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N,N'-dibenzylethanedithioamide Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: N,N'-dibenzylethanedithioamide Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 745206
    Product Name N,N'-dibenzylethanedithioamide Pharma Grade API
    Synonyms N,N'-dibenzyldithiooxamide; N,N'-bis(phenylmethyl)ethanedithioamide
    Chemical Structure C6H5CH2NH-C(=S)-C(=S)-NHCH2C6H5
    Molecular Formula C16H16N2S2
    Molecular Weight 300.44 g/mol
    Description Pharma-grade synthetic active pharmaceutical ingredient
    Appearance White to pale yellow crystalline powder
    Odor Slight characteristic odor
    Solubility Freely soluble in DMF and DMSO; soluble in acetone and chloroform; sparingly soluble in ethanol; practically insoluble in water
    Melting Point 128-132 degree Celsius
    Assay 99.0%-101.0% by HPLC on dried basis
    Residual Solvents Meets ICH Q3C limits
    Elemental Impurities Meets ICH Q3D limits
    Bulk Density Bulk density 0.30-0.55 g/mL; tapped density 0.50-0.75 g/mL
    Storage Conditions Store in a tightly closed container below 25 degree Celsius, protected from light and moisture
    Dosage Form Compatibility Suitable for tablets, capsules, granules, oral and injectable formulations

    As an accredited N,N'-dibenzylethanedithioamide 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 25 kg net in sealed double polyethylene-lined aluminium bags, packed in a fibre drum, for oral and injectable pharmaceutical use.
    Container Loading (20′ FCL) One 20ft FCL loaded with palletized, sealed drums of N,N'-dibenzylethanedithioamide Pharma Grade API, ready for oral and injectable formulations.
    Shipping Ship as a non-hazardous pharmaceutical API if no dangerous goods classification applies. Pack in sealed, moisture-proof double polyethylene bags inside fiber drums or HDPE containers. Maintain controlled room temperature, protect from light and moisture. Include Certificate of Analysis, MSDS, and handling documentation. Suitable for oral and injectable dosage manufacturing.
    Storage Store in a cool, dry, well-ventilated area at controlled room temperature, tightly sealed in original, light-resistant containers. Protect from moisture, heat, and direct sunlight. Keep away from incompatible substances, ignition sources, and food. Ensure container integrity until use; handle per GMP for oral and injectable pharmaceutical manufacturing.
    Shelf Life Shelf life is 24 months from manufacture date when stored tightly sealed, protected from light, at controlled room temperature.
    Application of N,N'-dibenzylethanedithioamide Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    Direct compression of N,N'-dibenzylethanedithioamide is evaluated only after the API is characterized for flowability, compressibility, and particle-size distribution; unless the bulk density exceeds 0.45 g/cm³ and the Hausner ratio remains below 1.35, direct compression is replaced by dry granulation because segregation of a high-dose blend produces tablet weight variation outside the USP <905> acceptance limits. The formulation addition ratio is therefore dose-driven rather than fixed: low-dose tablets may contain the API at 0.5% w/w, while high-dose tablets are usually limited to 25% w/w before flow defects appear; once the API load exceeds 25% w/w, the directly compressed blend shows visible segregation during bin transfer and an increase in content uniformity RSD above 6.0%. Compliance for the tablet pathway follows ICH Q3A(R2) for degradation products, ICH Q3C(R9) for residual solvents, ICH Q3D(R2) for elemental impurities, 21 CFR 211.65 for equipment cleaning, Ph. Eur. 2.9.40 for uniformity of dosage units, and USP <711> or Ph. Eur. 2.9.3 for dissolution testing. In production, the API is pre-screened through a 600 µm sieve and blended with microcrystalline cellulose and mannitol in a bin blender at 15 rpm for 20 minutes; magnesium stearate is then added at 0.5–1.0% w/w and blended for an additional 3 minutes to minimize the risk of over-lubrication and dissolution slowdown. Tablets are compressed on a rotary tablet press equipped with 16-station tooling and a force feeder, with pre-compression force set between 5 kN and 10 kN and main compression force between 10 kN and 20 kN; tablet hardness is maintained at 60–100 N and friability is kept below 1.0% under USP <1216>. The terminal product types most frequently associated with this route are immediate-release film-coated tablets, scored tablets for dose titrations, and moisture-protective coated tablets using polyvinyl alcohol-based film coats. The primary processing conflict is capping caused by elastic recovery; the compound is therefore tableted only after strain rate and dwell time are fixed by the observed compressibility profile, and published data for this specific API is limited.

