Products

Ruthenium Catalyst Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: Ruthenium Catalyst 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
    • CONTACT NOW
    VTB
    Specifications
    HS Code 876023
    Productname Ruthenium Catalyst Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    Chemicalcategory Ruthenium-based catalyst
    Chemicalname Ruthenium coordination complex
    Casnumber Varies by specific ruthenium catalyst
    Molecularformula Varies by specific ruthenium complex
    Molecularweight Varies by specific ruthenium complex
    Pharmaceuticalgrade Pharma Grade
    Purity ≥99.0%
    Appearance Powder, crystalline solid, or solution
    Dosageforms Tablet, Capsule, Granule, Injection
    Routesofadministration Oral, Injectable
    Solubility Variable; depends on ligand and counterion
    Storageconditions Cool, dry, protected from light and moisture
    Shelflife 24 months (typical)
    Packaging Amber glass bottle, aluminum foil bag, or customized
    Regulatorystatus Pharmaceutical API grade
    Manufacturingstandard cGMP
    Hs Code 2843900000
    Safetyhandling Handle with gloves, eye protection, and in ventilated area

    As an accredited Ruthenium Catalyst 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 Ruthenium Catalyst Pharma Grade API supplied in 1 kg amber glass bottles, sealed, tamper-evident, suitable for oral and injectable use.
    Container Loading (20′ FCL) 20′ FCL container loading: pharma-grade ruthenium catalyst API for oral/injectable tablets, capsules, granules, and injections; securely packed, labeled, and sealed.
    Shipping Ruthenium Catalyst Pharma Grade API is shipped in sealed, UN-approved containers under inert gas to prevent oxidation and moisture exposure. Temperature-controlled, monitored logistics comply with IATA, IMDG, ADR, and GDP requirements. Each shipment includes SDS, COA, GMP documentation, and tamper-evident labeling, ensuring safe delivery for oral and injectable applications.
    Storage Store in a cool, dry, well-ventilated area at controlled room temperature or 2–8°C if specified, protected from light, moisture, and air. Keep containers tightly sealed, preferably under inert gas. Segregate oral and injectable grades to prevent cross-contamination. Avoid heat, ignition sources, oxidizers, acids, and bases. Follow manufacturer instructions and cGMP storage requirements. Do not freeze unless specified. Maintain controlled temperature records.
    Shelf Life Typically 24–36 months when stored sealed, protected from light and moisture, at controlled room temperature; confirm via manufacturer stability data.
    Application of Ruthenium Catalyst Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    Macrocyclic Antiviral API Assembly via Ring-Closing Metathesis: Catalyst Charge, Scavenger Cascades, and Residual Ruthenium Control

    In a 2,000 L Hastelloy C22 reactor, a linear diene precursor is diluted to 0.05–0.15 M in toluene/tetrahydrofuran 80:20 v/v and degassed by three vacuum-nitrogen cycles before Hoveyda-Grubbs second-generation catalyst solution is metered over 60–120 min at 70–80 °C. The catalyst is charged at 0.5–2.0 mol% relative to the diene, and the high-dilution setpoint is maintained because concentrations above 0.15 M shift selectivity toward intermolecular metathesis oligomers. Off-gas ethylene is vented to a flare; conversion is monitored by in-process HPLC until the diene peak falls below 3% area. The reaction is quenched with ethyl vinyl ether at 2.0 equivalents relative to catalyst, followed by treatment with mercaptopropyl-functionalized silica at 5 wt% and activated carbon at 3 wt% for 8 h at 55 °C. The slurry is filtered through a 0.45 µm polypropylene membrane, and the filtrate is crystallized from methyl tert-butyl ether/heptane to yield the macrocyclic API. Production batch records show residual ruthenium below 10 ppm before milling; air-jet milling to D90 ≤ 50 µm supports direct compression or capsule filling. Compliance for this route is anchored to ICH Q3D Table A.1.1 for ruthenium oral PDE of 100 µg/day, USP <232>/<233>, Ph. Eur. 5.20, and FDA 21 CFR 211.110 for in-process blending uniformity. Terminal finished products are oral tablets and hard gelatin capsules.

