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Ecopipam O-β-D-glucuronide Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: Ecopipam O-β-D-glucuronide Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
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    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 961693
    Product Name Ecopipam O-β-D-glucuronide Pharma Grade API
    Api Name Ecopipam O-β-D-glucuronide
    Synonyms Ecopipam glucuronide; SCH 39166 glucuronide
    Chemical Class Dopamine D1/D5 receptor antagonist glucuronide metabolite
    Therapeutic Category Central nervous system agent
    Molecular Formula C25H28ClNO7
    Molecular Weight 489.95 g/mol
    Appearance White to off-white powder
    Purity ≥98% by HPLC
    Grade Pharma Grade
    Dosage Forms Tablet, Capsule, Granule, Injection
    Routes Of Administration Oral, Injectable
    Solubility Soluble in water; slightly soluble in ethanol
    Storage Conditions Store at 2-8°C, protected from light and moisture
    Shelf Life 24 months
    Packaging Double polyethylene bag in fiber drum or amber glass vial
    Quality Standard In-house specification; ICH guidelines
    Manufacturing Method Chemical synthesis or biotransformation
    Regulatory Status Investigational; for pharmaceutical development use
    Assay 98.0-102.0%
    Loss On Drying ≤1.0%
    Residue On Ignition ≤0.1%
    Heavy Metals ≤20 ppm
    Ph 5.0-7.5 (1% solution)
    Moisture Content ≤0.5%

    As an accredited Ecopipam O-β-D-glucuronide 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
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    Application of Ecopipam O-β-D-glucuronide Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    In direct compression workflows using rotary tablet presses fitted with 10 or 12 station B-tooling, Ecopipam O-β-D-glucuronide Pharma Grade API is characterized through USP <1174> powder flow and USP <616> bulk and tapped density before batch release. Published flow and compressibility data for this specific glucuronide conjugate are limited; therefore, preformulation cannot rely on aglycone-derived parameters. The glucuronide substituent raises polar surface area and can increase water uptake under uncontrolled ambient storage. Direct compression blends typically contain microcrystalline cellulose, spray-dried lactose monohydrate, croscarmellose sodium, colloidal silicon dioxide, and sodium stearyl fumarate. Lubricant screening is required because the conjugate carboxylate group can interact with metal ions from tableting tooling during prolonged press runs, and overlubrication risk is elevated when the blend is mixed beyond the optimized time. Blend water activity is monitored with a dew point chilled-mirror water activity meter, because residual moisture redistribution changes die-fill consistency and tablet hardness variability during extended runs.

    Compaction behavior is assessed on a compaction simulator or instrumented single-punch press. Ejection force, radial die-wall pressure, and hardness variability are logged after each 30-minute continuous run. If blend water activity exceeds 0.35, caking at the feed frame has been observed in production platforms handling high-polar-surface-area APIs, although published data for this exact conjugate are limited. Tablet disintegration is evaluated per USP <701>; a limit of 15 minutes for uncoated tablets is common for immediate-release oral dosage forms. Tablet weight variation and content uniformity are measured by USP <905>. Elemental impurities are controlled per ICH Q3D Option 1 or 2, and residual solvents are monitored under ICH Q3C Option 1. No release specification should be fixed until supplier-specific accelerated stability data are generated.

    Which High-Shear Wet Granulation Failure Modes Are Specific to the O-β-D-Glucuronide Conjugate?

    High-shear wet granulation in a 600 L top-drive mixer with impeller tip speed 4–6 m/s and chopper speed 1,800–2,400 rpm requires endpoint control based on torque rise and impeller power draw rather than fixed wet massing time. For Ecopipam O-β-D-glucuronide, binder addition rate affects granule size distribution more than total water volume because the conjugate has a water-soluble polar surface and localized overwetting at spray nozzle impact points can produce hard agglomerates. Binder solution based on povidone at 5%–10% w/w may be used, but the selected level must be confirmed by residual water and drug-related impurity results after drying. The glucuronide ether linkage is generally stable under neutral and mildly acidic conditions, but no published pH-rate profile for this compound exists; forced degradation under ICH Q1A(R2) should define pH 1.2 exposure limits before selecting binder solvent. Wet mass is dried in a fluid-bed dryer with inlet air temperature 50–60°C and dew point below 4°C.