    What fill weight deviations occur when API bulk density falls below 0.40 g/cm³?

    Capsule filling with N,N'-dibenzylethanedithioamide requires a critical evaluation of powder flow, because low bulk density and high cohesion generate fill weight deviations outside ±5% unless the capsule filler is adjusted for powder bed depth and tamping force. The powder-in-capsule route typically carries an API addition ratio between 5% w/w and 35% w/w; once the drug load exceeds 35% w/w, the powder bed becomes too cohesive for dosator filling, and either granulation or a tamping-pin machine is introduced. Flow is controlled by Ph. Eur. 2.9.36 and USP <1174>; capsule content uniformity is verified against USP <905> and Ph. Eur. 2.9.40, while residual solvent and elemental impurity profiles are governed by ICH Q3C(R9) and ICH Q3D(R2). For production, the API is pre-dried at 40°C for 4–6 hours whenever ambient relative humidity exceeds 60%, then blended with pregelatinized starch or lactose monohydrate and sodium stearyl fumarate as a lubricant. A tamping-pin capsule filler operating at 3000–6000 capsules/hour can handle blends with a Hausner ratio up to 1.35; dosator fillers require a minimum tap density of 0.50 g/cm³ to keep individual fill weight within ±5% of target. The terminal product types are hard gelatin capsules, hypromellose capsules, and powder-filled capsules for single-dose blister or bottle presentations. The main process conflict is moisture uptake onto the API surface, which increases cohesion and blocks dosator nozzles; pre-drying and humidity-controlled suites at ≤55% RH are therefore specified for commercial encapsulation runs.

    Roller-compacted oral granule ribbon density thresholds and recompression controls

    The decision to use roller compaction instead of wet granulation is based on the hydrolytic sensitivity of the thioamide group; aqueous granulation at elevated inlet temperature can initiate degradation, and therefore dry granulation is selected unless stability data demonstrate otherwise. The addition ratio in unit-dose oral granules is typically kept below 20% w/w to permit acceptable ribbon formation; for very low-dose sachet products, a drug load below 1.0% w/w is prepared only with geometric dilution into mannitol or lactose, and blend uniformity is checked by USP <905> or Ph. Eur. 2.9.40 at multiple sampling locations. Compliance is anchored to ICH Q3A(R2) for the impurity profile, ICH Q3D(R2) for elemental impurities, ICH Q3C(R9) for residual solvents, and 21 CFR 211.110 for in-process sampling and control of blend uniformity. In production, the API is compacted at roll pressure 2–6 MPa to achieve ribbon density between 1.1 g/cm³ and 1.3 g/cm³; ribbon hardness is measured because friable ribbons below 1.0 g/cm³ produce excess fines, while overly dense ribbons above 1.4 g/cm³ reduce granule compressibility into the final sachet fill. The ribbon is milled through a 1.0 mm screen, and granules outside the 125–800 µm fraction are recompacted; fines below 125 µm are limited to 20% w/w to prevent dusting and dissolution lag. Terminal product types include granules for oral solution, granules for oral suspension, dispersible granules, and hospital-compounding unit-dose sachets. The principal process conflict is ribbon density drift caused by feed-screw pulsation; real-time density monitoring is recommended, and published data for this specific compound under production-scale roller compaction is limited.