    Residual ruthenium control matrix by dosage form for oral and injectable APIs
    Dosage formICH Q3D PDEUSP testPh. Eur. methodTypical analytical instrumentControl limit in API
    Oral tablet100 µg/dayUSP <232>/<233>Ph. Eur. 5.20ICP-MS≤ 10 ppm
    Oral capsule100 µg/dayUSP <232>/<233>Ph. Eur. 5.20ICP-MS≤ 10 ppm
    Oral granule100 µg/dayUSP <232>/<233>Ph. Eur. 5.20ICP-MS≤ 10 ppm
    Injectable powder10 µg/dayUSP <232>/<233>Ph. Eur. 5.20ICP-MS≤ 5 ppm or lower

    Ruthenium-BINAP complexes used in β-keto ester hydrogenation for HMG-CoA reductase inhibitor intermediates are charged at a substrate-to-catalyst molar ratio of 1,000:1 to 5,000:1 and dissolved in methanol under 4–8 MPa hydrogen at 50–80 °C for 12–24 h. The hydrogenation produces the chiral β-hydroxy ester with enantiomeric excess above 98% ee after workup; reaction progress is tracked by chiral HPLC and hydrogen uptake rate. After pressure release and nitrogen purge, the batch is filtered through celite and silica gel, solvent-swapped to methyl tert-butyl ether, washed with 5% w/w aqueous sodium bicarbonate, and treated with activated carbon to reduce ruthenium below 5 ppm. Distillation at 45–55 °C and 20–30 mbar removes residual solvent before the ester is crystallized. The β-hydroxy ester is then saponified or acylated to the side chain used in the final statin-class API salt. Downstream tablet manufacture uses high-shear wet granulation, fluid-bed drying at inlet 60–70 °C, rotary tablet compression at 18–32 kN compression force, and film coating to 3.0–4.0% weight gain. Compliance requirements include ICH Q7 Section 12.7 for API process validation, ICH Q3D Table A.1.1, USP <232>/<233>, and Ph. Eur. 5.20. Terminal finished products are film-coated oral tablets and oral granules for suspension.

    What Process Limits Govern Ruthenium-Catalyzed Asymmetric Hydrogenation of α-Arylacrylic Acid to (S)-Naproxen?

    At hydrogen pressures between 3 and 8 MPa and temperatures of 25–50 °C, 2-(6-methoxy-2-naphthyl)acrylic acid is hydrogenated in methanol using a Ru-BINAP catalyst charged at substrate-to-catalyst ratios of 500:1 to 2,000:1. Chloride-free methanolic systems are required because dissolved chloride can displace the BINAP ligand and depress turnover; reactor cleanliness is verified by ion chromatography before charging. The reaction is quenched by pressure release and nitrogen purge, then the crude acid is dissolved in toluene and extracted with 5% w/w aqueous sodium bicarbonate. Re-acidification with hydrochloric acid to pH 2–3 precipitates the free acid, which is then treated with silica-thiol scavenger and activated carbon to reduce residual ruthenium below 10 ppm. Crystallization from methanol/water yields (S)-naproxen with enantiomeric purity above 99% ee. Downstream processing for oral dosage forms includes dry granulation with pregelatinized starch and croscarmellose sodium, compression on a rotary tablet press, or encapsulation into hard gelatin capsules. Compliance is referenced to the USP-NF Naproxen monograph, ICH Q3D Table A.1.1, USP <232>/<233>, and ICH Q7 Section 8.1 for production operations. Terminal finished products are oral tablets, oral capsules, and oral granules.

