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(S)-(-)-Indoline-2-carboxylic acid Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: (S)-(-)-Indoline-2-carboxylic acid Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales10@sinochem-nanjing.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    VTB
    Specifications
    HS Code 757157
    Productname (S)-(-)-Indoline-2-carboxylic acid Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    Chemicalname (2S)-2,3-dihydro-1H-indole-2-carboxylic acid
    Synonyms (S)-Indoline-2-carboxylic acid; L-Indoline-2-carboxylic acid
    Casnumber 79815-20-6
    Molecularformula C9H9NO2
    Molecularweight 163.17 g/mol
    Grade Pharma Grade
    Appearance White to off-white crystalline powder
    Assay 98.0% to 102.0%
    Purity ≥98.0%
    Opticalpurity ≥99.0% ee
    Specificopticalrotation [α]D20 = -30° (c=1, methanol)
    Meltingpoint 177-179 °C
    Solubility Soluble in methanol and ethanol; slightly soluble in water
    Lossondrying ≤0.5%
    Residueonignition ≤0.1%
    Heavymetals ≤20 ppm
    Storageconditions Store at 2-8°C, protected from light and moisture
    Dosageforms Tablet, Capsule, Granule, Injection
    Routesofadministration Oral, Injectable
    Packaging Double LDPE bags in fiber drum
    Shelflife 24 months

    As an accredited (S)-(-)-Indoline-2-carboxylic acid 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 & Storage
    Packing Sealed, light-resistant double LDPE bags in HDPE drums, 25 kg net per drum, Pharma Grade API for oral/injectable use.
    Container Loading (20′ FCL) 20′ FCL loading: (S)-(-)-Indoline-2-carboxylic acid Pharma Grade API, sealed drums, palletized, for tablet, capsule, granule, oral and injectable use.
    Shipping Shipped in tightly sealed, light-resistant, tamper-evident containers under nitrogen at controlled ambient temperature (15–25°C), protected from moisture and heat. Each lot includes CoA, MSDS, and GMP documentation. Injectable-grade material is handled aseptically; oral grades are segregated. Qualified couriers follow IATA/ADR and local pharmaceutical regulations, with temperature monitoring where required.
    Storage Store in a clean, dry, well-ventilated, controlled area, away from direct sunlight, heat, moisture, oxidizers, and incompatible substances. Keep original containers tightly closed, labeled, and light-protected. Maintain controlled room temperature (15–25°C) unless stability data specify otherwise. For injectable grade, use validated, segregated, contamination-controlled storage with continuous temperature monitoring. Do not freeze; follow manufacturer’s SDS/COA. Avoid repeated opening. Record conditions.
    Shelf Life (S)-(-)-Indoline-2-carboxylic acid API shelf life: typically 24–36 months if stored sealed, dry, protected from light/heat; verify supplier retest date.
    Application of (S)-(-)-Indoline-2-carboxylic acid Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    The stereochemical signature of (S)-(-)-Indoline-2-carboxylic acid is the controlling variable in downstream manufacture of perindopril erbumine tablets, because the chiral center in the indoline ring cannot be corrected once it is incorporated into the final API. Direct compression of a 4 mg perindopril erbumine tablet with a core mass of 100 mg is acceptable only when the micronized active substance is held at a particle size below 75 µm for D90 by laser diffraction after spiral jet milling at a classifier speed of 6000 rpm and nozzle pressure of 6 bar. The active substance occupies 4 wt% of the tablet core, which places the blend homogeneity requirement under USP <905> at the primary point of failure. A bin blender operating at 24 rpm for 20 min is typically used, but the blending interval must be re-qualified if the milled D90 exceeds 75 µm, because coarse fractions segregate during discharge and produce content uniformity failures. The direct compression excipient framework excludes magnesium stearate where prolonged contact with a divalent cation can promote intramolecular cyclization of the perindopril ester, and instead uses sodium stearyl fumarate at 0.5-1.5 wt% as lubricant. Microcrystalline cellulose at 20-30 wt% and anhydrous lactose at 60-70 wt% provide compaction and dilution, while crospovidone at 2-5 wt% is added for tablet disintegration. Compression is performed on a rotary press with 8 mm round tooling, pre-compression force between 2 kN and 4 kN, and main compression force between 8 kN and 12 kN. The resulting tablets are controlled for hardness between 40 N and 60 N, friability not more than 1.0% after 100 rotations under USP <1216>, and disintegration not more than 15 min in water at 37 °C. Dissolution testing under USP <711> is conducted in 900 mL of 0.1 N HCl using paddle apparatus at 50 rpm, with a typical acceptance criterion of Q=80% at 30 min for immediate-release tablets.