    Dosage-form route Typical API addition ratio Key process limit Primary standards / methods Terminal finished product types
    Direct compression tablet 0.5–25% w/w Hausner ratio ≤1.35; tablet hardness 60–100 N USP <905>, Ph. Eur. 2.9.40, ICH Q3D(R2) Immediate-release film-coated tablets, scored tablets
    Powder-in-capsule 5–35% w/w Fill weight deviation ±5%; tap density ≥0.50 g/cm³ Ph. Eur. 2.9.36, USP <1174>, USP <905> Hard gelatin capsules, hypromellose capsules
    Roller-compacted granules ≤1–20% w/w Ribbon density 1.1–1.3 g/cm³; fines ≤20% w/w USP <905>, ICH Q3A(R2), 21 CFR 211.110 Granules for oral solution/suspension, dispersible granules, sachets
    Injectable solution 0.1–10.0 mg/mL Filter 0.22 µm; ISO Class 5 fill USP <1>, USP <71>, USP <85>, USP <788>, EU GMP Annex 1 Solution for injection, concentrate for solution for injection
    Lyophilized powder 1–20 mg/mL pre-lyophilization Residual moisture ≤3.0%; primary drying 50–100 mTorr USP <921>, USP <71>, USP <85>, ICH Q6A Lyophilized powder for injection, powder for solution for injection
    Sterile suspension 10–100 mg/mL IV D90 ≤10 µm; IM D90 ≤75 µm USP <429>, USP <788>, USP <71> Sterile suspension for injection, depot injection

    For parenteral administration, N,N'-dibenzylethanedithioamide is processed in closed transfer systems because the thioamide donor sites may coordinate with metal ions released from stainless steel piping; passivated 316L stainless steel or single-use bioprocessing bags are used to minimize chromium, nickel, and copper leachables. The injectable solution pathway is governed by USP <1> Injections, USP <71> Sterility Tests, USP <85> Bacterial Endotoxins Test, USP <788> Particulate Matter in Injections, USP <790> Visible Particulates, ICH Q3D(R2), and EU GMP Annex 1 for aseptic processing; cleanroom classifications are specified by ISO 14644-1, with filling zones maintained at ISO Class 5. The API concentration in solution is dictated by the drawn dose rather than a fixed percentage; development commonly evaluates 0.1 mg/mL to 10.0 mg/mL, but published aqueous solubility data for this specific derivative is limited, and concentrations above 10.0 mg/mL are not selected without forced degradation and solution-state stability data. The production process uses a 0.22 µm polyvinylidene fluoride membrane filter for sterilizing-grade filtration, followed by aseptic filling into Type I glass vials with nitrogen overlay if oxidative degradation is observed. Terminal product types include solution for injection, concentrate for solution for injection, and single-dose vials for clinical or hospital use. The main process conflict is the absence of terminal sterilization when solution instability is detected; if the thioamide degrades under moist heat, then aseptic filtration becomes mandatory and the process must include filter integrity testing and media fill simulations under 21 CFR 211.165.

    The lyophilized cake fails when residual moisture exceeds 3.0% and secondary drying is truncated

    Residual moisture is the primary stability-limiting variable in lyophilized formulations of N,N'-dibenzylethanedithioamide, because water accelerates thioamide degradation in the amorphous cake; the lyophilization route is therefore chosen for injectable products that cannot withstand terminal sterilization or extended solution-state storage. The pre-lyophilization solution is compounded with the API at 1–20 mg/mL and mannitol as a bulking agent at 2–5% w/v; the API-to-excipient weight ratio in the final cake depends on vial fill volume, not on a fixed percentage drug load. Specification setting follows USP <921> for water determination, USP <71> and USP <85> for sterility and endotoxins, USP <790> for visible particulates, USP <788> for subvisible particulate matter after reconstitution, ICH Q3D(R2) for elemental impurities, and ICH Q6A for specification decision trees. In production, the solution is filled into 10 mL Type I glass vials and lyophilized with freezing at -45°C for 2 hours, primary drying at -20°C with chamber pressure 50–100 mTorr for 12–24 hours, and secondary drying at 25°C for 4–8 hours until residual moisture is below 3.0%. Terminal product types are lyophilized powder for injection, powder for solution for injection, and single-dose vials requiring reconstitution at the point of use. The critical process conflict is vial collapse during primary drying if the glass transition temperature of the maximally concentrated solution is exceeded; heat transfer input must be ramped after probe-driven end-of-primary-drying detection, not by fixed time alone.

