| HS Code | 626075 |
| Productname | Aripiprazole Pharma Grade API |
| Dosageforms | Tablet, Capsule, Granule, Injection |
| Routesofadministration | Oral and Injectable |
| Casnumber | 129722-12-9 |
| Molecularformula | C23H27Cl2N3O2 |
| Molecularweight | 448.39 g/mol |
| Iupacname | 7-[4-[4-(2,3-dichlorophenyl)piperazin-1-yl]butoxy]-3,4-dihydro-1H-quinolin-2-one |
| Pharmacopoeiagrade | Pharma Grade API |
| Appearance | White to off-white crystalline powder |
| Assay | 98.0% to 102.0% on dried basis |
| Purity | >=99.0% |
| Solubility | Slightly soluble in water; soluble in methanol, ethanol, and dimethyl sulfoxide |
| Meltingpoint | 139-141 °C |
| Storageconditions | Store in a cool, dry place, protected from light and moisture |
| Therapeuticcategory | Atypical antipsychotic |
| Mechanismofaction | Partial agonist at dopamine D2 and serotonin 5-HT1A receptors; antagonist at serotonin 5-HT2A receptors |
| Manufacturingstandard | cGMP |
| Shelflife | Typically 24-36 months when stored as directed |
As an accredited Aripiprazole 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.
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In a direct-compression or roller-compacted immediate-release tablet line, aripiprazole API is first delumped through a 500 µm stainless steel screen and then blended at a drug mass fraction that depends on the target label claim of 2 mg, 5 mg, 10 mg, 15 mg, 20 mg, or 30 mg. The free base has low bulk density and moderate cohesive behaviour, so low-dose blends containing less than 1.0% API are particularly susceptible to segregation and content uniformity failure. A production-scale bin blender of 600 L typically requires 15–25 min at 8–12 rpm to reach acceptable blend homogeneity, but published data for this exact formulation configuration is limited. Lactose monohydrate, maize starch, microcrystalline cellulose, hydroxypropyl cellulose, and magnesium stearate are added sequentially; magnesium stearate is screened through a 500 µm mesh and blended for only 3–5 min to avoid excess lubrication and dissolution slowdown. Roller compaction on an Alexanderwerk WP 120 or Gerteis MACRO-PACTOR is operated at a specific roll force of 8–18 kN/cm and a roll gap of 2–4 mm to produce ribbon density of 1.1–1.3 g/cm³; milling through a 0.8–1.0 mm screen gives granules with a D50 in the 180–250 µm range. Tablets are compressed on a 45-station rotary press with flat-faced bevel-edged tooling, precompression force 2–5 kN, and main compression force adjusted to a hardness of 5–10 kP. Friability is maintained below 0.8% after 100 drops when tested according to USP <1216>. Dissolution is evaluated using USP <711> Apparatus 2 at 50 rpm in 900 mL of 0.1 N HCl at 37 °C; in approved immediate-release tablet dossiers, a Q value of 80% at 30 min is commonly applied for aripiprazole tablets. Assay and related substances are determined by reverse-phase HPLC with UV detection at 254 nm, and the finished tablet must satisfy USP <905> uniformity of dosage units with an acceptance value of 15.0 or less. Residual moisture is controlled below 2.0% loss on drying by Ph.Eur. 2.2.32 to prevent polymorphic conversion of the anhydrous form to monohydrate during shelf life. Elemental impurities are assessed according to ICH Q3D, with Class 1 and Class 2A limits applied at the finished-product level on the basis of a 30 mg maximum daily dose.