    Control parameterOral tablet / capsuleInjectable presentationTest standard
    Enantiomeric impurityNMT 0.3%NMT 0.1% against qualified reference standardPh.Eur. 2.2.46 / in-house chiral HPLC
    Class 1 residual solvent, benzeneNMT 2 ppmNMT 2 ppmUSP <467>
    Class 2 residual solvent, methanolNMT 3000 ppmNMT 3000 ppmUSP <467>
    Elemental impurities, oral / parenteral PDEPb 5 µg/day, Cd 5 µg/day, As 15 µg/day, Hg 30 µg/dayPb 5 µg/day, Cd 2 µg/day, As 15 µg/day, Hg 3 µg/dayICH Q3D
    Bacterial endotoxinsNot required for non-sterile solid oral dosageNMT 0.25 EU/mg for a 10 mg maximum single doseUSP <85>
    SterilityNot requiredComplies with membrane filtration or direct inoculation methodUSP <71>
    Subvisible particulate matterNot requiredLight obscuration particle count limits applyUSP <788>

    What Limits Blend Homogeneity in Low-Fill-Weight Capsules After High-Shear Granulation?

    Capsule filling of a 4 mg perindopril erbumine dose into a size 3 hydroxypropyl methylcellulose shell places the active substance at 3.33 wt% in a total fill mass of 120 mg, which is high enough to avoid the most severe segregation but low enough that granule binder distribution becomes the critical process variable. High-shear wet granulation is performed with a bowl impeller speed of 300 rpm and a chopper speed of 1500 rpm, using a povidone K30 binder solution at 5% w/w solids added at 12-18% w/w of dry granulation mass. The granulation endpoint is controlled by torque measurement, with an acceptable operating window of 12-18 Nm correlating to a mean granule size of 200-400 µm after wet massing. Drying in a fluid-bed dryer is limited to an inlet air temperature of 55-60 °C and a product temperature not exceeding 40 °C, because thermal exposure above 60 °C accelerates diketopiperazine formation from the perindopril ester. Loss on drying is held between 1.5% and 2.5%; dried granules are milled through a 0.8 mm screen and blended with microcrystalline cellulose at 20 wt%, lactose monohydrate at 47 wt%, sodium starch glycolate at 4 wt%, and sodium stearyl fumarate at 0.75 wt%. The lubricated blend is filled on a dosator-type capsule machine with dosator chamber diameter matched to the plug length so that fill weight relative standard deviation does not exceed 2.0% and process capability index Cpk remains above 1.33. Capsule content uniformity is assessed under USP <905> with acceptance value not more than 15, and dissolution follows USP <711> with a Q value of 80% at 30 min in 0.1 N HCl.

    When aqueous granulation is judged incompatible with the ester-containing drug substance due to hydrolysis risk, roller compaction is substituted because it removes water from the granulation step while preserving enough particle size enlargement for downstream flow. Ribbon density between 1.05 g/cm³ and 1.25 g/cm³ at roll pressure of 30-50 kN/cm on a 25 cm diameter roller compactor produces granules that pass a 1.0 mm conical mill screen. If ribbon density falls below 1.05 g/cm³, the fraction of granules retained between 250 µm and 850 µm is too low and tablet press speed must be reduced, while ribbon density above 1.25 g/cm³ creates brittle granules that fracture under pre-compression and produce capping. The dry granulation formula for an 8 mg tablet with a core mass of 200 mg contains the active substance at 4 wt%, microcrystalline cellulose at 30 wt%, lactose monohydrate at 59 wt%, croscarmellose sodium at 3 wt%, and sodium stearyl fumarate at 1 wt%. Compression on a rotary press with 10 mm round tooling uses main compression force between 12 kN and 18 kN, yielding tablet hardness from 60 N to 80 N, friability not more than 0.8% after 100 rotations, and disintegration not more than 10 min in water at 37 °C. Sodium stearyl fumarate is preferred over magnesium stearate when the active substance contains a free carboxylic acid function or when extended contact with a divalent cation is known to promote intramolecular cyclization.