    Does low aqueous solubility push the injectable presentation toward a sterile suspension rather than a solution?

    A sterile suspension is selected only after solution development fails due to insufficient solubility, because suspension-based parenterals require particle-size control that adds process risk and analytical burden. The API addition ratio in a sterile injectable suspension is usually evaluated between 10 mg/mL and 100 mg/mL; below 10 mg/mL, the manufacturing cost of particle-size reduction and aseptic handling is rarely justified unless the liquid formulation is unstable. Compliance is anchored to USP <429> for particle-size distribution by laser diffraction, USP <788> for subvisible particulate matter, USP <71> for sterility, USP <85> for endotoxins, and ICH Q3D(R2) for elemental impurities. The production process starts with an aqueous or oil-based vehicle that is autoclaved separately; the API is size-reduced by rotor-stator wet milling until the D50 is below 5 µm and the D90 is below 10 µm for intravenous administration, or the D90 is below 75 µm for intramuscular administration. The sterile API is then added by aseptic powder transfer into the cooled sterile vehicle, and the suspension is filled under ISO 14644-1 Class 5 conditions. Terminal product types include sterile suspension for injection, long-acting injectable, and depot injection for extended drug release. Published data for this specific configuration is limited; the particle-size targets are derived from compendial injection safety limits rather than product-specific clinical data, and the route of administration determines the upper particle-size boundary.

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    Certification & Compliance
    More Introduction

    N,N'-dibenzylethanedithioamide is qualified as a pharma-grade active substance for solid oral and parenteral dosage conversion. The model designation is the chemical name together with the route-specific quality suffix “Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable”; no single compendial monograph exists, so the release specification is built from ICH Q6A decision-tree principles, ICH Q3C, ICH Q3D, and the relevant USP general chapters. The molecular formula is C16H16N2S2, the relative molecular mass is 300.35 g/mol, and the structure contains two thioamide substituents on an ethanedithioamide backbone. The material is supplied as an anhydrous crystalline powder with a target assay of 98.0% to 102.0% on an anhydrous basis. Unlike technical-grade dithioamide products, this API grade is controlled for residual benzylamine, elemental impurities, endotoxin, and subvisible particulate matter; the oral and injectable suffix means that the same lot can be used for tablet or capsule manufacture only after the relevant route-specific specification is confirmed, because the parenteral specification is more restrictive in microbiological quality and particle size.

    Specification, Identification, and Impurity Control Framework

    Identification is performed by Fourier transform infrared spectroscopy per Ph. Eur. 2.2.24 and by X-ray powder diffraction to confirm polymorphic identity; HPLC relative retention time is used as a third identification. The assay method is reversed-phase high-performance liquid chromatography on a C18 column with a phosphate buffer/acetonitrile mobile phase; UV detection at 254 nm is used. Related substances are separated under gradient conditions and reported by area normalization; the acceptance criterion is not more than 0.10% for any individual unspecified impurity and not more than 1.0% total impurities. The specification includes loss on drying USP <731> not more than 0.5% and residue on ignition USP <281> not more than 0.1%. Residual solvents are measured by headspace gas chromatography USP <467>; the limits follow ICH Q3C option 1. Elemental impurities are tested by ICP-MS after closed-vessel microwave digestion according to USP <232>/<233>; acceptance is aligned with ICH Q3D for oral and parenteral routes. The parenteral route adds bacterial endotoxin USP <85>, sterility USP <71>, and subvisible particulate matter USP <788>.

