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4-(4-fluorophenyl)-6-isopropyl-2-[(n- methyl-n-methylsulfonyl)amino]pyriminl- 5-yl-methanol Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: 4-(4-fluorophenyl)-6-isopropyl-2-[(n- methyl-n-methylsulfonyl)amino]pyriminl- 5-yl-methanol 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 967701
    Product Name 4-(4-Fluorophenyl)-6-isopropyl-2-[(N-methyl-N-methylsulfonyl)amino]pyrimidin-5-yl-methanol Pharma Grade API
    Chemical Name 4-(4-Fluorophenyl)-6-isopropyl-2-[methyl(methylsulfonyl)amino]pyrimidin-5-yl-methanol
    Cas Number 355816-29-2
    Molecular Formula C16H20FN3O3S
    Molecular Weight 353.41 g/mol
    Appearance White to off-white crystalline powder
    Solubility Soluble in methanol, ethanol, DMSO, and acetone; practically insoluble in water
    Storage Conditions Store in a tightly closed, light-protected container in a cool, dry place
    Dosage Form Compatibility Suitable for tablet, capsule, granule, and injection dosage forms via oral and injectable pharmaceutical routes

    As an accredited 4-(4-fluorophenyl)-6-isopropyl-2-[(n- methyl-n-methylsulfonyl)amino]pyriminl- 5-yl-methanol 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 Packaging: 25 kg in sealed double polyethylene-lined drums, with desiccant, tamper-proof label; suitable for oral and injectable pharma grade API storage.
    Container Loading (20′ FCL) One 20-foot FCL loaded with pharma-grade API, carefully packed in sealed drums for tablet, capsule, granule, and injectable formulations.
    Shipping Ship as a controlled pharmaceutical active ingredient in sealed, moisture-proof containers, protected from light and heat. Transport in clean, dry vehicles under recommended temperature; include desiccant. Label “4-(4-fluorophenyl)-6-isopropyl-2-[(N-methyl-N-methylsulfonyl)amino]pyrimidin-5-yl-methanol Pharma Grade API.” Ensure GDP compliance, full documentation, and secure handling for oral/injectable formulations.
    Storage Store in a tightly closed container, protected from light and moisture, at controlled room temperature (20–25°C), with excursions permitted between 15–30°C. Keep in a cool, dry, well-ventilated area, away from incompatible substances. For Pharma Grade API used in oral and injectable dosage forms, ensure container integrity and avoid exposure to humidity.
    Shelf Life Shelf life is 24 months when stored in original container under recommended conditions, suitable for oral and injectable formulations.
    Application of 4-(4-fluorophenyl)-6-isopropyl-2-[(n- methyl-n-methylsulfonyl)amino]pyriminl- 5-yl-methanol Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    In oral immediate-release tablet manufacture by direct compression, the active compound is passed through a 40-mesh stainless steel sieve and dry-blended with microcrystalline cellulose and anhydrous lactose. The direct compression route is selected only when the resulting pre-blend exhibits a flow function coefficient above 6.0 in an annular shear cell test conducted according to ASTM D6128 and a Hausner ratio below 1.25. Lower values produce segregation across the die table and unacceptable weight variability on high-speed rotary presses. The API fraction is controlled between 5.0% and 20.0% w/w, with microcrystalline cellulose at 30.0–60.0% w/w, anhydrous lactose at 20.0–40.0% w/w, crospovidone at 2.0–5.0% w/w, and magnesium stearate at 0.25–1.0% w/w. The pre-lubrication blend is tumbled for 10 min at 25 rpm in a bin blender; magnesium stearate is then added and blended for an additional 3 min to limit overlubrication. Compression is performed on a 27-station rotary tablet press at 8–20 kN main compression force. Core tablets are accepted only when hardness is 60–120 N, friability is not more than 1.0% after 100 revolutions per USP <1216>, and disintegration is not more than 15 min per USP <701>. If neutral-pH solubility limits release, the dissolution medium is supplemented with 0.5% sodium lauryl sulfate; Q=80% at 30 min is used as an in-process release criterion in 900 mL of pH 6.8 phosphate buffer per USP <711> Apparatus II at 50 rpm. When ambient relative humidity exceeds 60%, direct compression is suspended or the blend is processed within 8 h because lactose absorbs moisture and magnesium stearate loses lubricant efficiency. The terminal product is a film-coated immediate-release tablet in PVC/aluminum blister packaging.
    ComponentFunctionw/w % rangeControl standard
    Active compoundAPI5.020.0USP <905>
    Microcrystalline celluloseFiller/binder30.060.0USP <1174>
    Anhydrous lactoseFiller20.040.0USP <731>
    CrospovidoneDisintegrant2.05.0USP <701>
    Magnesium stearateLubricant0.251.0USP <1216>

    What Limits Binder Level in High-Shear Wet Granulation for High-Dose Tablets?