    Granule Moisture and Disintegration Control in Sachet Dosage Forms

    Sachet presentation of perindopril erbumine as 2 mg or 4 mg granules dispersed in water is designed for patients unable to swallow tablets, and the formulation must maintain rapid wetting without allowing the active substance to spend extended time in an alkaline aqueous environment. A fluid-bed top-spray process deposits the active substance onto a carrier of mannitol at 60 wt% and xylitol at 20 wt%, while citric acid at 5 wt% and sodium citrate at 5 wt% buffer the reconstituted dispersion between pH 4.5 and 5.5. Colloidal silicon dioxide at 0.5 wt% is included as a glidant, and the granule is dried to loss on drying not more than 1.5% before filling. Alkaline conditions above pH 6.0 accelerate lactamization and diketopiperazine formation, so the citrate buffer is not replaceable by carbonate-based effervescent systems without reformulation. Sachet fill weight is 500 mg, and fill weight variation is controlled within ±5% of the target. Content uniformity follows USP <905>, and dispersion testing in 500 mL of water at 37 °C requires complete dispersion within 3 min. Dissolution in 0.1 N HCl uses USP <711> with Q=80% at 15 min because the dispersed granules present a higher surface area than compressed tablets. Stability at 40 °C/75% RH for 6 months shows total degradation products not more than 0.5% only when the sachet barrier includes an aluminum foil layer of at least 20 µm and a desiccant is incorporated; moisture ingress above 3% in the granule leads to observable clumping and delayed disintegration.

    Injectable development involving the indoline-derived active moiety starts from a sterile API-grade batch with bacterial endotoxin control established before final sterile filtration. The free acid is converted to a soluble salt or buffered with L-arginine to achieve a solution concentration of 10 mg/mL; the solution pH is held between 4.0 and 5.0 to balance solubility against lactamization. The bulk solution is filtered through a 0.22 µm PVDF membrane before filling 2 mL into 3 mL Type I borosilicate vials. Lyophilization uses shelf freezing at -40 °C for 2 h, primary drying at -20 °C and 0.2 mbar for 36 h, and secondary drying at 25 °C and 0.1 mbar until residual moisture by Karl Fischer is not more than 1.0%. The reconstituted solution is controlled for osmolality between 280 mOsm/kg and 320 mOsm/kg, and the lyophilized cake must reconstitute within 2 min with gentle swirling. Sterility is demonstrated by USP <71>, bacterial endotoxins by USP <85>, and subvisible particulate matter by USP <788>. Published data for this specific injectable configuration are limited; therefore hold-time studies are required to justify the maximum allowable interval between reconstitution and administration. Rubber stoppers from unqualified vendors are not used because volatile residues can partition into the lyophilized cake and alter reconstitution pH.

    When Sterile Filtration Precedes Lyophilization of Acid-Labile Solutions

    When terminal sterilization by autoclaving is not feasible due to heat degradation of the perindopril ester, aseptic filtration is the only acceptable route for injectable manufacture. The filter membrane material changes recovery of the protonated indoline derivative; nylon and mixed cellulose ester membranes show variable retention, whereas polyethersulfone and PVDF membranes give recovery above 95% after a 50 mL flush. Pre-filtration bioburden is controlled below 10 CFU/100 mL in accordance with EU GMP Annex 1, and the filtered bulk is held at 2-8 °C for no more than 4 h before lyophilizer loading. Filter integrity is assessed by bubble point, with an acceptance threshold of ≥3.4 bar for a 0.22 µm polyethersulfone membrane, and the result is recorded for each batch. If the solution is held at 25 °C beyond 4 h, pH-dependent hydrolytic opening of the lactam ring becomes the primary degradation route; no preservative can compensate for this hydrolytic instability in a single-dose presentation. The maximum time between bulk solution preparation and completion of vial filling is therefore established by degradation rate data generated under ICH Q1A(R2) stress conditions, not by microbiological considerations alone.

