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

    • Product Name: Maxacalcitol Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales10@sinochem-nanjing.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    VTB
    Specifications
    HS Code 448306
    Product Name Maxacalcitol Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    Api Name Maxacalcitol
    Synonyms 22-Oxacalcitriol; 22-Oxa-1alpha,25-dihydroxyvitamin D3; OCT; Oxarol
    Cas Number 103909-75-7
    Molecular Formula C26H42O3
    Molecular Weight 402.61 g/mol
    Drug Class Vitamin D3 analog; Vitamin D receptor agonist
    Mechanism Of Action Binds to vitamin D receptor, regulates calcium and phosphate homeostasis, inhibits keratinocyte proliferation, and promotes differentiation
    Appearance White to off-white crystalline powder
    Purity ≥98.0% (HPLC)
    Grade Pharma Grade; API
    Solubility Soluble in ethanol, methanol, and DMSO; practically insoluble in water
    Storage Conditions -20°C, protected from light, under inert gas, desiccated
    Dosage Forms Tablet, capsule, granule, injection
    Routes Of Administration Oral, injectable
    Therapeutic Indications Psoriasis, secondary hyperparathyroidism, calcium metabolism disorders
    Packaging Amber glass vial or sealed aluminum foil bag
    Shelf Life 24 months when stored properly
    Regulatory Status API for pharmaceutical manufacturing; prescription product
    Manufacturing Standard GMP-compliant

    As an accredited Maxacalcitol 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: 1 kg Maxacalcitol Pharma Grade API in double LDPE-lined aluminum foil bags, sealed in fiber drums, for oral and injectable formulations.
    Container Loading (20′ FCL) 20′ FCL loaded with Maxacalcitol Pharma Grade API for tablets, capsules, granules, oral and injectable use, securely sealed and temperature-controlled.
    Shipping Ship Maxacalcitol Pharma Grade API in sealed, light-resistant, pharma-grade containers under controlled temperature, typically 2–8°C, protected from moisture, heat, and light. Use qualified packaging, temperature monitoring, and compliant labeling for tablet, capsule, granule, oral, and injectable forms. Maintain cold chain; avoid freezing unless specified.
    Storage Store Maxacalcitol Pharma Grade API in original, tightly sealed, light-resistant containers under inert gas at -20°C (or 2–8°C if validated short-term). Protect from light, moisture, heat, and oxygen. Avoid repeated freeze-thaw. Keep away from incompatible materials. Maintain clean, dry, controlled conditions for oral and injectable-grade use. For injectable-grade, maintain sterile, endotoxin-controlled handling. Follow cGMP, label instructions, and first-in-first-out rotation.
    Shelf Life Shelf life: typically 24–36 months for oral solid and injectable Maxacalcitol API when stored protected from light, heat, and moisture.
    Application of Maxacalcitol Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    In direct-compression tableting of maxacalcitol, the principal process conflict arises from the combination of a microgram-level active concentration and a compression cycle that leaves limited residence time for corrective blending. A tablet core with a mass of 100 mg containing 2.5 µg maxacalcitol corresponds to 0.0025% w/w; the 10 µg strength at the same core mass corresponds to 0.010% w/w. At this concentration, direct addition of the API to the final blender without staged dilution produces superpotent and subpotent stratified samples. The manufacturing procedure therefore starts with a 1:10 (w/w) API-to-lactose monohydrate premix, passed through a 500 µm stainless-steel screen, then geometrically diluted with spray-dried lactose monohydrate, microcrystalline cellulose, croscarmellose sodium and colloidal silicon dioxide. Final lubrication uses magnesium stearate at 0.25–0.5% w/w in a bin blender fitted with an intensifier bar; extended lubrication beyond 10 minutes is avoided because hydrophobic film formation on the carrier particles retards tablet disintegration. The blend is compressed on a rotary press with forced feeders and B-tooling at hardness ranges adjusted to 50–100 N; tablet weight and hardness are monitored at 15-minute intervals during the batch. Compliance testing for the terminal immediate-release tablet includes blend uniformity sampling after press setup, content uniformity per USP <905> with acceptance value ≤15, and dissolution per USP <711> using apparatus II with a surfactant-containing medium selected under ICH Q6A decision tree principles. Residual solvents and elemental impurities are controlled per ICH Q3C and ICH Q3D; in-process sampling is governed by 21 CFR 211.110. The terminal finished product type is an uncoated immediate-release tablet intended for once-daily oral administration, with the uncoated core serving as the substrate for subsequent light-protective film coating or final packaging in opaque blister materials.