    When the API fraction exceeds 25.0% w/w or particle-size distribution shows a span greater than 2.5, direct compression is replaced by high-shear wet granulation in a 600 L bowl with a three-blade impeller and side chopper. Hypromellose 2910 solution is prepared at 3.0–5.0% w/w dry basis and sprayed at 2.5–3.0 kg/min while the impeller runs at 180–220 rpm and the chopper at 1,800–2,000 rpm. The wet mass endpoint is determined by impeller power consumption; aqueous granulation above pH 8 is avoided unless forced degradation per ICH Q1B shows less than 2.0% assay loss after 3 h at 40°C. Drying in a fluid bed at 60°C inlet air is continued until loss on drying is 1.5–2.5% per USP <731>; the dried granulate is milled through a 1.0 mm conidur screen. Extragranular croscarmellose sodium at 2.0–4.0% w/w and magnesium stearate at 0.5% w/w are added before compression at 12–25 kN. Tablet hardness is specified at 80–150 N, friability at not more than 0.8%, and disintegration at not more than 10 min. Binder level above 5.0% w/w increases granulation viscosity and delays disintegration beyond 15 min; below 3.0% w/w granule friability increases and capping appears on the press. In-process testing is performed under FDA 21 CFR 211.110; the terminal product is a film-coated tablet for oral administration.After particle-size reduction through a cone mill fitted with a 1.0 mm screen at 1,000 rpm, the active compound is filled into hard gelatin capsules. The fill formulation consists of the API at 3.0–15.0% w/w, lactose monohydrate at 50.0–70.0% w/w, pregelatinized starch at 10.0–20.0% w/w, croscarmellose sodium at 2.0–4.0% w/w, and sodium stearyl fumarate at 0.5–1.5% w/w. The blend is sampled at 10 points after 15 min of mixing and content uniformity is verified before filling; the acceptance value must be not more than 15.0 per USP <905>. The capsule filler is a tamping-pin machine with five dosing stations, pin diameter 5 mm, and dosing chamber depth adjusted to a target fill weight of 180–240 mg for size 1 capsules. Fill weight is monitored every 15 min with limits of ±5.0% relative to target; empty shell moisture is equilibrated at 35–45% RH to avoid brittle fracture during filling. The finished capsule meets disintegration not more than 15 min per USP <701> and dissolution Q=80% at 30 min in 900 mL pH 6.8 buffer with 0.1% sodium lauryl sulfate if solubility-limited. The terminal product is a hard gelatin or hydroxypropyl methylcellulose capsule packed in aluminum-aluminum blisters.