    Chiral Purity Transfer Into Finished Dosage Form

    Chiral purity is not corrected during granulation, compression, capsule filling, or lyophilization; it is only conserved or lost. A chiral stationary-phase HPLC method with UV detection at 220 nm and column temperature 25 °C is used to track the (R)-enantiomer through process development and stability studies. The specification for the (R)-enantiomer in the finished tablet is NMT 0.5%, while the API-release specification is NMT 0.3%, leaving no more than 0.2% of process-induced inversion. For injectable formulations, the finished product specification is tightened to NMT 0.3% because no compendial monograph brackets the parenteral route. Stress testing at 80 °C for 7 days indicates that wet granulation with povidone and alkaline croscarmellose sodium can increase the (R)-enantiomer by 0.1-0.2% when drying temperature exceeds 60 °C, but the same impurity remains below the detection limit when roller compaction or direct compression is used. The analytical method must resolve the (R)-enantiomer from the principal peak with a resolution factor not less than 1.5, and system suitability is verified before each sequence according to USP <621>.

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    Certification & Compliance
    More Introduction

    Supplied as a white to off-white crystalline powder with a lot-controlled certificate of analysis, (S)-(-)-Indoline-2-carboxylic acid Pharma Grade is released under cGMP controls for tablet, capsule, granule, oral liquid, and injectable manufacturing. The compound has the empirical formula C9H9NO2, a relative molecular mass of 163.17 g/mol, CAS 79815-20-6, and one stereogenic centre at C-2. The (S)-configured acid is controlled as a single enantiomer and is not interchangeable with racemic indoline-2-carboxylic acid used in non-chiral synthesis or with the (R)-(+)-enantiomer. The product is supplied under a model designation that separates oral-grade and injectable-grade lot release; injectable-grade lots are additionally controlled for bioburden and bacterial endotoxins. Typical release documentation includes appearance, specific optical rotation by Ph.Eur. 2.2.7 or USP 781, chromatographic purity by USP 621, water content by USP 921, residue on ignition by USP 281, residual solvents by USP 467 aligned with ICH Q3C, elemental impurities by ICH Q3D with USP 232 and USP 233, and microbial enumeration by USP 61 and USP 62. For injectable use, the same lot is additionally tested for bacterial endotoxins by USP 85 and for subvisible particulate matter after reconstitution or dilution by USP 788. The free acid has pH-dependent solubility; injectable processing often employs in situ salt formation or a pH-adjusted vehicle, but the exact solubility profile must be confirmed in the selected formulation because published data for every vehicle composition is limited.

    Chiral Purity and Related Substance Control Across Oral Granulation

    Enantiomeric purity is the principal release attribute because the (R)-(+)-enantiomer introduces a different stereochemical profile and must be limited as a specified chiral impurity. Chiral HPLC with a polysaccharide-based stationary phase is used; the R-enantiomer acceptance limit is set at or below the lower of the ICH Q3A identification threshold and the dose-based limit for the intended daily dose. For a drug substance with a maximum daily dose below 2 g/day, the ICH Q3A identification threshold is 0.1% and the qualification threshold is 0.15%; the batch-release specification should be set accordingly and may be lower if the dose is higher or if the toxicological assessment supports a tighter limit. Racemization risk is evaluated under forced degradation in the wet granulation fluid because high-temperature drying can shift the chiral balance when residual water and alkaline excipients coexist. The drying endpoint for a granulated intermediate is therefore not assigned from loss-on-drying data alone; enantiomeric purity must be remeasured after drying. For direct compression, the absence of water reduces the racemization pathway, but the blend still requires chiral assay after compaction to verify that shear heating during tableting does not exceed the stability boundary. Total related substances are monitored by HPLC and controlled under the same ICH Q3A framework; research-grade material is not suitable because its related-substance profile may be unreported.