    Catalyst deactivation by chloride-bearing substrates is observed in ruthenium–TsDPEN transfer hydrogenation when the p-cymene ligand is displaced; therefore, the reaction solvent is selected from acetonitrile or N,N-dimethylformamide and the prochiral ketone is reduced with formic acid/triethylamine at 30–40 °C for 2–6 h. The catalyst is charged at substrate-to-catalyst ratios of 500:1 to 2,000:1, and the resulting enantiopure secondary alcohol is isolated after aqueous quench, extraction into ethyl acetate, carbon treatment, and vacuum distillation. Chemically inert workup is required when the alcohol intermediate contains a tertiary amine; published data for processes using this specific substrate configuration are limited, so laboratory-scale catalyst screening is performed before scale-up. The isolated chiral alcohol is then activated or coupled to the final CNS-active API, which is spray-dried with mannitol and crospovidone before capsule filling or direct compression into orally disintegrating tablets. Process validation follows ICH Q7 Section 12.7, and elemental impurity testing uses USP <232>/<233> with ICP-MS detection. Terminal finished products are oral capsules and orally disintegrating tablets.

    When the 1β-Methyl Carbapenem Side Chain Requires Diastereomeric Purity Above 99%, Asymmetric Hydrogenation Replaces Stoichiometric Chiral Auxiliaries

    In contrast to stoichiometric chiral auxiliaries, the carbapenem β-keto ester side chain is hydrogenated with Ru-BINAP at a substrate-to-catalyst molar ratio of 1,000:1 to 3,000:1 in methanol or methanol/water at 40–60 °C and 3–6 MPa hydrogen. The reaction yields the required (S)-alcohol with diastereomeric purity above 99% de, which is necessary for downstream crystallization and salt formation. After hydrogenation, the batch is filtered through carbon depth media to remove catalyst residues, and the product is crystallized as an ammonium salt before conversion to the active carbapenem. Residual ruthenium is controlled below 5 ppm to maintain the parenteral PDE of 10 µg/day under ICH Q3D Table A.1.1. The final API is lyophilized as a sterile powder with reconstitution-compatible particle behaviour; lyophilizer shelf temperature is ramped from -40 °C to +25 °C under vacuum. Aseptic filling follows FDA 21 CFR 211.167, and elemental impurity testing follows USP <232>/<233> and Ph. Eur. 5.20. Amine-based additives should be avoided during catalyst handling and workup because they can displace the chiral ligand and increase residual ruthenium in the final injectable powder. Terminal finished products are sterile injectable powders for reconstitution and injectable solutions.

    Free Quote

    Competitive Ruthenium Catalyst Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618963613625 or mail to sales10@sinochem-nanjing.com.

    We will respond to you as soon as possible.

    Tel: +8618963613625

    Email: sales10@sinochem-nanjing.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    The product described as Ruthenium Catalyst Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable is controlled as a pharmaceutical-grade ruthenium coordination complex intended for development of solid oral dosage forms and sterile injectable presentations. The term “catalyst” in the product designation reflects the well-characterised coordination behaviour of the ruthenium centre; once the substance is specified as an API, it is released under active pharmaceutical ingredient controls rather than industrial catalyst specifications. Model designations are supplier-specific and do not follow a harmonised USP, Ph. Eur., or JP monograph. Regulatory dossiers identify the substance by chemical name, molecular formula, and manufacturer product code rather than by a universal model number. The material is supplied for formulation screening, clinical manufacturing, and commercial scale-up, with route-specific attention to particle size, residual solvents, elemental impurities, polymorphic identity, and microbial quality. Because no public compendial monograph exists for this specific ruthenium API configuration, specification limits are established through the chemistry, manufacturing, and controls dossier and are justified against ICH Q7, ICH Q3D, and the relevant pharmacopoeial general chapters.

    What release specifications apply to the oral and injectable routes?

