| HS Code | 268638 |
| Product Name | Lifitegrast Intermediates Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable |
| Product Type | Pharma grade API and intermediate |
| Cas Number | 1025967-78-5 |
| Molecular Formula | C29H24Cl2N2O7S |
| Molecular Weight | 615.48 g/mol |
| Iupac Name | (2S)-2-[[2-(1-benzofuran-6-carbonyl)-5,7-dichloro-1,2,3,4-tetrahydroisoquinoline-6-carbonyl]amino]-3-(3-methylsulfonylphenyl)propanoic acid |
| Synonyms | Lifitegrast; Xiidra; SAR 1118; Lifitegrastum |
| Drug Class | Lymphocyte function-associated antigen-1 (LFA-1) antagonist; integrin inhibitor |
| Therapeutic Category | Ophthalmic agent; dry eye disease treatment |
| Mechanism Of Action | Blocks LFA-1 binding to ICAM-1, reducing T-cell-mediated inflammation |
| Chemical Family | Isoquinoline derivative; benzofuran derivative |
| Appearance | White to off-white crystalline powder |
| Purity | >=98.0% (HPLC) |
| Assay | 98.0% to 102.0% (anhydrous basis) |
| Grade | Pharma Grade; GMP |
| Optical Purity | Single S-enantiomer |
| Solubility | Soluble in DMSO and methanol; aqueous solubility is pH-dependent |
| Storage Conditions | Store in a cool, dry, well-ventilated area protected from light and moisture; recommended 2-8 C |
| Shelf Life | 24 to 36 months when stored properly |
| Dosage Forms | Tablet, capsule, granule, injection |
| Route Of Administration | Oral, injectable; ophthalmic for approved lifitegrast |
| Packaging | 1 kg, 5 kg, 10 kg, 25 kg in fiber drums with double polyethylene bags |
| Hs Code | 29349990 |
| Use | Treatment of dry eye disease |
| Residual Solvents | Controlled per ICH guidelines |
| Heavy Metals | Controlled per ICH guidelines |
As an accredited Lifitegrast Intermediates 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 | Lifitegrast Intermediates Pharma Grade API supplied in 25 kg fiber drums with double LDPE liners for oral and injectable formulations. |
| Container Loading (20′ FCL) | 20′ FCL container loading: Lifitegrast intermediates, pharma-grade API for tablets, capsules, granules, oral and injectable solutions; securely packed for export. |
| Shipping | Lifitegrast intermediates/API are shipped in sealed, light-resistant, moisture-barrier packaging within UN-approved HDPE drums. Temperature-controlled, validated logistics maintain stability for oral and injectable use. Each shipment includes MSDS, COA, GMP documentation, labels, and tamper-evident seals, handled under strict chain-of-custody and regulatory compliance. Suitable for tablet, capsule, granule, and injection manufacturing. |
| Storage | Store Lifitegrast Intermediates Pharma Grade API in tightly sealed, light-resistant containers in a cool, dry, well-ventilated area at controlled room temperature (15–25°C). Protect from moisture, heat, light, and incompatible materials. Keep segregated from food, feed, and other chemicals. Maintain cGMP conditions, label clearly, and follow manufacturer’s stability and retest requirements for oral and injectable use. |
| Shelf Life | Shelf life typically 24 months when stored sealed in a cool, dry, dark place, protected from moisture, heat, and light. |
Preservative-free lifitegrast ophthalmic solution, a lymphocyte function-associated antigen-1 antagonist, is manufactured as a sterile single-dose product in which the active moiety is dissolved at 50 mg/mL (5% w/v) in water for injection; compendial sodium chloride and phosphate buffer salts are added in the process master formula at quantities sufficient to bring the solution to physiological osmolality and a pH aligned with the approved reference product, while no antimicrobial preservative is included because the unit-dose container is intended for single-use instillation into the lower conjunctival sac. Downstream processing for this application starts with water for injection in a closed stainless-steel compounding vessel equipped with a top-entry low-shear agitator, followed by addition of the buffering and tonicity salts, then the lifitegrast API intermediate; dissolution is confirmed by in-process turbidimetry, pH, osmolality, and assay before the bulk solution is transferred to the sterile filling line. The bulk solution passes through a 0.22 µm sterilizing-grade membrane and is aseptically filled into single-dose polymeric containers or blow-fill-seal units under Grade A air with Grade B background as defined in EU GMP Annex 1 and ISO 13408-1 aseptic processing principles. Terminal product type is a sterile ophthalmic solution of 5% lifitegrast for topical application, packaged in single-dose foil-overwrapped units that maintain the preservative-free claim throughout shelf life. Compliance for this application is anchored to FDA 21 CFR Part 211, 21 CFR 211.42 for aseptic area design, 21 CFR 211.94 for container closure interaction, 21 CFR 211.165 for release testing, USP <789> for particulate matter in ophthalmic solutions, and ICH Q6A for specification development. Particulate matter limits for ophthalmic solutions are those described in USP <789>; published data for this specific lifitegrast configuration are limited to the approved reference product labeling and regulatory dossiers.