    What Limits Blend Uniformity in Low-Dose Maxacalcitol Capsule Formulations?

    Segregation of the micronized active from coarse carrier particles during transfer and hopper residence in capsule filling is the principal source of blend non-uniformity, rather than chemical incompatibility with the shell. A size 4 hard capsule with a 120 mg fill weight containing 5 µg maxacalcitol gives 0.00417% w/w; a 160 mg fill at 10 µg gives 0.00625% w/w. The API is pre-dispersed in 1:20 (w/w) with sieved mannitol or lactose monohydrate before final low-shear blending in a V-blender at 10–15 rpm for 15–20 minutes. Ordered mixing using a carrier with particle size substantially larger than the API is applied to reduce dusting and electrostatic drift; the lubricant is magnesium stearate at 0.25% w/w, screened through a 250 µm mesh and added at the end of blending. The blend is filled on a dosator or tamping-pin capsule filler, with empty shell handling maintained at 45–50% RH for gelatin or 35–45% RH for HPMC to avoid brittleness, static charging and capsule deformation. In-process controls include fill weight variation, disintegration and stratified blend sampling from the hopper. The terminal finished product type is a hard gelatin or HPMC capsule containing an immediate-release powder blend; compliance includes content uniformity per USP <905>, dissolution per USP <711> using the capsule method, residual solvents per ICH Q3C, elemental impurities per ICH Q3D, and charge-in verification under 21 CFR 211.101.

    When Roller-Compacted Granules Replace Direct Compression for Maxacalcitol Sachet Filling

    Roller compaction is selected when the terminal dose form is a granule-filled sachet and direct compression cannot provide sufficient bulk density or flow for stick-pack filling at low fill weights. A 500 mg sachet with 2.5 µg maxacalcitol corresponds to 0.0005% w/w; a 1,000 mg sachet with 10 µg corresponds to 0.001% w/w. Because the active mass fraction is below the detection limit of ordinary process sensors, a staged dry pre-blend is prepared at 1:50 (w/w) with mannitol and then processed through a roller compactor using 100 mm rolls, hydraulic pressure 40–120 bar, gap 1.0–2.5 mm, and roll speed 4–12 rpm. Ribbon density is held between 0.9 g/cm³ and 1.2 g/cm³ to avoid both brittle fines and hard granules; the ribbon is subsequently milled through a 0.8 mm screen with an oscillating granulator, and the 250–800 µm granule fraction is collected. Fines below 250 µm are recycled at a controlled rate to prevent accumulation of API-rich fines; recycle load above 30% of fresh feed increases segregation risk and is avoided. The granules are filled into stick packs on a vertical form-fill-seal machine with nitrogen flush if the packaging material is not opaque. The terminal finished product type is an oral granule sachet; compliance testing includes unit dose uniformity per USP <905>, moisture content ≤2.0% w/w, related substances per ICH Q3B(R2), residual solvents per ICH Q3C, elemental impurities per ICH Q3D, and in-process sampling under 21 CFR 211.110.

