperature can produce local pH and concentration gradients that promote aggregation. The thawed material is transferred with peristaltic or rotary piston pumps under conditions validated to limit shear; high shear in rotary piston pumps with tight clearance can increase subvisible particles above the USP <787> reporting thresholds if fill speed exceeds the qualified range. Contact surfaces should be evaluated for protein adsorption and particulate generation; silicone oil from pre-filled syringe barrels has been associated with protein aggregation in monoclonal antibody formulations, and fluoropolymer-coated or silicone-free surfaces are preferred where long hold times are required. Fill operations are conducted in ISO 14644-1:2015 Class 5 or EU GMP Annex 1 Grade A zones with unidirectional airflow and terminal filter integrity testing. Sterile filtration through 0.22 μm polyvinylidene fluoride or polyethersulfone membranes is standard; the filter train is validated for bacterial retention, product compatibility, and extractables. Terminal sterilization by autoclave or gamma irradiation is not appropriate because the protein denatures at elevated temperature and radiation-induced fragmentation can compromise potency. Endotoxin control requires depyrogenation of product-contact equipment by dry heat at 250 °C or validated alkaline wash; sterile filtration removes organisms but not endotoxin. The formulated solution is typically diluted into 0.9% sodium chloride injection before administration and should not be frozen after dilution. Process hold times at room temperature should be limited; published data for this specific configuration is limited, but monoclonal antibody solutions generally show increased aggregate formation after multiple freeze-thaw cycles or prolonged storage above 8 °C.
The native antibody has no current pharmacopoeial monograph for oral trastuzumab tablets, capsules, or granules, and no ICH Q6B-aligned release specification exists for an oral solid dosage form of this molecule. Conventional direct compression and granulation operations are not compatible with the intact antibody. Dry blending with microcrystalline cellulose or lactose exposes the protein to hydrophobic interfaces and mechanical stress; compression pressures above 100 MPa can induce aggregation in dried protein formulations unless the API is co-processed with a stabilizing matrix. Wet granulation with water or ethanol-water mixtures introduces air-liquid interfaces, and subsequent drying above 40 °C accelerates deamidation, methionine oxidation, and aggregate formation. The gastrointestinal environment further limits absorption: pepsin cleaves the hinge region at gastric pH 1.2–3.5, and the molecular weight of 145 500 Da restricts passive transcellular uptake. Any oral tablet, capsule, or granule application would require a separately qualified enteric or nanocarrier system, stability data under ICH Q1A(R2) conditions, and a bioavailability study demonstrating intact drug exposure. Without such data, the oral route remains outside the validated scope of this injection-grade API.
Unlike small-molecule APIs used in direct compression and high-shear granulation, the biopharmaceutical operating envelope for trastuzumab injection grade is constrained by cold-chain logistics, aseptic handling, and protein aggregation limits. Small-molecule APIs often tolerate drying at 60–80 °C, micronization, and organic solvent granulation; this API cannot be micronized, must be maintained at 2–8 °C for liquid storage, and is incompatible with hot-melt extrusion above its denaturation onset. Compared with the conjugated derivatives trastuzumab emtansine and trastuzumab deruxtecan, the unconjugated API has a drug-to-antibody ratio of 0 and does not contain a cytotoxic linker-payload; consequently, containment, waste handling, and operator protection are governed by conventional biological safety policies rather than cytotoxic drug requirements. Compared with biosimilar trastuzumab products, the API is expected to demonstrate comparability in primary structure, higher-order structure, glycosylation, charge variants, and biological activity according to ICH Q5E. Batch-to-batch variance in host cell protein clearance, glycan occupancy, and aggregate content should be monitored with statistical process control because these variables can alter pharmacokinetic clearance and immunogenicity risk. The product should not be co-formulated with amine-based buffers that raise pH above the stability range, and it should not be exposed to strong oxidizing agents unless the impact on methionine residues in the Fc region is specifically controlled.
| Parameter | Small-molecule API | Trastuzumab Injection Pharma Grade API |
|---|---|---|
| Molecular weight | 200–500 Da | 145 500 Da |
| Thermal processing range | Dry heat 60–80 °C | Cold chain 2–8 °C; denaturation above 40 °C |
| Terminal sterilization | Autoclave or dry heat | Sterile filtration only |
| Conventional oral absorption | Often passive transcellular transport | Native antibody not absorbed intact |
| Validated dosage-form routes | Tablet, capsule, granule | Injectable solution, lyophilized powder |
Batch documentation for the injectable grade includes the certificate of analysis, viral safety summary under ICH Q5A(R2), and stability assignment under ICH Q5C. The API is released with a defined retest period supported by stability data; typical storage is −20 °C for frozen liquid or 2–8 °C for lyophilized powder. Repeated freeze-thaw cycles should be avoided; if thawing exceeds 48 h at 2–8 °C, subvisible particle counts may increase. Equipment cleaning validation must address protein carryover at low parts-per-million levels; 21 CFR 211.67 requires written cleaning procedures, and ICH Q7 provides guidance for cleaning validation in API manufacturing. These controls, rather than a simple interchangeability statement, define the boundary between this injection pharma grade material and lower-grade research reagents.