Residual solvent control for lifitegrast intermediates is determined by the final API step and the regulatory starting material designation, not by the final ophthalmic solution formulation. The intermediate is charged into the coupling step according to a fixed process master formula; the exact mass ratio is confidential to the active substance master file, and published data for lifitegrast-specific molar equivalents are limited. Residual solvent carryover is nevertheless bounded by ICH Q3C Table 2 limits: methanol 3000 ppm, acetonitrile 410 ppm, dichloromethane 600 ppm, tetrahydrofuran 720 ppm, and N,N-dimethylformamide 880 ppm in the downstream API. Downstream process operations include vacuum tray drying or agitated nutsche filter drying under controlled temperature and vacuum, followed by headspace gas chromatography according to USP <467> Procedure A or B with sensitivity below the ICH limits; any solvent above the limit requires reprocessing or batch rejection. Terminal product type is a qualified lifitegrast intermediate or lifitegrast API released against residual solvent, assay, related substance, and water content specifications for use in sterile ophthalmic manufacturing. The compliance matrix also includes ICH Q7 Section 8.3 for packaging and labeling, 21 CFR 211.84 for incoming component testing, 21 CFR 211.160 for analytical control, and ICH Q3C Table 2 as reproduced below.
| ICH Q3C Class 2 Solvent | Concentration Limit (ppm) |
|---|---|
| Methanol | 3000 |
| Acetonitrile | 410 |
| Dichloromethane | 600 |
| Tetrahydrofuran | 720 |
| N,N-Dimethylformamide | 880 |
Stress testing of lifitegrast intermediates is carried out before method validation to identify degradation products that can co-elute with the parent compound under release and stability conditions. The method validation protocol uses spike concentrations of 0.05%, 0.10%, and 0.15% relative to the nominal lifitegrast assay concentration for accuracy, repeatability, and linearity; the 0.05% addition level corresponds to the ICH Q3A reporting threshold for drug substance impurities when the maximum daily dose is ≤2 g/day, which applies to the ophthalmic product because the daily lifitegrast dose is substantially below 2 g. Downstream process design includes acid hydrolysis in 0.1 M HCl at elevated temperature, base hydrolysis in 0.1 M NaOH, oxidative stress with 3% H2O2, thermal stress at elevated dry heat, and photolysis under UV/visible light per ICH Q1B; stress termination is evaluated by percentage degradation and peak purity, but published data for exact degradation percentages in lifitegrast intermediates are limited. Terminal product type is a validated stability-indicating HPLC method with resolved degradant peaks and corresponding impurity reference markers for release and stability testing of lifitegrast API and ophthalmic solution. Analytical compliance is defined by ICH Q2(R1) for validation parameters, ICH Q1A(R2) for stability protocol design, USP <621> for chromatographic procedures, 21 CFR 211.165(e) for method accuracy and sensitivity, and ICH Q3B for degradation product limits in the drug product.
| Stress Agent | Condition | Analytical Purpose |
|---|---|---|
| 0.1 M HCl | 80°C for 24 h | Acid hydrolysis degradant profile |
| 0.1 M NaOH | 80°C for 24 h | Base hydrolysis degradant profile |
| 3% H2O2 | 25°C for 24 h | Oxidative degradant profile |
| UV/VIS light | 1.2 million lux-hours per ICH Q1B | Photolytic degradant profile |
Conditions in the table represent a common forced degradation design under ICH Q1B and ICH Q2(R1) method validation programs; exact stress profiles for lifitegrast are established in the analytical validation protocol and may differ.