When a 5 mg aripiprazole capsule is filled at a total fill weight below 120 mg, the API mass fraction is 4.2%; for a 2 mg capsule at 100 mg fill weight the fraction drops to 2.0%. Content uniformity risk rises sharply because the API is practically insoluble and is not wet-massed, so the dry blend must be produced by geometric dilution rather than single-pot mixing. A 25 kg high-shear granulator may be used only as a preblender with chopper speed 300–500 rpm and impeller speed 150–250 rpm for 5–8 min; the resulting preblend is then passed through a 600 µm sieve. Lactose monohydrate is the primary diluent, with 0.5% colloidal silicon dioxide added as a glidant and 1.0–2.0% magnesium stearate added as a lubricant. Capsule filling on an MG2 Planeta or Zanasi 6/E continuous motion machine uses size 0 hard gelatin or HPMC shells; speed is typically limited to 50,000–80,000 capsules/h because low fill weight and electrostatic charge reduce powder flow into the dosator nozzle. HPMC shells are preferred for export to ICH Zone IVb markets because gelatin crosslinking under elevated temperature and humidity can reduce dissolution rate and create false failures in USP <711> testing. Process analytical technology such as near-infrared blend uniformity scanning at 15 min intervals with a 10 capsule sample is used to detect segregation before filling. The finished capsules are tested for content uniformity according to USP <905> with an acceptance value of 15.0 or less, and dissolution under USP <711> Apparatus 2 at 50 rpm in 900 mL of 0.1 N HCl with sinkers. Terminal capsule strengths of 2 mg, 5 mg, 10 mg, 15 mg, 20 mg, and 30 mg are produced from the same validated master blend; batch-to-batch variance in fill weight RSD is kept below 2.0% for fill weights above 100 mg.
A top-spray fluid-bed granulator with an 18 L bowl and 1.0 mm two-fluid nozzle is used to layer aripiprazole monohydrate onto mannitol and xylitol substrates for sachet-based oral suspension granules. The binder solution is hydroxypropyl cellulose 5.0% w/w in purified water, sprayed at inlet air temperature 60–70 °C and atomization pressure 1.5–2.5 bar; product temperature is maintained below 40 °C during spraying to avoid monohydrate dehydration and agglomeration. Aripiprazole is pre-suspended or pre-dispersed in the binder solution with the aid of 0.1–0.3% polysorbate 80, and the suspension is kept under continuous stirring to prevent sedimentation during spraying. Granule growth is controlled by spray rate ramp from 10 g/min to 25 g/min for a 5 kg batch; after spraying, the material is dried to a loss on drying of 1.5–2.5% by Ph.Eur. 2.2.32. The final granules are screened through a 1.0 mm sieve to remove oversize material; D50 is typically 150–250 µm, and bulk density is 0.55–0.65 g/mL. Crospovidone 3.0% is added as extragranular disintegrant after drying, along with 0.5% colloidal silicon dioxide, sucralose, and orange flavour. Sachet fill weight is 500 mg or 1000 mg depending on the dose; the granules are dispersed in 30–50 mL of water immediately before administration. The suspension pH after reconstitution is controlled between 5.5 and 7.5; viscosity and sedimentation volume are monitored during development because aripiprazole monohydrate undergoes slow wetting in aqueous media. Microbiological quality is assessed by Ph.Eur. 2.6.12 total aerobic microbial count and Ph.Eur. 2.6.13 specified organisms; water activity is maintained below 0.60 to prevent microbial growth in single-dose sachets. The terminal granule dosage form is used in clinical titration kits and in pediatric or dysphagia patient populations where tablet swallowing is compromised.
The long-acting injectable suspension is manufactured from aripiprazole monohydrate that is wet-milled to a Dv90 of 2.5 µm or less and a Dv50 of 1.0–1.5 µm. Milling is performed on a recirculating bead mill with 0.3 mm yttrium-stabilized zirconia beads at a tip speed of 10–14 m/s; the suspension contains mannitol as a tonicity modifier and a cellulosic suspending agent, with pH adjusted to 6.5–7.5 using sodium hydroxide. Particle size is monitored by laser diffraction according to ISO 13320-1:2020 and USP <429>. The milled suspension is filled into vials and lyophilized; the lyophilization cycle must maintain product temperature below -20 °C during primary drying and below 25 °C during secondary drying to avoid dehydration of the monohydrate and irreversible particle aggregation. After reconstitution with sterile water for injection, the suspension concentration is 200 mg/mL; the 300 mg vial is reconstituted with 1.5 mL and the 400 mg vial with 2.0 mL. The dosing volume is given by deep intramuscular gluteal injection; the suspension is designed for 28-day release through slow dissolution of the low-solubility monohydrate particles.