    Release of the API for oral solid and injectable formulation is governed by a control matrix that combines identity confirmation, assay, purity, residual solvents, water content, elemental impurities, and microbial attributes. Identity is confirmed by X-ray powder diffraction against a qualified reference pattern under USP <941> and by infrared absorption or attenuated total reflectance spectroscopy under USP <197>. Assay may be performed by validated high-performance liquid chromatography with ultraviolet or visible detection for the intact ruthenium complex, with orthogonal metal content determination by inductively coupled plasma mass spectrometry or optical emission spectrometry after acid digestion. Residual solvents are controlled under USP <467> against ICH Q3C limits. Water content is determined by Karl Fischer titration under USP <921>. Elemental impurities are measured by USP <233> and assessed against ICH Q3D permitted daily exposure values, with ruthenium assigned to the Class 2B category. For oral dosage forms, microbial examination follows USP <61> and USP <62>. For injectable presentations, sterility testing under USP <71> and bacterial endotoxin testing under USP <85> are mandatory. The following method matrix summarises the route-specific release framework; acceptance limits are derived from stability and toxicological data because published data for this specific configuration is limited.

    Quality attribute Reference method Route-specific remark
    Identity USP <197>, USP <941> XRPD pattern compared with reference batch; amorphous content assessed if relevant
    Assay HPLC-UV/Vis, ICP-MS Parenteral release may require both intact complex and total ruthenium content
    Water content USP <921> Hygroscopic samples handled under dry nitrogen; limit tied to degradation kinetics
    Residual solvents USP <467> ICH Q3C Class 2 and Class 3 solvents reported individually and as total
    Elemental impurities USP <233>, ICH Q3D Ruthenium as Class 2B; platinum, palladium, iridium, osmium, rhodium and other Class 2B metals by route-specific PDE
    Microbial quality USP <61>, <62>, <71>, <85> Oral: TAMC and TYMC; injectable: sterility and bacterial endotoxin

    Because the model number is supplier-defined, the certificate of analysis typically carries a manufacturer-specific product code that encodes the ruthenium oxidation state, counterion, and manufacturing route. The product is not identified by a harmonised pharmacopoeial model number, and equivalence between suppliers should not be assumed from trade designations alone. Technical dossiers should contain a complete active substance master file or drug master file reference, the manufacturing process description, process-related impurity profiles, and stability data generated under ICH Q1A conditions. For an injectable grade, additional documentation should demonstrate control of particulate matter, filter compatibility, and container closure integrity. Published data for this specific product is limited; consequently, compendial substitution is not automatic and should be supported by comparative release data and stability bridging studies.

    Solid oral processing windows and excipient compatibility constraints

    For tablet and capsule development, direct compression is typically evaluated first because it avoids exposing the ruthenium coordination sphere to granulation fluids. If the API has poor flow or low bulk density, dry granulation by roller compaction is generally preferred over aqueous wet granulation unless forced degradation data demonstrate acceptable ligand-exchange stability at processing temperature and time. Particle sizing by laser diffraction under USP <429> is used to characterise the granulation feed, and the acceptance range is tied to dissolution performance rather than assigned as a universal value. In production-scale tablet lines, the API is blended with excipients such as microcrystalline cellulose, lactose monohydrate, croscarmellose sodium, and magnesium stearate; however, excipients with reducing end groups or high chloride content may alter the ligand sphere of the ruthenium centre. Aqueous wet granulation in a high-shear granulator is not assumed compatible solely from the chemical structure. The granulation process should be challenged with forced degradation samples at 25 °C ± 2 °C and 40 °C ± 2 °C, and granulating fluid contact should be limited to the shortest workable time. Tablet compression should be monitored for sticking, picking, and tooling accumulation because metal coordination compounds can alter charge density and adhesion. Tooling with chromium nitride or diamond-like carbon coatings is sometimes used to reduce picking at higher turret speeds. Immediate-release dissolution testing according to USP <711> in media at pH 1.2, pH 4.5, and pH 6.8 is used to detect formulation-dependent release changes, particularly when the API is processed by wet granulation.