    Drying endpoint must be measured by loss on drying under USP <731> or Karl Fischer titration USP <921> Method Ia. Granule moisture target of 1.5%–3.0% w/w is typical for glucuronide-containing granules intended for tablet compression, but specific data for this API remain limited. Milling through a 1.0 mm screen with a conical mill at 1,500 rpm is used to normalize oversized granules; if the mill screen is too fine, attrition raises fines below 75 µm and reduces downstream die-fill uniformity. Batch-to-batch median granule size variation above 8% should trigger adjustment of binder atomization rate or wet massing endpoint. Torque endpoint qualification must use impeller power in kilowatts, not impeller speed alone, because granule densification changes bulk density and can challenge disintegration. Granule flow is confirmed by USP <1174>; the Hausner ratio and Carr index are recorded for each batch. If residual moisture exceeds 3.0% w/w, the subsequent compression step may exhibit sticking to punches.

    Automatic capsule filling machines with dosator or tamping-pin technology handle Ecopipam O-β-D-glucuronide blends only after flow-aid optimization and measured shear cell flow function. Because the API molecule contains multiple polar oxygen atoms, cohesive forces can produce ratholing in the feed hopper. On a four-station dosator machine operating at 60,000 capsules/hour, the blend must be free-flowing and de-dusted. A flow function coefficient above 4.0 by ring shear testing is generally workable for capsule filling, but the blend may still require 0.5%–1.0% w/w colloidal silicon dioxide and 0.5%–1.5% w/w sodium stearyl fumarate. Overlubrication must not exceed 1.0% w/w magnesium stearate, because hydrophobic film formation on the polar API can delay dissolution under USP <711>.

    Fill weight variation is monitored by USP <905>. For capsules with target fill weight below 100 mg, the acceptance value should be tightened beyond the compendial 15% limit to prevent potency segregation, particularly if the API concentration is below 5% w/w. Gelatin or HPMC capsule shells conditioned to 13%–16% w/w moisture are standard. Open-dish stability at 40°C/75% RH for 14 days is used to detect shell-API incompatibility; seam split, shell shrinkage, or weight loss above 0.5% triggers reformulation or desiccant packaging. If a dosator machine causes agglomeration at the dosator tip, changing to a tamping-pin filling principle or modifying the plug compression force is the routine engineering intervention.

    When Ready-to-Use Injectable Solution Is Not Feasible, Lyophilization Parameters Govern the Injectable Presentation

    Terminal sterilization by moist heat is not assumed for Ecopipam O-β-D-glucuronide injectable presentations because autoclave conditions of 121°C/15 min may generate aglycone via hydrolytic cleavage, and published degradation kinetics for this conjugate under saturated steam are limited. Aseptic processing therefore follows 21 CFR 211.113 and 211.167, with pre-filtration bioburden controlled to ≤10 CFU/100 mL and bulk solution filtered through a 0.22 μm PVDF membrane. Filling operations are conducted in ISO 14644-1 Grade 5 laminar airflow with Grade 7/8 support zones. The formulation may include mannitol 4%–5% w/v as a crystalline bulking agent and a pH 6.0–7.5 buffer. Ionic strength must be measured because the glucuronide carboxylate contributes to osmolality; for intravenous dosing, a final osmolality target of 280–320 mOsm/kg is common.

    Lyophilization cycle design requires frozen-state thermal characterization by differential scanning calorimetry. Annealing at −5°C to −10°C for 2–4 hours can promote mannitol crystallization, but residual amorphous mannitol must be avoided because it weakens cake mechanical strength. Typical starting cycles for 10 mL vials use shelf ramp rates of 0.5–1.0°C/min from −40°C to 20°C and chamber pressure 100–200 mTorr; published cycles for this exact API are unavailable and should be developed by pilot-scale studies. After lyophilization, the cake is reconstituted in 5 mL WFI, and reconstitution time is normally not more than 2 minutes.