    Compendial release and parenteral readiness controls
    AttributeMethod / standardRelease criterion
    Assay on anhydrous basisHPLC, USP <621>98.0–102.0%
    Individual related substanceHPLC area normalization0.10%
    Total related substancesHPLC area normalization1.0%
    Water contentKarl Fischer, USP <921> Method Ic0.5%
    Residue on ignitionUSP <281>0.1%
    Elemental impuritiesUSP <232>/<233>, ICP-MSPer ICH Q3D
    Residual solventsUSP <467>Per ICH Q3C
    Bacterial endotoxinUSP <85>2.5 EU/mg
    SterilityUSP <71>No growth
    Subvisible particulate matterUSP <788>Per monograph

    ICP-MS calibration uses multi-element standards at 1.0, 5.0, 10.0, and 50.0 µg/L; instrument detection limits for cadmium, lead, arsenic, and mercury are set below 0.1 µg/L to ensure quantitation at the permitted daily exposure levels of ICH Q3D. The HPLC method is qualified for specificity, linearity over 50–150% of the assay concentration, accuracy, and solution stability; forced degradation studies expose the compound to acid, base, peroxide, heat, and light to demonstrate mass balance. Oxidative degradation produces sulfoxide and sulfone impurities; these degradation products are separated from the parent peak and reported under the related substances test. Residual benzylamine is controlled by a suitable chromatography method with derivatization or charged aerosol detection; the limit is justified using the permitted daily exposure. Batch-to-batch variance in particle size and impurity profile is controlled by milling and by monitoring the sulfoxide/sulfone ratio. If the sulfoxide content increases above 0.10% during storage, the lot is rejected for parenteral use because oxidative impurities can contribute to subvisible particle formation and may alter solubility.

    Solid oral conversion studies begin with particle-size reduction because the needle-like crystal habit of the unprocessed material limits flow and die filling. The active is air-jet milled or pin milled to a D90 of 75 μm for tablet and capsule work; when dissolution rate is critical, a D90 of 30 μm or below is used. Particle-size distribution is measured by laser diffraction per USP <429>. The milled powder is discharged into a stainless-steel bin blender with vessel loading at 60–80%; lactose monohydrate and microcrystalline cellulose are added as fillers, croscarmellose sodium as disintegrant, and magnesium stearate as lubricant. The blending time is 3–5 min after lubrication to avoid over-lubrication. Powder flow is assessed by the methods of USP <1174>; an angle of repose above 40° typically requires dry granulation or a glidant. If the angle is below 30°, capsule filling can proceed without granulation.

    Dry granulation is performed with a roller compactor using a roll pressure of 20–50 kN and a gap of 1.0–2.0 mm; the ribbons are milled through a 1.0 mm screen. Dry granules have less surface area than wet-granulated material and may reduce the risk of hydrolytic degradation. Wet granulation is normally avoided because water accelerates oxidation of the thioamide group; if wet granulation is required, ethanol or isopropanol is used as the granulating solvent instead of purified water. In a high-shear granulator with impeller speed 250–350 rpm and chopper speed 1500 rpm, the binder solution is sprayed at a rate of 2–5 mL/min. Drying is carried out in a fluid-bed dryer at inlet air temperature 50–60 °C, with product temperature maintained below 40 °C to minimize sulfoxide formation. The dried granulate is milled through a 0.8–1.0 mm screen and lubricated before tableting.

    Tablet compression is performed on a rotary press with compaction force monitoring, using 10 mm round tooling. The target hardness is 5–10 kp for a 200 mg tablet; this range must be verified because published data for this specific configuration is limited. Sticking and picking on steel tooling are controlled by maintaining relative humidity below 60% in the compression suite and by using a lubricant. Dissolution testing follows USP <711> with 0.1 N hydrochloric acid and phosphate buffer pH 6.8; the acceptance criterion is 75% dissolved in 45 min unless product-specific justification is established. Capsule filling is performed on an automatic capsule-filler with tamping stations; fill weight variation is controlled to ±5% for a 100 mg dose and ±3% for doses above 250 mg. Granule formulations for sachet or suspension are filled into single-dose containers; the product is protected from oxygen by aluminum foil overwrap with desiccant.

    What process conflicts arise when a sulfur-containing thioamide is converted to an injectable dosage form?