    Dispersible Granules Packed in Sachets Require a Different Disintegrant Profile

    Top-spray fluidized-bed granulation is used when the oral product must be dispersed in water before administration. The API is first dry-blended with mannitol and crospovidone in a fluid bed at an inlet air temperature of 60–70°C. A binder solution containing povidone K30 at 2.0–4.0% w/w and, if required, ethylcellulose at 3.0–5.0% w/w for taste masking is sprayed at 20–30 g/min per kg batch. The granulation endpoint is a particle size D50 of 200–400 µm and loss on drying of 1.0–2.0% per USP <731>. Finished granules are sieved through 20-mesh and 60-mesh screens; the fraction between 20 and 60 mesh is packed at 500–1,000 mg into polyethylene-lined sachets. The disintegrant profile is shifted toward swelling agents: crospovidone at 3.0–6.0% w/w and sodium starch glycolate at 2.0–4.0% w/w are added both intragranularly and extragranularly. The terminal sachet product disperses in 20–30 mL water in less than 2 min; the suspension remains pourable for at least 30 min without sedimentation when xanthan gum at 0.2–0.5% w/w is incorporated. Dissolution is assessed by USP <711> Apparatus II at 50 rpm in 500 mL pH 6.8 buffer; Q=80% at 30 min is the release criterion. Water activity is controlled below 0.6 to inhibit microbial growth in the packed granule.Because parenteral administration requires a sterilizing-grade filtration step through a 0.22 µm polyethersulfone membrane, the preformulation screen begins with pH-solubility measurements from pH 3.0 to 8.0 in 0.05 M phosphate-citrate buffers under USP <791>. Published pH-rate profiles for this specific methanol derivative in parenteral cosolvent systems are limited; therefore forced degradation is executed per ICH Q1B before selecting terminal sterilization. When the aqueous solubility at pH 6.0–7.4 is below 5 mg/mL, a cosolvent system of propylene glycol 10.0–40.0% v/v and polyethylene glycol 300 at 10.0–30.0% v/v is screened. The formulation is adjusted to 280–320 mOsm/kg per USP <785> with sodium chloride or mannitol and to pH 5.5–7.0 with 0.1 N hydrochloric acid or sodium hydroxide. The bulk solution is filtered through a 0.45 µm polyethersulfone clarification membrane and then through two serial 0.22 µm sterilizing-grade filters under ISO 13408-1 aseptic processing. Terminal sterilization at 121°C for 15 min is used only if assay loss after one autoclave cycle is not more than 1.0% and the known impurity level remains within ICH Q3B limits. The container is Type I borosilicate glass tubing with a bromobutyl rubber stopper per Ph. Eur. 3.2.1; photolabile formulations are enclosed in amber glass if ICH Q1B light stress shows a quantifiable degradation product.

    Cryoprotectant Ratio and Primary Drying Limits in Lyophilized Vials

    Lyophilized injection is selected when the compound in aqueous solution fails to retain at least 95.0% assay after 24 h at 25°C or when terminal sterilization is not tolerated. The pre-lyo solution contains the API at 1.0–5.0 mg/mL, mannitol at 2.0–4.0% w/v as a crystalline bulking agent, and trehalose dihydrate at 2.0–5.0% w/v as an amorphous stabilizer. A phosphate-citrate buffer at 0.02–0.05 M maintains pH 6.0–7.0; polysorbate 20 at 0.005–0.02% w/v is added only if subvisible particle distress is observed after reconstitution. The solution is filled at 5.0 mL per 10 mL vial and loaded onto shelves pre-cooled to -40°C at 1.0°C/min. Annealing at -15°C for 2 h is introduced when mannitol crystallizes incompletely. Primary drying is carried out at a chamber pressure of 80–120 µbar and shelf temperature of -20°C for 36–48 h; secondary drying at +25°C for 6–10 h reduces residual moisture to not more than 1.0% w/w by Karl Fischer titrimetry per Ph. Eur. 2.5.12. The freeze-dried cake is accepted when it is white to off-white, retains cake structure after a 1.0 m drop, and reconstitutes in 2.0 mL water for injection in less than 2 min to a clear solution with pH 6.0–7.0, osmolality 280–320 mOsm/kg, endotoxin not more than 0.5 EU/mg per USP <85>, and sterility per Ph. Eur. 2.6.1.
    Lyophilization parameterSet point or rangeControl standard/method
    Pre-lyo API concentration1.05.0 mg/mLPh. Eur. 2.2.46
    Primary drying chamber pressure80–120 µbarCapacitance manometer
    Primary drying shelf temperature-20°CProduct temperature below collapse temperature
    Secondary drying temperature+25°CResidual moisture ≤1.0% w/w
    Reconstitution time<2 minVisual clarity, pH 6.0–7.0
    The terminal product is a lyophilized powder for solution for injection, aseptically processed in Type I glass vials and reconsituted with water for injection before administration.
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    Competitive 4-(4-fluorophenyl)-6-isopropyl-2-[(n- methyl-n-methylsulfonyl)amino]pyriminl- 5-yl-methanol Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable prices that fit your budget—flexible terms and customized quotes for every order.