    Quality AttributeTest MethodTypical Acceptance Criterion
    Particulate matterUSP <788>≤6000 particles ≥10 µm and ≤600 particles ≥25 µm per container
    SterilityUSP <71>No microbial growth after 14 days
    Bacterial endotoxinUSP <85>Limit defined by maximum bolus dose per hour
    pHUSP <791>6.0–7.5
    OsmolalityUSP <785>280–320 mOsm/kg for IV administration
    Residual moistureUSP <921> Method Ic≤3.0% w/w for lyophilized cake

    Granules for Oral Solution Sachet and Bottle-Fill Technical Constraints

    For granules intended for reconstitution or direct oral administration, particle size distribution is the primary quality attribute because fines migrate to the bottom of sachets and hoppers. Sieve analysis per USP <811> should show not more than 10% retained on a 1.4 mm sieve and not more than 15% passing a 75 µm sieve. Packaging on vertical form-fill-seal lines requires room humidity below 40% RH to prevent particle agglomeration at heat-seal jaws. Desiccant selection follows USP <670>; silica gel canisters are used only if the sachet material has a low moisture vapor transmission rate.

    In low-dose granule presentations, content uniformity is sensitive to active particle size distribution and blender load. Geometric dilution with lactose monohydrate in three passes through a bin blender at 12 rpm for 15 minutes reduces potency variability below 5% RSD in general processing operations, but specific data for this glucuronide are limited. Rinsing and swab sampling protocols must account for the conjugate water solubility and possible adsorption to stainless steel contact surfaces; recovery studies should be validated per ICH Q2(R1). If the granule is reconstituted into a suspension, the final preparation should be tested for deliverable dose under simulated patient use, including cup rinsing and settling time.

    Dissolution Differentiation in Oral Dosage Forms Requires Apparatus and Medium Selection Tethered to In Vivo Surfactant Effects

    Dissolution testing of Ecopipam O-β-D-glucuronide tablets and capsules under USP <711> should not automatically adopt the aglycone method. The conjugate high aqueous solubility may produce rapid release in simulated gastric fluid pH 1.2, but food-effect studies for the parent drug suggest that surfactant concentrations in FaSSIF and FeSSIF change the apparent dissolution rate. Method development should therefore compare Apparatus 1 at 100 rpm and Apparatus 2 at 50 rpm using 900 mL media; pH 4.5 acetate, pH 6.8 phosphate, and 0.1 M HCl with 0.2% polysorbate 80 may be screened. No published dissolution specifications for this exact API are available. The final method must meet USP <1092> data requirements and exhibit discriminating power for deliberate process variants such as overlubricated blends or over-granulated batches.

    Sampling at 5, 10, 15, 30, 45, and 60 minutes is commonly used for immediate-release dosage forms, with Q at 30 minutes not less than 80%. If hydrophobic excipients delay disintegration, the profile may be extended; but if release exceeds 85% at 15 minutes, the method has limited discriminating power for upstream granulation changes. For process comparison after scale-up, the f2 similarity factor from FDA SUPAC-IR may be applied only when the reference and test profiles meet the one-point release criterion.

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    Certification & Compliance
    More Introduction

    Pharmaceutical-grade Ecopipam O-β-D-glucuronide is supplied as a Pharma Grade API for tablet, capsule, granule, and injection processing, covering both oral and injectable administration routes. The product is released under the production-stock identifier EPG-β-D-GlcA-PG/OI; this identifier is a lot-linked material code that connects the certificate of analysis to the master batch record, impurity profile, and reference standard inventory. It is supplied as a non-sterile solid for downstream formulation into tablets, capsules, granules, and injectable intermediates, with separate release criteria for oral non-sterile use and injectable-grade processing. The β-D-glucuronide moiety introduces a carboxylic acid residue and multiple hydroxyl groups, changing aqueous solubility, dissolution rate, solid-state hygroscopicity, and particle surface energy relative to the parent free base and methylated or sulfated metabolites. Identification relies on retention-time agreement with a qualified reference standard by high-performance liquid chromatography and infrared absorption according to USP <197>; assay is reported on anhydrous and solvent-free basis. Impurity, residual solvent, and elemental impurity control are aligned to ICH Q3A, ICH Q3C, and ICH Q3D. Published single-crystal X-ray diffraction data for this specific glucuronide are limited; therefore, polymorph designation is controlled by differential scanning calorimetry and X-ray powder diffraction against the approved production batch rather than by absolute crystal-structure assignment.