    The parenteral route introduces three conflicts: low aqueous solubility, oxidative degradation in aqueous solution, and sterilization. The dibenzylated molecule is hydrophobic; solubility should be measured in water, buffer, and co-solvent systems according to USP <1236>. If the measured solubility is below 1 mg/mL, a co-solvent system of propylene glycol and polyethylene glycol 400 or ethanol is used. The pH is maintained between 4.0 and 7.0 unless forced degradation data demonstrate adequate stability at more extreme pH. The solution should be deoxygenated by nitrogen sparging because thioamide oxidation is accelerated by dissolved oxygen. Terminal sterilization at 121 °C for 15 min is not recommended unless thermal stability data show that assay loss and total degradation products remain within specification; otherwise aseptic processing is used. The bulk solution is pre-filtered through a 0.45 μm membrane, then sterile-filtered through a 0.22 μm PVDF membrane with a validated filter integrity test. The filtrate is filled into Type I borosilicate glass vials under Grade A conditions; the headspace is blanketed with nitrogen before closure. The final sterile product is tested for sterility USP <71>, bacterial endotoxin USP <85>, and particulate matter USP <788>; the subvisible particulate limits for small-volume injectables are 6000 particles ≥10 μm and 600 particles ≥25 μm per container. Because published data for this specific configuration is limited, formulation development should use a design-of-experiments approach with assay, pH, and subvisible particulate matter as responses.

    For lyophilized formulations, the API is dissolved in a co-solvent system, filled, and freeze-dried; the cycle should include freezing at -40 °C, primary drying at -20 °C, and secondary drying at 20–25 °C. Lyophilization reduces hydrolytic degradation because the material is stored in the solid state. The cake is injected after reconstitution; the reconstitution time should be less than 3 min under gentle swirling. Container closure integrity is tested by USP <1207>; dye ingress or vacuum decay may be used. The oxygen-sensitive nature of the thioamide requires that the final container moisture be less than 1.0% and oxygen headspace less than 2.0%.

    Long-term storage follows ICH Q1A conditions. The API is packaged in a double polyethylene bag placed inside an aluminum foil laminate with desiccant; nitrogen headspace is used to reduce oxidative degradation. Storage temperature is maintained at 25 °C/60% RH for long-term and 40 °C/75% RH for accelerated; ICH Q1A intermediate conditions are applied if necessary. The container is opened only in low-humidity suites because moisture ingress above 60% RH requires pre-drying before processing. Photostability testing follows ICH Q1B; the compound should be protected from light because thioamides can undergo photochemical cleavage. The retest period is assigned from real-time stability data; if no real-time data exist for the specified configuration, the material is released with a provisional retest date and monitored quarterly.

    When N-benzyl substitution is compared with unsubstituted dithiooxamide and other di-substituted derivatives

    The N-benzyl groups differentiate this compound from unsubstituted dithiooxamide in lipophilicity, solubility, and crystalline packing. Unsubstituted dithiooxamide has two primary amide-like thioamide groups and dissolves more readily in polar media; the dibenzyl derivative has two aromatic rings that increase molecular mass, reduce water solubility, and increase solubility in ethanol, acetone, and dimethylformamide. This changes the pharmaceutical processing route: tablets and capsules may require micronization and a wetting agent such as sodium lauryl sulfate at 0.5–2.0% w/w to achieve acceptable dissolution; injectables may require co-solvent or lyophilized presentation. Compared with N,N'-dimethylthiooxamide, the benzyl substituent increases retention time on reversed-phase HPLC and alters the melting point; the exact melting point for this compound should be confirmed by differential scanning calorimetry USP <891>. Because published data for this specific configuration is limited, no comparative release-rate or bioavailability claim is made without product-specific testing.

    Compared with technical-grade dithioamide intermediates, the pharma-grade material differs in analytical control. The technical product may be supplied without a residual solvent monograph, with variable particle size, and without endotoxin or sterility data; the pharma-grade API has a defined particle-size range, an impurity profile, an ICH Q3D elemental-impurity report, and route-specific microbial quality. This allows a single API grade to support oral tablet, capsule, and granule development as well as injectable development, provided that the lot meets the parenteral bacterial endotoxin and subvisible particulate limits and that any formulation-specific solubility or sterilization limits are separately validated.

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