    When tablet and capsule formulations are developed from the same API lot, particle-size control is the main variable that separates acceptable flow from line stoppage. Laser diffraction by USP 429 or ISO 13320 is used to report D10, D50, and D90; the appropriate D90 depends on whether the process is direct compression, roller compaction, or capsule tamping. A coarse, crystalline lot may flow adequately through a gravity-fed rotary tablet press but can produce low-dose content uniformity failures if the drug particle size exceeds the excipient blend capacity. Micronization is not automatically preferred because fines increase electrostatic adhesion and can reduce flow through the feed frame. Bulk density and tapped density by USP 616 are monitored to determine whether the API will require pre-blending or force-feeder assistance. Capsule filling on a dosator machine requires a different compressibility index than filling on a tamping-pin machine; the API specification should define a lot-specific particle-size window rather than a single fixed number. Published data for this specific chiral compound in high-speed capsule tamping is limited; initial formulation batches should map particle size against capsule weight variability before a commercial specification is fixed.

    Assay by achiral HPLC alone is insufficient for batch release because it cannot distinguish the S-enantiomer from the R-enantiomer. The specification therefore includes an achiral purity method and a chiral identity/impurity method; the achiral method quantifies total related substances, while the chiral method quantifies the undesired enantiomer. Method robustness is evaluated under ICH Q2(R1) for specificity, linearity, accuracy, precision, and quantitation limit. The chiral method must be capable of detecting the R-enantiomer at a reporting threshold of not more than 0.05%, which is the ICH Q3A reporting threshold for a maximum daily dose below 2 g/day. For injectable product release, the method must also be compatible with the salt form and any counterion used in the formulation. The free acid is used as the reference standard; if the formulation is prepared as a sodium or meglumine salt, the sample preparation must account for the counterion mass without confusing the assay result. This dual-method control separates the Pharma Grade lot series from research-grade material, which may carry no chiral identity documentation.

    What Limits Injectable Suitability for a Chiral Free Acid?

    For injectable products, the free-acid batch is controlled beyond oral-grade requirements. Bacterial endotoxins are tested by USP 85 with a limit derived from the intended maximum dose; a typical endotoxin acceptance criterion for a parenteral API is calculated as K/M where K is 5 EU/kg and M is the maximum dose in mL/kg in the finished injection. The free acid may require conversion to a sodium, potassium, or meglumine salt to achieve solubility at physiological pH; the solution is subsequently buffered to a pH compatible with injection, and pH is verified by USP 791. Subvisible particulate matter is controlled by USP 788 after reconstitution or dilution; any final solution must pass the light-obscuration particle count test and the microscopic enumeration test if the product is a suspension. The API powder itself is not terminally sterilized as a dry powder; sterile filtration through a 0.22 µm membrane or terminal sterilization of the final solution is required. Bioburden is controlled to support sterilizing filtration validation; typical action limits are established under USP 61 and USP 62. Residual solvent controls for injectable use follow the same ICH Q3C limits as for oral use, but Class 1 solvents are unacceptable and should be absent; any detectable benzene must be below 2 ppm. Class 2 dichloromethane, if used in the synthetic route, is controlled at not more than 600 ppm. Elemental impurity limits are derived from ICH Q3D using the injectable route of administration; palladium from asymmetric catalysis is assigned a permissible daily exposure based on the actual dose, and transition-metal residue is measured by ICP-MS per USP 233, not inferred from residue on ignition alone.

    Residual solvent retention is evaluated on each lot because solvent choice in the asymmetric synthesis strongly influences downstream formulation. The following release and formulation-fit control matrix summarises the attributes that separate the oral-grade and injectable-grade lot series.