| Quality attribute | Method | Acceptance criterion |
|---|---|---|
| Sterility | USP <71> | No growth after 14 days |
| Bacterial endotoxin | USP <85> | Validated limit specific to the finished product monograph |
| Particulate matter | USP <788> | ≥10 µm: NMT 6000/container; ≥25 µm: NMT 600/container |
| Particle size | ISO 13320-1:2020 | Dv50 1.0–1.5 µm; Dv90 ≤ 2.5 µm |
| pH after reconstitution | USP <791> | 6.5–7.5 |
The main process conflict arises because particle size reduction increases both depot dissolution control and Ostwald ripening risk; the cellulosic suspending agent is therefore added to raise low-shear viscosity to 15–40 mPa·s at 25 °C, measured with a Brookfield viscometer at 60 rpm. If the Dv90 exceeds 2.5 µm, injectability through 21 G needles deteriorates and delivered dose uniformity may fail; if the Dv50 falls below 0.5 µm, release may become too fast and the 28-day dosing interval cannot be maintained. Lyophilization also requires precise control of the frozen-state microstructure, because collapse or meltback leads to cakes that are difficult to reconstitute and may trap API agglomerates. The sterile diluent is filled in separate vials and must meet USP <71>, USP <85>, and USP <788> requirements as a water for injection-based product.
Because aripiprazole free base remains practically insoluble at neutral pH, a short-acting intramuscular injection is formulated in an acidified aqueous vehicle rather than as a neutral suspension. The API is dissolved at a concentration of 7.5 mg/mL in a vehicle containing an organic acid buffer and water for injection; the solution pH is maintained between 2.8 and 3.5 to keep the protonated tertiary amine in solution. The solution is sterile-filtered through a 0.22 µm PVDF membrane into sterilized 2 mL Type I glass vials; fill volume is 1.3 mL with a small overage to compensate for needle hub loss during withdrawal. Terminal analysis includes assay by HPLC with UV detection at 254 nm, pH by USP <791>, osmolality by USP <785>, particulate matter by USP <788>, sterility by USP <71>, and bacterial endotoxin by USP <85>. Vial compatibility is evaluated under USP <660> for glass surface durability and USP <1663> extractables assessment; terminal sterilization of the acidified solution is usually limited to aseptic filtration because terminal heat sterilization can cause pH shift and degradation of aripiprazole-related impurities. The marketed single-dose vial delivers 9.75 mg of aripiprazole per 1.3 mL injection. Intramuscular administration is normally into the deep deltoid or gluteal muscle using a 21–23 G needle; the injection is not intended for intravenous use, and any visible precipitate formed by neutralization with blood can be avoided by ensuring appropriate needle length and injection depth. The short-acting injection is used for acute agitation in schizophrenia or bipolar mania; the terminal product is stable in the acidified solution as long as pH is held below the upper control limit, because solubility drops sharply when pH approaches the pKa of aripiprazole.
The manufacture of orally disintegrating tablets introduces a direct conflict between mechanical strength and disintegration speed, and this conflict is more severe for aripiprazole because the API is hydrophobic and can become trapped in polymer matrices. Two routes are used: freeze-drying of a suspension in preformed blister pockets, and direct compression of mannitol-based granules with high levels of crospovidone. In the freeze-drying route, aripiprazole monohydrate is dispersed in a solution of gelatin or fish gelatin, mannitol, and xanthan gum, then dosed into 0.5 mL blister pockets and lyophilized. The finished unit disintegrates in less than 30 s when tested by USP <701> in 900 mL water at 37 °C, but mechanical strength is limited to handling without direct push-through force. In the direct compression route, mannitol with a D50 of 100–150 µm, crospovidone 5–10%, microcrystalline cellulose 10–20%, sucralose, and an orange or peppermint flavour are blended with API; compression force is kept below 8 kN to avoid densification that slows water ingress. The resulting tablet hardness is 20–40 N, friability is below 1.0%, and disintegration time is 15–60 s by USP <701>. Freeze-dried blister packaging uses PVC/PCTFE/aluminium laminates with moisture vapour transmission rate below 0.05 g/m²/day to prevent moisture ingress and polymorph conversion. Polymorph conversion risk is controlled by maintaining process RH below 60% and product moisture below 2.0%; if the anhydrous form is used, contact with aqueous binder solutions can cause conversion to monohydrate, which changes dissolution behaviour and requires revalidation. Terminal strengths are 5 mg, 10 mg, 15 mg, 20 mg, and 30 mg.