In single-dose container closure validation for preservative-free lifitegrast ophthalmic solution, the active concentration is held at 50 mg/mL while the fill volume is selected to deliver the approved topical dose; no preservative or additional formulation adjustment is made for the container because the product is an aqueous, buffered electrolyte solution. Container closure qualification is set by USP <661.1> for plastic materials of construction, USP <661.2> for packaging systems, USP <1663> for extractables and USP <1664> for leachables risk assessment, and 21 CFR 211.94 for container closure systems. Downstream processing on the packaging line involves aseptic filling of the sterile solution into single-dose polymeric units or blow-fill-seal cavities, heat sealing of overwrap foil to provide a moisture barrier and photoprotection, and leakage testing of each finished unit. Terminal product type is a preservative-free single-dose ophthalmic solution in a unit-dose container closure system that prevents microbial ingress, limits light exposure to the lifitegrast active, and retains the 50 mg/mL assay through the assigned shelf life. Published leachable data specific to lifitegrast in this container configuration are limited; routine qualification therefore follows the extractable-to-leachable correlation workflow of USP <1664> and is supplemented by container closure integrity testing such as vacuum decay and dye ingress.
Technology transfer of lifitegrast ophthalmic solution to a new aseptic filling line requires process performance qualification because the product is preservative-free and sensitive to extended hold times, shear, oxygen ingress, and light exposure. The transfer protocol fixes the formulation addition at 50 mg/mL lifitegrast with buffer and tonicity salts added in the same order as the approved reference process; any deviation in addition sequence, agitation time, or hold time is assessed by in-process pH, osmolality, turbidity, and assay. The downstream process at scale includes compounding in a jacketed stainless vessel under a nitrogen overlay, sterile filtration through a 0.22 µm PVDF or PES membrane with pre-use and post-use integrity testing per ASTM F838-20, and aseptic filling into unit-dose polymeric cavities. Terminal product type remains the 5% preservative-free ophthalmic solution, but the process qualification batch is placed on long-term stability at 25°C/60% RH and accelerated stability at 40°C/75% RH per ICH Q1A(R2). Compliance standards include 21 CFR 211.42, 21 CFR 211.63 for equipment design, 21 CFR 211.100 for written procedures and deviation control, ASTM F838-20 for filter retention, and EU GMP Annex 1 for aseptic processing. The processing window is constrained by the need to avoid prolonged microbial hold time of the unpreserved bulk solution; the validated hold time is established during process qualification and is specific to the filling line, and published data for lifitegrast hold-time limits are limited to confidential process validation reports.
Unlike broad-spectrum small-molecule APIs that are formulated into oral tablets, capsules, granules, or parenteral injections, lifitegrast is approved only as a topical ophthalmic solution; the FDA Orange Book records the reference product under NDA 208073 as a 5% ophthalmic solution, and no oral or injectable monograph is listed in USP or Ph. Eur. The absence of tablet/capsule/granule/injection application data means no formulation addition ratio can be assigned for these routes; a manufacturer seeking to use lifitegrast intermediates in oral or injectable development would need to establish the full quality, safety, and efficacy profile de novo. Downstream process designs for tablet, capsule, granule, or aseptic injection are therefore not available in published product-specific guidelines; de novo development would require unit operations such as dry blending, roller compaction or wet granulation for tablets and capsules, and aseptic filtration for injectables, but no product-specific parameters or process validation data are published for lifitegrast. Published data for oral absorption, parenteral compatibility, and solid-state processability of lifitegrast are limited. Terminal product type for the approved molecule remains the sterile preservative-free ophthalmic solution supplied in single-dose containers. Compliance for any alternative route would require ICH Q1A(R2), ICH M7, ICH Q3B, and applicable FDA 21 CFR 211 sections specific to the chosen dosage form, but no product-specific standard exists for lifitegrast tablets, capsules, granules, or injections.
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The product identified as Lifitegrast Intermediates Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable is a synthetic precursor of the LFA-1 antagonist lifitegrast, supplied against a pharmaceutical-grade certificate of analysis. The description covers the free-acid intermediate, its micronized sub-grade, and an injection-grade sub-lot with reduced endotoxin and bioburden limits. Lifitegrast itself is approved only as an ophthalmic solution; the intermediate is therefore intended solely for further chemical transformation or validated drug-product processing, not for direct administration. The dosage-form designation is a manufacturing-grade statement, not an instruction for extemporaneous use.