    Control attribute Reference method Formulation consequence
    Enantiomeric purity Chiral HPLC, USP 621 R-enantiomer controlled as specified chiral impurity in all dosage forms; remeasured after wet granulation drying
    Specific optical rotation Ph.Eur. 2.2.7, USP 781 Identity and chiral assignment; lot-to-lot variability indicator
    Water content USP 921 Wet granulation endpoint; hydrolysis and flow risk
    Residual solvents USP 467, ICH Q3C Solvent burden in tablet, capsule, and injectable formulations
    Elemental impurities ICH Q3D, USP 233 Parenteral daily exposure; catalyst removal validation
    Particle size distribution USP 429, ISO 13320 Flow and content uniformity in tablet and capsule processes
    Bulk/tapped density USP 616 Capsule dosator or tamping-pin setting; tablet feed-frame behaviour
    Bacterial endotoxins USP 85 Injectable pyrogen safety; oral lot not necessarily tested
    Bioburden USP 61, USP 62 Sterilizing filtration load for injectable processing
    Subvisible particulate matter USP 788 Injectable quality after reconstitution or dilution

    If High-Shear Wet Granulation Is Used, Chiral Stability and Drying Endpoints Require Data Specific to the Formulation

    During high-shear wet granulation, the API is exposed to moisture, binder alkalinity, and elevated temperature. The drying endpoint is defined by loss on drying USP 731 and final water content USP 921, but neither substitutes for chiral HPLC assay. If the granulating fluid contains sodium hydroxide or a basic buffer, the free acid may form a salt, altering solubility and possibly the physical state of the drug in the granule. Samples should be withdrawn at the start, middle, and end of drying to map enantiomeric purity against residual moisture. If dryer inlet air temperature is raised to reduce drying time, the outlet product temperature must remain below the temperature at which chiral drift or degradation is detected in preformulation forced-degradation studies. A fluid-bed dryer with adjustable air flow is preferred over a static tray dryer because it provides uniform moisture removal and reduces the risk of localized overheating. When a twin-screw granulator is used for continuous processing, the screw configuration and barrel temperature profile must be qualified with the API because residence time and shear energy input differ from batch granulation. Published data for this exact S-enantiomer in continuous twin-screw granulation is limited; early batches should include chiral assay at multiple barrel temperatures before the process parameter range is locked.

    Granule-based sachet and dispersible tablet processing require additional weight-unit uniformity because the active is distributed across multiple granules. If the API is formulated as a granule for oral suspension, the blend should be evaluated for sedimentation, dispersity, and dose uniformity after reconstitution. The free acid may require taste-masking if the granule is intended for oral dispersible use; this is a formulation constraint, not a material deficiency. A wet granulation route is often selected to reduce segregation of the active, but the granule moisture must be dried to a level that prevents hydrolysis and microbial growth while preserving the crystalline or amorphous state. Sticking to punch faces during tablet compression is evaluated through compression force and ejection force monitoring; if sticking occurs, the lubricant type and level are adjusted rather than changing the API specification. The S-enantiomer can exhibit batch-to-batch variability in crystal habit, which affects flow and compaction; the particle-size specification is not a substitute for crystal morphology control.

    Compared with the racemate and the (R)-(+)-enantiomer, the S-(-)-form is the only grade suitable for chiral drug product development where the active species is stereospecific. The racemic form cannot be substituted through a simple mass correction because the R-enantiomer becomes an uncharacterized impurity and changes the total related-substance profile. Research-grade lots of indoline-2-carboxylic acid often lack particle-size control, endotoxin testing, and residual solvent documentation; such material is not acceptable for oral commercial batch release or injectable manufacture. The Pharma Grade oral/injectable series is supported by a stability-indicating method and a retest programme based on ICH Q1A storage conditions. Handling incompatibilities include strong oxidizing agents, which can degrade the secondary amine, and prolonged storage in open containers at high relative humidity, which can increase water uptake and change flow. Compatibility with common tablet lubricants, disintegrants, and capsule shells should be confirmed because the free carboxylic acid can interact with basic excipients through salt formation or acid-base reactions. For lyophilized injection formulation, the API may be dissolved with a pH-adjusting agent; the solution should be filtered through a 0.22 µm membrane, filled into depyrogenated vials, and lyophilized under a cycle that preserves enantiomeric purity and residual moisture.

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