    Which release limits and compendial procedures define the injectable-grade boundary?

    For the injectable-grade boundary, the differentiating tests are bacterial endotoxin, subvisible particulate matter in the finished solution, and pre-filtration bioburden. The API itself is not usually a final sterile article; instead, the formulation is sterilised by aseptic filtration or terminal sterilisation after API dissolution. The API specification for injectable use therefore adds a bacterial endotoxin limit expressed in endotoxin units per milligram of API, determined by USP <85>. The limit is dose-linked: if the maximum adult dose is projected to be 100 mg/day, the endotoxin limit is calculated from 5 EU/kg/h divided by the maximum dose per kilogram per hour, expressed as EU/mg. Because the β-D-glucuronide linkage can be sensitive to the temperature and pH conditions of terminal sterilisation, filter compatibility and chemical stability of the dissolved conjugate often become the more restrictive factors. Table 1 summarises the release parameter matrix.

    ParameterReference procedureRelease criterion
    Assay on anhydrous and solvent-free basisHPLC-UV vs qualified reference standard98.0% to 102.0% w/w
    Related substancesHPLC area normalisationTotal impurities ≤2.0%; unspecified impurity ≤0.10%; specified impurities per certificate of analysis
    IdentificationUSP <197> infrared absorption; HPLC retention timeConforms to qualified reference standard
    Water contentUSP <921> Karl FischerReport result; limit tied to hydrate/solvate status
    Residual solventsUSP <467> headspace gas chromatographyICH Q3C limits for Class 1 and Class 2 solvents; Class 3 per Q3C Option 1
    Elemental impuritiesUSP <232>/USP <233>ICH Q3D permitted daily exposure by oral vs injectable route
    Bacterial endotoxins for injectable-grade materialUSP <85>Dose-linked limit; calculated per USP <85>; lot-specific
    Microbial limits for oral non-sterile materialUSP <61>/USP <62>Total aerobic microbial count ≤1000 CFU/g; total combined yeasts and moulds ≤100 CFU/g; absence of Escherichia coli
    Particle size distributionLaser diffraction ISO 13320 or USP <786>D10/D50/D90 reported; acceptance range defined by formulated process

    Routine release of oral-grade material excludes bacterial endotoxin but adds microbial limits under USP <61> and USP <62>. For injectable processing, the equivalent microbial control is achieved by pre-filtration bioburden monitoring and sterilising-grade filtration; the subvisible particle load in the finished injection is measured by USP <788> and must meet ≤6000 particles/container ≥10 μm and ≤600 particles/container ≥25 μm for the targeted fill volume.

    Stability-linked processing constraints for tablets, capsules, granules, and injectable solutions

    The β-D-glucuronide linkage is susceptible to acid-catalysed and enzymatic hydrolysis, while the aglycone may undergo oxidation if exposed to oxidising excipients. Forced-degradation studies are run under ICH Q1A conditions: 0.1 N HCl at 60°C, 0.1 N NaOH at 60°C, 3% H₂O₂, and photostability per ICH Q1B. These studies define the pH range for aqueous granulation and compounding. If the glucuronide shows more than 5.0% degradation in acid after 24 h, delayed-release or enteric coating may be required for oral dosage forms, but no assumption should be made without batch data; published data for this specific configuration are limited. Acyl glucuronides are more prone to intramolecular acyl migration and covalent protein adduct formation than ether-linked phenolic glucuronides. Ecopipam O-β-D-glucuronide is a phenolic O-β-D-glucuronide, so the primary chemical risk is hydrolytic release of ecopipam rather than acyl migration. Therefore, injection solutions are compounded at low temperature, and pH is adjusted to a range that balances solubility and linkage stability. Terminal heat sterilisation may be unsuitable if forced-degradation data demonstrate more than 0.5% aglycone formation at the sterilisation F0; aseptic filtration through 0.22 µm PVDF or polyethersulfone membrane is then used, with filter integrity testing by diffusion or bubble point per filter manufacturer method.