    Sterile injectable manufacturing of maxacalcitol is constrained by the heat lability and light sensitivity of the molecule; terminal steam sterilisation is generally avoided when forced degradation studies show unacceptable related substance formation. A single-dose 1 mL presentation containing 2.5 µg or 5.0 µg maxacalcitol corresponds to 0.00025% w/v and 0.0005% w/v, respectively. For the poorly water-soluble active, formulation development uses a parenteral-grade co-solvent or non-ionic surfactant, with exact levels limited by the target market pharmacopoeial monograph, parenteral tolerability, and ICH Q3C when ethanol or propylene glycol is present; published data for this specific configuration is limited. The bulk solution is compounded under nitrogen overlay in stainless-steel vessels and filtered through a sterilising-grade 0.22 µm PVDF or polyethersulfone membrane; bioburden before filtration is maintained at ≤10 CFU/100 mL. The filtrate is filled aseptically into amber type I glass vials or ampoules inside an isolator or RABS meeting ISO 14644-1:2015 Class 5 at rest; stoppers are inserted under inert headspace, and ampoules are melt-sealed. Particulate matter is controlled per USP <788>, bacterial endotoxins per USP <85>, sterility per USP <71>, and the process is validated under EU GMP Annex 1:2022 with media-fill runs, filter integrity testing, and hold-time validation. The terminal finished product type is a sterile injectable solution for intravenous use, packaged with secondary light protection because vitamin D analogues are degraded by ultraviolet and visible light.

    Light-Protective Film Coating of Low-Dose Maxacalcitol Tablets

    Film-coating of maxacalcitol tablet cores is performed to reduce photodegradation and improve mechanical integrity during blister packaging. The core contains 2.5 µg, 5.0 µg or 10 µg of maxacalcitol and is coated to a weight gain of 2.0–4.0% w/w based on the 100 mg core. A 2.5 µg dose in a 103 mg coated tablet at 3% weight gain corresponds to 0.00243% w/w; a 10 µg dose in a 104 mg coated tablet at 4% weight gain corresponds to 0.00962% w/w. The coating suspension is prepared at 10–15% w/w solids using an HPMC- or PVA-based film former combined with titanium dioxide and iron oxide opacifiers; the opacifier grade and coating thickness are selected to reduce light transmission in the 280–450 nm range. A perforated pan coater with inlet air temperature 55–65°C, exhaust air 40–50°C, atomising air pressure 1.5–3.0 bar, and spray rate 2–6 g/min per kg of tablet bed is used; tablets are preheated to 40–45°C before spraying to avoid overwetting. Spray rate above 6 g/min per kg risks logo bridging and tablet-to-tablet sticking, while atomising air below 1.0 bar causes orange peel and poor film uniformity. The terminal finished product type is a light-protective film-coated tablet; process validation is governed by 21 CFR 211.113, photostability is assessed under ICH Q1B, and dissolution of the coated tablets is tested per USP <711> to confirm that the coating does not delay drug release beyond the specified acceptance range.

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    Certification & Compliance
    More Introduction

    Maxacalcitol Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable is a secosteroidal vitamin D receptor agonist supplied as the 22-oxa analogue of calcitriol. The material is released for incorporation into low-dose solid oral dosage forms and injectable finished drug product where the active pharmaceutical ingredient is present in the microgram range. Two physical grades are commonly used: a micronized grade for direct compression or capsule filling and a crystalline grade for wet or dry granulation. The certificate of analysis should state particle size distribution by laser diffraction according to ISO 13320, loss on drying, residue on ignition, residual solvent profile, and assay relative to a pharmacopoeial reference standard. For injectable applications, additional release controls for bacterial endotoxins, bioburden, and subvisible particulate matter after reconstitution are required. The product is not interchangeable with calcitriol, alfacalcidol, doxercalciferol, or paricalcitol without formulation revalidation: the 22-oxa side-chain changes lipophilicity, oxidative sensitivity, and vitamin D receptor transactivation behavior compared with the parent secosteroid. In finished product, Maxacalcitol is used for suppression of parathyroid hormone secretion in secondary hyperparathyroidism associated with end-stage renal disease. Because the therapeutic dose is low, the API imposes stricter uniformity, cleaning, and cross-contamination controls than high-dose drugs.

    What release specifications and ICH compliance thresholds govern the API for dual oral and parenteral routes?