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    Certification & Compliance
    More Introduction

    The product is released as a pharma-grade 4-(4-fluorophenyl)-6-isopropyl-2-[(N-methyl-N-methylsulfonyl)amino]pyrimidin-5-yl-methanol, identified by CAS 147118-36-3, molecular formula C16H20FN3O3S, and molecular weight 353.41 g/mol. The substance is a white to off-white crystalline powder intended for oral and injectable pharmaceutical manufacturing routes where the C5 primary alcohol is either carried forward as a synthetic handle or converted to the corresponding aldehyde, halide, or sulfonate ester. Although the product descriptor sometimes appears with the truncated spelling “pyriminl,” the CAS and IUPAC descriptions retain “pyrimidin.” The free alcohol is not equivalent to the final calcium heptenoate salt: it lacks the 3,5-dihydroxyheptenoic acid side chain and the calcium counterion, and therefore does not exhibit the same HMG-CoA reductase inhibition, aqueous solubility, or salt-dependent compaction behavior.

    Model coding across manufacturers is subordinate to the CAS registry number and IUPAC identifier. Purchase specifications should require CAS 147118-36-3 and the alternative description {4-(4-fluorophenyl)-6-isopropyl-2-[methyl(methylsulfonyl)amino]pyrimidin-5-yl}methanol because supplier-specific product codes may change without chemical equivalence. The release specification framework for tablet, capsule, granule, and injection work is built on compendial general chapters and ICH guidance rather than on a single product monograph, because no individual public monograph has been established for this intermediate.

    Table 1: Release-test matrix for pharma-grade 5-ylmethanol
    AttributeMethod or standard codeRepresentative pharma-grade release criterion
    AppearanceVisual inspection against referenceWhite to off-white crystalline powder
    Identification by IRUSP <197>Spectrum corresponds to reference standard
    Identification by HPLCUSP <621>Retention time matches reference standard
    AssayUSP <621>≥98.0% area normalized for a late intermediate
    Related substancesICH Q3A(R2)Unspecified impurity ≤0.10%, total impurities ≤1.0%
    Loss on dryingUSP <731>≤0.5% after 2 h at 60 °C under vacuum
    WaterUSP <921> Method Ic≤0.5%
    Residue on ignitionUSP <281>≤0.1%
    Elemental impuritiesICH Q3D, USP <232>/<233>Class-specific PDE-based limits
    Residual solventsUSP <467>, ICH Q3C(R8)Class 1 benzene ≤2 ppm; Class 2 cumulative per ICH Q3C
    Bacterial endotoxinsUSP <85>Injectable application limit set by monograph; commonly <0.25 EU/mg when aqueous solubility permits
    Particulate matterUSP <788>Injectable after reconstitution or terminal filtration
    SterilityUSP <71>Required only for sterile injectable final product

    The table is a specification-test menu rather than a batch certificate; each manufacturer must justify acceptance limits from process capability, stability data, and the intended route of administration. For oral solid forms, endotoxin and sterility are omitted; for injectable forms they are added.

    When the 5-ylmethanol oxidation state controls downstream process windows

    The C5 primary alcohol separates this product from the corresponding 5-carboxaldehyde, CAS 147118-37-4, and the 5-carboxylic acid, CAS 147118-35-2. The carboxaldehyde is a direct Wittig or Horner-Wadsworth-Emmons partner for side-chain extension, but it is more sensitive to air oxidation, hydrate formation, and self-condensation. The methanol form is selected when downstream activation is staged rather than immediate: the alcohol can be oxidized to the aldehyde under controlled conditions, or converted to a halide or sulfonate ester for phosphonium salt formation. This difference is not trivial in production. If residual alcohol remains in an aldehyde intermediate, it can quench the ylide and reduce coupling yield; if over-oxidation generates the carboxylic acid, aqueous workup may become complicated by emulsification and charge rejection. An HPLC method operated under USP <621> can resolve the alcohol, aldehyde, and acid using a C18 column and phosphate-buffered acetonitrile, provided relative retention times are established with reference standards.

    Published data for this specific configuration is limited, but process-development reports for closely related pyrimidine alcohols describe exothermic oxidation in glass-lined reactors with jacket temperature held below -50 °C for Swern-type activation. Endpoint control should target residual alcohol at ≤0.5% relative to the product before entering the next stage. The acid form may be selected if salt formation or esterification is required, while the aldehyde may be selected if direct C–C bond formation is the rate-limiting step.