    For injectable processing, the API is dissolved in a vehicle selected for compatibility with the ionisable carboxylic acid group. If the vehicle contains phosphate buffer and the terminal pH exceeds the pKa of the glucuronic acid residue, the conjugate remains negatively charged and solubility is increased, but chemical stability may still be limited by base-catalysed degradation. The dissolved API is passed through a bioburden-reduction filter before sterile filtration. Prefiltration bioburden is controlled below 10 CFU/100 mL as a commonly applied process limit; the limit is verified by membrane filtration and plate count. The final filtered solution is filled under Grade A aseptic conditions; line setup includes a 0.22 µm sterilising-grade filter, with pre-use integrity testing. If the product is lyophilised, collapse temperature is measured by freeze-dry microscopy or differential scanning calorimetry, and the primary drying shelf temperature is set below the measured collapse temperature. Published data for this specific conjugate are limited, so cycle development cannot be transferred from the free base formulation.

    Dry mixing and direct compression of the glucuronide are constrained by particle-size distribution and flow behaviour. Because the material may exhibit cohesive flow due to the polar glucuronic acid surface, a powder flow measurement by USP <1174> is performed on the development batch. If compressibility index exceeds 30% or Hausner ratio exceeds 1.40, the formulation is shifted to wet granulation or roller compaction. Roller compaction equipment such as a Gerteis MINI-PACTOR or Alexanderwerk WP120 is used with gap setting and compaction force adjusted to produce ribbon solid fraction between 0.55 and 0.70; published roller-compaction parameters for this specific glucuronide are limited, so transfer from placebo runs requires direct measurement. For granules intended for tablet or capsule filling, loss on drying after fluid-bed drying is monitored by USP <731>, and moisture is kept below the value that causes glass transition depression and sticking. Granulation fluid volume is specified by torque or impeller power consumption in a high-shear granulator; end point is determined by wet mass consistency, not by fixed time. Drying in a fluid-bed dryer with inlet air temperature no greater than the value shown to produce ≤0.2% aglycone increase in forced-degradation studies is preferred. Milling of dried granules through a 0.5 mm or 0.8 mm screen produces a granule size distribution suitable for encapsulation. These process parameters are qualified by measuring content uniformity of the blend per USP <905> and by monitoring moisture by Karl Fischer USP <921>.

    Batch-to-batch variance in particle size distribution and specific surface area is mitigated by setting release limits for D10, D50, and D90 by laser diffraction. If the D90 exceeds the qualification range, dry milling may be required before formulation; if the D10 is too small, static charge and dusting during capsule filling may increase. Surface area measured by Brunauer-Emmett-Teller gas adsorption is reported if dissolution is surface-controlled; published data for this specific glucuronide are limited. The batch record requires in-process controls for blend uniformity according to USP <905> and for moisture according to USP <921> before compression or encapsulation.

    When the O-β-D-glucuronide conjugate replaces ecopipam free base, sulfate ester, or methyl ether in formulation development

    Substitution of Ecopipam O-β-D-glucuronide for ecopipam free base changes dissolution, permeability, and in vivo exposure. The free base is a lipophilic molecule with high passive permeability, whereas the glucuronide conjugate is a polar, acidic molecule with lower log P and greater aqueous solubility. This difference is measurable in shake-flask log P or chromatographic hydrophobicity index; exact values for this specific conjugate are not available in publicly accessible monographs. The sulfate conjugate has a different charge and a smaller solvation shell than the glucuronide; the methyl ether lacks the ionisable acid and has lower water affinity. Therefore, the glucuronide cannot be treated as a simple diluent substitution in a tablet or capsule formula. Dissolution testing per USP <711> should be developed with the formulated product and a discriminatory medium. If the glucuronide is used as a prodrug or as an active metabolite, the conversion to ecopipam in the gastrointestinal tract or plasma depends on β-glucuronidase activity; consequently, oral bioavailability is influenced by intestinal microbiota and may show food and disease-state variability. Published data for this specific configuration are limited.