    Release specifications are route-dependent. For oral solid dosage forms, the API release panel typically includes appearance, identification by infrared absorption and high-performance liquid chromatography retention time, assay, related substances, residual solvents, elemental impurities, water content, and particle size distribution. A pharmacopoeial assay window of 98.0%–102.0% on the anhydrous basis is common; a tighter registered specification may be justified by stability data. Related substances are controlled under ICH Q3A. For a maximum daily dose of 10 mg or less, the identification threshold is 0.10% or 1.0 mg total daily intake, whichever is lower, and the qualification threshold is 0.15% or 1.0 mg total daily intake, whichever is lower. Because Maxacalcitol doses are in the microgram range, the percentage thresholds remain the critical limits; the absolute daily intake mass may be many orders of magnitude higher than the actual impurity burden. Residual solvents are controlled by ICH Q3C Option 1 for Class 1, Class 2, and Class 3 solvents. Injectable grades require a headspace gas chromatography method with sufficient sensitivity to detect Class 1 solvents below their limiting concentrations. Elemental impurities are assessed per ICH Q3D for both oral and parenteral permitted daily exposure values; the parenteral assessment applies the more restrictive limits for cadmium, lead, arsenic, mercury, and catalyst-derived elements. Because the secosteroid is sensitive to oxygen and light, the container closure system commonly uses amber glass or foil laminate with desiccant and oxygen absorber under nitrogen headspace. Stability-indicating methods are validated according to ICH Q2(R1). Long-term storage is typically controlled at 2–8°C, with accelerated testing at 25°C/60% RH and photostability testing under ICH Q1B.

    Attribute Method or reference Route-specific note
    Identification IR and HPLC retention time relative to reference standard Required for oral and injectable grades
    Assay HPLC with pharmacopoeial reference standard Anhydrous basis
    Related substances ICH Q3A thresholds Identification threshold 0.10% or 1.0 mg total daily intake
    Residual solvents ICH Q3C Option 1 Class 1 and 2 solvents by headspace GC
    Elemental impurities ICH Q3D Separate oral and parenteral PDE assessments
    Particle size distribution ISO 13320 laser diffraction D90 and D50 controls for solid dosage forms
    Microbial limits USP <61> / Ph. Eur. 5.1.4 Non-sterile oral grade
    Bacterial endotoxins USP <85> / Ph. Eur. 2.6.14 Injectable grade
    Subvisible particulate matter USP <788> / Ph. Eur. 2.9.19 Injectable finished product after reconstitution
    Visible particulate matter USP <790> Injectable finished product
    Sterility USP <71> / Ph. Eur. 2.6.1 Finished injectable only

    Because the therapeutic dose is in the microgram range, direct compression and capsule filling are constrained by segregation, electrostatic adhesion, and dissolution of the micronized API. A drug load below 0.1% w/w is not blended directly. A pre-blend at 1:10 API-to-diluent ratio is prepared in a V-blender or bin blender fitted with an intensifier bar, then diluted geometrically to an intermediate concentration near 0.5% w/w before final lubrication. Magnesium stearate is added at the end, with total lubrication time limited to 3–5 min to avoid overlubrication and dissolution slowdown. Dissolution is monitored by USP <711> Apparatus 2 or JP 18 General Test 6.10, with the method selected to maintain sink conditions. Granulation may be required when direct compression produces an acceptance value greater than 15 under USP <905> or JP 18 General Test 6.02. For low-dose granulation, Maxacalcitol can be dissolved in ethanol and sprayed onto mannitol or microcrystalline cellulose in a fluid-bed granulator with a Wurster column. The spray rate and inlet air dew point are controlled to limit thermal degradation and moisture uptake. Because the molecule is oxygen-sensitive, the granulation headspace is nitrogen-blanketed and the product temperature is maintained below 35°C. Production-scale bottlenecks include electrostatic charging of micronized API during transfer, wall losses, and blend assay drift. Contact surfaces should be 316L stainless steel or compatible polymer, with grounding and relative humidity maintained at or below 40% RH in weighing and sifting suites. Cross-contamination control for a microgram-level API requires dedicated suites, validated cleaning limits, and swab sampling analyzed by LC-MS/MS. Batch-to-batch variance in particle size at D90 above 15 µm may cause content uniformity failure in direct compression. Micronized API is therefore typically controlled with D90 not greater than 10 µm and D50 in the 2–5 µm range, measured by laser diffraction with dry dispersion at 0.1–0.3 MPa air pressure according to ISO 13320.