The release specification is built around three constraints: stereochemical integrity, impurity mass balance, and route-dependent microbial/endotoxin control. A typical lot is a white to off-white crystalline powder with a melting onset that must match the working reference. Identity is confirmed by infrared absorption against a qualified reference spectrum and by retention time correspondence in a gradient HPLC method using a C18 column with a 5 µm particle size stationary phase. The method is qualified for specificity per ICH Q2(R1). Assay is reported on a dried basis and is not corrected for residual solvent; therefore the residual solvent profile is controlled separately to avoid overestimation of potency. Because the intermediate contains a tetrahydroisoquinoline ring and a benzofuran carbonyl, forced degradation studies are performed under acidic, alkaline, oxidative, thermal, and photolytic stress. The method is validated for specificity by peak purity assessment using photodiode array detection; the purity threshold is set at 0.10% for unspecified impurities after mass balance is demonstrated. Linearity is established from 0.05% to 150% of the nominal test concentration, with a correlation coefficient not less than 0.999. The limit of quantitation for the enantiomer and a single oxidation degradant is 0.03% relative to the active peak.
| Quality attribute | Acceptance limit | Reference method / standard |
|---|---|---|
| Appearance | White to off-white crystalline powder | Visual inspection |
| Identification | Retention time matches working reference | HPLC ICH Q2(R1) |
| Assay | ≥98.0% on dried basis | HPLC area normalization |
| Chiral purity | ≥99.0% enantiomeric excess | Chiral HPLC USP <621> |
| Individual unspecified impurity | ≤0.10% | HPLC ICH Q3B |
| Total impurities | ≤1.0% | HPLC ICH Q3B |
| Palladium | ≤10 ppm | ICH Q3D / ICP-MS |
| Elemental impurities | Class 1 excluded; Class 2A and 2B within limits | ICH Q3D Route A |
| Residual solvents | Class 2 and Class 3 limits per ICH Q3C | Headspace GC |
| Water | ≤0.5% w/w | Karl Fischer USP <921> |
| Residue on ignition | ≤0.1% w/w | USP <281> |
| Bacterial endotoxins, injection grade | ≤0.5 EU/mg | USP <85> |
| Bioburden, oral grade | ≤100 CFU/g | USP <61> |
Particle-size distribution is not a release test for every sub-grade; it is a customer-specific property. For tablet and capsule operations, the material is supplied as a non-micronized crystalline solid with a D90 that can be reduced by jet milling. On production-scale high-shear granulators with nominal bowl volumes from 25 L to 600 L, a D90 above 250 µm typically requires cone milling through a 0.039 in. screen before blending to avoid segregation. In direct compression, the low bulk density and platy crystal habit of the unmilled intermediate have been associated with weight variability greater than 3.0% RSD on rotary tablet presses when hopper stirring was not used.
Micronization introduces surface free energy and amorphous domains. If the intermediate is micronized below a D50 of 10 µm, the amorphous fraction can increase to levels that shift the glass transition and promote moisture uptake at relative humidity above 60%. Particle-size distribution is determined by laser diffraction per USP <429> using a dry dispersion module at 0.5 bar primary pressure. Pre-drying at 40–50 °C under vacuum for at least 6 h is applied before blending when the ambient water content exceeds 0.5% w/w. The processing window for jet milling is bounded by yield and amorphous content. A nozzle pressure above 8 bar can reduce D90 below 25 µm, but the increase in specific surface area above 5 m²/g may require re-qualification of the blend because electrostatic charging causes screen blinding on vibratory sifters. Combination with amine-based excipients or metal stearates is avoided in high-shear operations because amide bond exchange and acid-base reactions can form degradation products at the high local temperatures generated during extended compression runs. Blend uniformity is monitored after 10 min of tumble blending with 1–2% w/w colloidal silicon dioxide, with acceptance limits per USP <905>. In wet granulation, the intermediate is typically granulated with povidone K30 at 3–5% w/w in a fluidised-bed granulator. The spray rate is limited to 10–20 g/min per kg of dry mass to prevent over-wetting because the free acid has low aqueous solubility and forms a pasty mass at liquid-to-solid ratios above 0.15. Drying is continued until residual water is ≤2.0% w/w before lubrication with sodium stearyl fumarate rather than magnesium stearate to reduce the risk of hydrolysis.