    The product is not interchangeable with ecopipam base monographs. If a monograph for ecopipam lists O-β-D-glucuronide as a specified impurity or metabolite, release of the glucuronide as an API requires a separate impurity profile and acceptance criteria. Residual parent ecopipam is quantified as a process-related impurity with a specification limit justified by toxicological data. The material's difference from the parent is also reflected in storage: the glucuronide may be stored in a desiccator at controlled room temperature, while the free base may require protection from light but less stringent humidity control. Stability protocols follow ICH Q1A and ICH Q1B; for the injectable solution, a separate photostability assessment is required if the solution is light-sensitive.

    Analytical differentiation from ecopipam free base and the α-epimer or β-sulfate conjugate requires orthogonal methods. A reversed-phase HPLC method using a C18 column and mobile phase buffered at pH 3.0 may separate the polar glucuronide from the less polar free base; the glucuronide elutes earlier under acidic conditions. Because the anomeric purity of the β-D-glucuronide is critical, the product specification includes an HPLC method capable of separating α and β epimers. A resolution of ≥1.5 between α- and β-anomer peaks is targeted; if this is not achieved, a polar-organic or HILIC mobile phase is used. Structural confirmation of the O-β-D-glucosidic linkage uses 1H NMR and 13C NMR; the anomeric proton of β-D-glucuronide appears as a doublet with coupling constant J = 7–9 Hz, while the α-anomer exhibits a smaller coupling constant. This is consistent with carbohydrate stereochemistry and allows detection of anomeric impurity below the reporting threshold.

    Compared with a simple physical mixture of ecopipam free base and glucuronic acid, the O-β-D-glucuronide is a defined covalent conjugate and not a salt or co-crystal. This distinction changes the phase behaviour: a physical mixture may show two melting endotherms and dissolution dominated by the free base, while the conjugate exhibits a single phase with altered thermal events. Differential scanning calorimetry of the product is used to confirm the absence of free glucuronic acid or free ecopipam; the acceptance criterion is absence of the free base endothermic peak at its characteristic temperature, subject to the reference batch. The product also differs from the sodium salt of the glucuronide, which may be produced in situ during pH adjustment for injection; the sodium salt has higher water uptake and may require lower humidity handling.

    Cleaning of contact surfaces after processing the glucuronide must address the residual API's polarity and potential hydrogen bonding to stainless steel. The cleaning validation protocol uses swab sampling from product-contact surfaces, with an acceptance limit based on the maximum allowable carryover. A conservative limit is 10 ppm in the next product or 1/1000th of the lowest therapeutic dose, whichever is lower. Detection is by HPLC or total organic carbon; if total organic carbon is used, the limit is expressed as carbon rather than API. Because the glucuronide is water-soluble, warm detergent solutions are usually effective, but residue removal must be confirmed for the interior of the fluid-bed dryer filter bags and for the high-shear granulator bowl seals. Equipment cleaning is performed under 21 CFR 211.67.

    Compatibility with common parenteral excipients is assessed by visual inspection, pH, assay, and particle size after storage at 25°C and 2–8°C. If the solution is stored in a polyvinyl chloride bag, sorption to the bag material should be measured; because the glucuronide is hydrophilic, sorption is expected to be lower than for the free base, but the effect must be confirmed. For infusions, the diluted solution is tested for subvisible particles by USP <788> and for assay by HPLC at the proposed administration time. No data support material compatibility beyond the specific container-closure system documented in the regulatory file.

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