    Particle geometry, specific surface area, and photodegradation limits in injectable formulation

    Because Maxacalcitol is a hydrophobic secosteroid, aqueous injectable formulation requires a cosolvent system, a surfactant-based micellar vehicle, or a cyclodextrin inclusion complex. The choice changes the ability to use terminal sterilization. Terminal moist heat sterilization at 121°C for 15 min is generally incompatible with the 22-oxa side-chain when oxygen and trace iron are present. Oxidative degradation produces compounds with altered vitamin D receptor binding. Production-scale injectable processing therefore commonly uses aseptic filtration through a 0.22 µm polyvinylidene fluoride or polyethersulfone membrane. The API is pre-dissolved in a sterile-filtered ethanol/propylene glycol phase under nitrogen. Filter compatibility is evaluated for plastic components according to ISO 10993 or USP <88>, and maximum filtration pressure is controlled to prevent particle shedding. Bacterial retention of the filter is verified with Brevundimonas diminuta at a challenge of 10⁷ CFU per cm² according to ASTM F838-20. Endotoxin control for the parenteral finished product is tested by USP <85> or JP 18 Bacterial Endotoxins Test. The limit is derived from the maximum adult dose using the K/M formula, commonly yielding a limit in the range of 0.5–5.0 EU per mg of API or per vial, subject to route and dosing schedule. The API for injectable use must also meet clarity and particulate controls after reconstitution. Visible particles are assessed per USP <790>, and subvisible particles per USP <788> or Ph. Eur. 2.9.19. Processing under yellow or red light is required because the vitamin D triene chromophore undergoes photoisomerization. Light protection is validated under ICH Q1B. Storage with nitrogen headspace reduces pre-vial precipitation and oxidative damage.

    When Maxacalcitol injection routes are terminal sterilized rather than aseptically filtered, which stability-limiting degradation pathways appear first?

    When Maxacalcitol injection routes are terminal sterilized rather than aseptically filtered, the stability-limiting pathways that appear first are oxidative opening of the secosteroid ring and cis-trans isomerism of the triene chromophore. Forced degradation at 80°C in the presence of hydrogen peroxide or transition-metal spiking can generate degradation products detectable by HPLC, but published data for this specific configuration is limited. The formulation cannot be autoclaved without an oxygen-scavenging overlay and metal chelator; even then, assay loss may exceed 5% after 15 min at 121°C. Aseptic filtration is therefore preferred when short heat exposure and a release assay of 98.0%–102.0% must be preserved. If terminal sterilization is requested, the product dossier should contain comparative stability data at 121°C for 15 min and F0 values between 8–12, according to Ph. Eur. 5.1.1 and ISO 17665-1. Process conflicts arise because the ethanol cosolvent can reduce steam penetration and require vacuum cooling, and residual water can cause API precipitation. Terminal sterilization is not applicable when the formula contains no antioxidant or when the pH is outside 5.0–7.5. In such cases, aseptic processing under ISO 13408-1 and EU GMP Annex 1 is the defined route.

    In contrast to calcitriol, the 22-oxa substitution in Maxacalcitol reduces the calcemic liability at equivalent parathyroid hormone-suppressive activity in published preclinical models. Compared with alfacalcidol, Maxacalcitol does not require hepatic 25-hydroxylation for activation, which removes a metabolic activation step and reduces dependence on hepatic enzyme capacity. Compared with paricalcitol, the active substance retains the vitamin D3 nucleus rather than the 19-nor vitamin D2 scaffold, and the side-chain ether linkage alters vitamin D receptor dissociation kinetics. These differences affect not only clinical handling but also pharmaceutical development: the solubility, oxidative stability, and photostability profiles differ enough that formulation methods validated for calcitriol or alfacalcidol cannot be transferred directly to Maxacalcitol without forced degradation testing, excipient compatibility studies, and process validation. For tablet and capsule manufacture, the main operational boundary is the microgram-level drug load, which requires geometric dilution, particle size control, and strict cleaning validation. For granule and injection manufacture, the main boundary is oxygen and light exposure during processing. Published data for formulation-specific failure modes of this API in all possible vehicles is limited; therefore each formulation must be characterized using stability-indicating methods and route-specific acceptance criteria.

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