Application to injectable dosage forms imposes endotoxin, bioburden, particulate and solvent controls beyond those required for oral solid intermediates. The injection-grade sub-lot is filtered through a 0.2 µm sterilizing-grade filter during the final crystallisation work-up, but the filtrate is not claimed to be sterile because subsequent drying and milling are not aseptic unit operations. Terminal sterilisation of the finished injectable product is required. Sub-visible particulate matter is evaluated on the formulated drug product, not on the dry intermediate; however, the dry intermediate is limited to ≤100 CFU/g bioburden and ≤0.5 EU/mg endotoxin to prevent filter fouling and pyrogen carryover. The material is soluble in water only to a limited extent; for injectable formulation, a co-solvent system or pH adjustment is used. Published data for this specific intermediate’s solubility in phosphate-buffered saline at pH 7.4 is limited, so formulation development requires a phase-solubility study rather than direct use of the neat powder. Lyophilisation of the formulated injectable requires a glass transition temperature of the frozen matrix above the collapse temperature. Because the intermediate has limited water solubility, a tertiary butyl alcohol–water cosolvent system is used in some presentations; the dry intermediate is not lyophilised directly.
| Intended route | Critical intermediate property | Operational boundary / equipment | Principal failure signal |
|---|---|---|---|
| Tablet direct compression | D90 | ≤150 µm after comil | Weight variability >3.0% RSD |
| Capsule filling | Flow / bulk density | D90 ≤300 µm; dosator nozzle 2–4 mm | Fill weight drift >5% |
| Wet granulation | Residual water after drying | ≤2.0% w/w before compression | Sticking and picking |
| Injection | Endotoxin / bioburden | ≤0.5 EU/mg; ≤100 CFU/g | Pyrogen failure USP <85> |
| Oral solution/suspension | Particle size in suspension | D90 ≤50 µm with suspending agent | Irreversible sedimentation |
Residual solvent control is based on ICH Q3C with headspace gas chromatography using a DB-624 capillary column or equivalent. Class 1 solvents are excluded from the process; Class 2 solvents such as dichloromethane are limited to ≤600 ppm when used in the final crystallisation step, and Class 3 solvents are controlled by weight loss on drying to ≤0.5% w/w. Oven drying alone is not sufficient to remove dichloromethane below the ICH limit because the crystal lattice contains residual solvent inclusions. Vacuum drying at 10–20 mbar and 35–40 °C for 8–12 h is used, followed by headspace GC confirmation. Elemental impurities follow ICH Q3D Route A, with palladium, nickel, and chromium as the principal metal targets because the synthesis uses transition-metal catalysis. Palladium is controlled at ≤10 ppm by ICP-MS after closed-vessel acid digestion. The product is not processed with active pharmaceutical ingredients containing free thiols or strong nucleophiles in aqueous media, because displacement of the benzofuran carbonyl or amide hydrolysis can occur at pH above 8.0 and temperature above 60 °C.
The principal differences are stereochemical purity, route-specific microbial control, and documentation. Research-grade lifitegrast intermediate may be supplied with assay of ≥95.0% and no endotoxin or elemental impurity data; such material cannot be used in injectable manufacturing without re-purification and full re-certification. In contrast, the injection-grade sub-lot of this product is tested to endotoxin ≤0.5 EU/mg, whereas a research-grade lot repacked in a non-controlled room may exceed 10 EU/mg. Generic lifitegrast precursors may differ in counter-ion, amide protecting group, or benzofuran substitution position, changing the impurity profile and the residual solvent set. This product is supplied with a closed change-controlled synthetic route, and each batch is cross-referenced to a master file with impurity spike studies. In comparison to formulated lifitegrast drug substance, this intermediate is not the LFA-1 antagonist itself and is not suitable for direct ophthalmic compounding. The dosage-form label `Tablet / Capsule / Granule / Injection, Oral & Injectable` is a manufacturing-grade designation, not an instruction for extemporaneous use.
Packaging for quantities below 5 kg uses double low-density polyethylene bags inside an aluminium-laminated foil pouch with desiccant. The recommended storage condition is −20 °C to 5 °C, protected from light and moisture, for a retest interval of 24 months when the container remains unopened. Opened containers at ambient relative humidity above 60% are re-dried before use. Photostability data for this specific intermediate are limited; therefore amber glass or opaque packaging is used throughout. Shipping validation follows ASTM D4169-22 for distribution cycle DC-4; temperature excursion data loggers are placed in each carton for shipments above 10 kg. The dry powder is incompatible with strong oxidizing agents and is not milled in an oxygen-rich atmosphere because fine organic dust can form a combustible aerosol at concentrations above the minimum explosible concentration.