    For tablet and capsule manufacture, the free alcohol may require particle-size modification before direct compression. The key physical properties are particle size distribution by laser diffraction under USP <429>, bulk and tapped density under USP <616>, and flow behavior through a shear cell. If the d90 exceeds 250 µm, dry granulation or wet granulation is usually required. In high-shear granulation, the granulation endpoint should be controlled by impeller torque and power consumption rather than a fixed water volume, because the primary alcohol can interact with water and produce overwetting. Tablet press parameters such as compression force, precompression, and turret speed must be established from experimental compaction profiles; direct substitution from the final calcium salt is not valid.

    What Limits Sterile Injectable Release for a Pyrimidinyl Alcohol Without a Terminal Carboxylate?

    Injectable processing imposes stricter requirements than oral solid processing. The free alcohol lacks an ionizable carboxylate, so pH adjustment alone may not achieve the solubility needed for a simple aqueous injectable. Co-solvent systems such as polyethylene glycol or cyclodextrin may be required, but compatibility data must be generated; published data for this exact configuration is limited. Endotoxin control is critical when water is used in the final purification or equipment rinse. Depyrogenation of equipment by dry heat or chemical inactivation must be validated, and the API must meet bacterial endotoxin limits under USP <85> before release for injectable use.

    Sterile filtration through a 0.22 µm PVDF or PES filter is common, but filter compatibility and drug binding must be tested under 21 CFR 211.67. If the primary alcohol is not stable to terminal moist-heat sterilization, aseptic processing under 21 CFR 211.113(b) is required. Residual solvent limits under ICH Q3C(R8) are also route-dependent: a lot that is acceptable for oral administration may not be acceptable for injection because the permitted daily exposure for Class 2 solvents is lower in parenteral products. Particulate matter must meet USP <788> after reconstitution or terminal filtration; if the API is milled to support oral dosing, the same lot may not be acceptable for injectable use without further purification.

    The oral and injectable routes therefore require separate release designations. Oral-grade material should be tested for microbial limits under USP <61> and <62>, while injectable-grade material requires endotoxin, particulate matter, and sterility when the final product is sterile. Particle size control is also route-specific: oral dry granulation may tolerate a broader distribution, while injectable processing generally requires finer, filterable material with low bioburden.

    Table 2: Comparative identity and processing role of structurally related pyrimidine substances
    SubstanceCASC5 functional groupMolecular weightKey processing role
    5-ylmethanol147118-36-3–CH2OH353.41Activation, oxidation, halogenation, sulfonate ester formation
    5-carboxaldehyde147118-37-4–CHO351.40Direct Wittig or Horner-Wadsworth-Emmons coupling
    5-carboxylic acid147118-35-2–COOH367.40Salt formation, esterification, amidation
    Rosuvastatin calcium147098-20-2Heptenoic acid calcium salt1001.14Final statin API for tablet, capsule, granule, and injectable finished dosage forms

    Release-test differentiation by route of administration

    The distinction matters in specification setting: the methanol is not a simple substitute for the final calcium salt in direct compression or injectable formulation. Pharmacopoeial assays for the final salt are not applicable; the methanol requires its own impurity markers, including the des-fluoro alcohol, N-demethylated sulfonamide, and oxidation products such as the C5 carboxaldehyde and C5 carboxylic acid. Each batch should be tracked by HPLC retention times and relative response factors established under ICH Q2(R1).

    Residual solvents must be controlled with reference to the actual manufacturing route. If halogenated solvents are used during alcohol activation, they require Class 2 or Class 1 assessment under ICH Q3C(R8). The N-methylsulfonylamino group may hydrolyze under forcing aqueous base at elevated temperature, so aqueous washes should be confined to controlled pH and time. Incoming raw material testing under 21 CFR 211.84 should include identity, assay, related substances, residual solvents, and elemental impurities; additional endotoxin and particulate matter tests are route-dependent.

    The compound may be stored in tightly closed HDPE or glass containers under nitrogen with desiccant. Primary alcohols of similar structure can undergo slow oxidation, so headspace oxygen and temperature should be controlled during long-term storage. For solid oral development, experimental compaction and excipient compatibility remain the decisive controls; for injectable development, filter compatibility, endotoxin, and particulate matter define release. The two uses are not interchangeable simply by changing the label.

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