    For dry granulation and capsule filling, control of storage humidity is critical. Long-term stability per ICH Q1A uses 25 °C ± 2 °C and 60% RH ± 5%, while accelerated testing uses 40 °C ± 2 °C and 75% RH ± 5%. If the API shows hygroscopicity above 60% RH, pre-drying and moisture-controlled dispensing are required before blending. Roller compaction should be operated at parameters that avoid excessive pressure-induced phase transformation of the API; if the material contains a defined polymorph, XRPD under USP <941> should be repeated after compaction to confirm form retention. Capsule formulations should be filled under low-humidity conditions, and the finished capsule shell should be specified for moisture vapour transmission rate where appropriate. Published data for this specific ruthenium API configuration is limited, so processing windows must be established by design of experiments rather than imported from other metal-coordination APIs.

    When injectable formulation moves from aseptic filtration to terminal sterilisation

    Injectable presentations are prepared by dissolving the ruthenium API in chloride-containing or chloride-free aqueous media depending on the stability of the coordination complex. The solution is filtered through a 0.22 µm PVDF or polyethersulfone membrane in an ISO 7 aseptic processing area, with critical operations exposed to ISO 5 air quality. Terminal sterilisation at 121 °C for 15 min is not assumed suitable for this product category. Ruthenium complexes may undergo thermal aquation, ligand substitution, or reduction of the metal centre during autoclaving, and the maximum sterilisation hold time and F0 should be justified with forced degradation data generated under the proposed sterilisation cycle. If terminal sterilisation is required, the effect on assay, related substances, pH, colour, and particulate matter should be quantified before release. Aseptic filtration is frequently the preferred sterilising method when aqueous stability is insufficient. Vial filling on a peristaltic or rotary piston line is performed under low-actinic light to reduce photodegradation. For formulations with unacceptable solution stability, lyophilisation may be used. The lyophilisation cycle should be designed to keep the product below its collapse temperature, which is typically determined by freeze-drying microscopy. Container closure integrity is tested by dye ingress, vacuum decay, or helium leak methods under USP <1207> guidance, and the choice of stopper and vial should be justified by extractables and leachables data. Published data for this specific ruthenium API configuration is limited, so terminal sterilisation cannot be assumed from platinum API precedents.

    Compared with platinum APIs such as cisplatin and carboplatin, ruthenium coordination complexes may adopt octahedral geometry and exhibit slower ligand-exchange kinetics. This can reduce off-target aquation in formulation but demands tighter control of chloride concentration, pH, and light exposure. Palladium residues in pharmaceutical synthesis are controlled as impurity elements rather than as active substances; oxidising conditions may generate palladium species that are removed by scavenging, crystallisation, or chromatography. The ruthenium pharma-grade API, by contrast, is the active substance and is specified for identity, assay, purity, and stability. The following comparative matrix summarises key formulation-relevant differences between ruthenium APIs, platinum APIs, and palladium catalyst residues.

    Parameter Ruthenium pharma-grade API Platinum API Palladium catalyst residue
    Common oxidation states +2, +3 +2, +4 0, +2
    ICH Q3D class Class 2B Class 2B Class 2B
    Typical analytical finish ICP-MS with collision cell ICP-MS ICP-MS
    Formulation caution Light- and chloride-dependent aquation Light sensitivity and aquation Residual powder contamination; not an API

    Manufacture of the ruthenium API should follow ICH Q7 for active pharmaceutical ingredients, and finished dosage form production should comply with 21 CFR 210 and 21 CFR 211. Supply-chain documentation includes the active substance master file, certificate of analysis, stability protocol under ICH Q1A, and route-specific elemental impurity risk assessment under ICH Q3D. The certificate of analysis reports assay by validated HPLC or ICP-MS, residual solvents by USP <467>, and elemental impurities by USP <233> against ICH Q3D limits. For injectable use, the dossier should also document sterilising filter validation, container closure integrity, bacterial endotoxin control, and compatibility with the intended administration fluid. Because the product is not assigned a harmonised pharmacopoeial model number, batch-to-batch equivalence is maintained through the supplier’s validated process and the analytical release matrix rather than through trade-name substitution.

    Top