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Aripiprazole Pharma Grade API for tablet, capsule, granule, and oral or injectable finished dosage forms is supplied under manufacturer lot designation APZ-PH-GMP as a white to off-white crystalline powder with CAS 129722-12-9, molecular formula C23H27Cl2N3O2, and molecular mass 448.39 g/mol. The current USP and Ph.Eur monographs define the baseline release tests. Assay by HPLC is fixed at 98.0% to 102.0% on the dried basis. Total related substances are limited to not more than 0.5%, and unspecified impurities to not more than 0.10%. Residual solvents are controlled under USP <467> Option 1; water content by Ph.Eur 2.5.12 is not more than 0.5%; residue on ignition is not more than 0.1%. Elemental impurities follow ICH Q3D with USP <232>/<233> as the analytical platform. Polymorphic identity is verified by XRPD against a supplier-held reference diffractogram. The API is produced under ICH Q7 conditions with a Type II US FDA drug master file and a European CEP maintained. For injectable grades, bacterial endotoxins are tested by Ph.Eur 2.6.14 and bioburden by membrane filtration; the limits are derived from the intended dose and route.
The API is released in non-micronized, micronized, and injectable suspension grades. Non-micronized material is used where dissolution is not the limiting step, such as acidified short-acting intramuscular solutions. Micronized material is intended for direct compression, capsule blending, and granulation where dissolution rate depends on surface area. The injectable suspension grade is controlled for wet-media milling and aseptic fill-finish. Bulk packaging uses low-density polyethylene double liners in aluminium-foil or fibre drums; storage is below 25 °C and 50% relative humidity. Open handling at relative humidity above 60% is not recommended for micronized grade because increased surface area accelerates moisture uptake.
The most common residual solvents in aripiprazole synthesis are dichloromethane, methanol, acetone, and isopropyl alcohol. The supplier release specification under USP <467> Option 1 ensures class 1 solvents are absent, class 2 solvents are below permitted daily exposure, and class 3 solvents are below 5000 ppm. Batch-to-batch variation in solvent residues is controlled by gas chromatography with headspace sampling, which prevents solvent-related tablet friability or injectable vehicle incompatibility.
| Quality attribute | Oral and granule grade | Injectable grade | Method/standard |
|---|---|---|---|
| Appearance | White to off-white crystalline powder | Ph.Eur 2.2.1/2.2.2 | |
| Assay by HPLC | 98.0–102.0% dried basis | USP monograph | |
| Total related substances | Not more than 0.5% | HPLC area normalisation | |
| Unspecified impurity | Not more than 0.10% | HPLC area normalisation | |
| Water content | Not more than 0.5% | Ph.Eur 2.5.12 | |
| Residue on ignition | Not more than 0.1% | Ph.Eur 2.4.14 | |
| Residual solvents | USP <467> Option 1 | GC headspace | |
| Elemental impurities | ICH Q3D Options 1 and 2 | USP <232>/<233> | |
| Polymorph | Supplier reference diffractogram | XRPD | |
| Bacterial endotoxins | Not specified | Lot-specific limit, e.g. not more than 0.25 EU/mg | Ph.Eur 2.6.14 |
| Bioburden | Not specified | Not more than 100 CFU/g | Membrane filtration |
| Particle size | Supplier CoA by laser diffraction | Malvern Mastersizer 3000 | |
Micronized aripiprazole is generated by air-jet milling or fluidized-bed opposed-jet milling with classifier control; the resulting specific surface area is raised from less than 1 m²/g in non-micronized grade to typically 3–10 m²/g in micronized grade as measured by nitrogen adsorption according to Ph.Eur 2.9.26. The increase in surface energy alters powder flow and die fill. Non-micronized grade has Carr index values below 20% and is manageable in gravity-fed tablet presses, whereas micronized grade often exceeds 35% in Carr index and requires a forced feeder or granulation. The non-micronized fraction is therefore preferred when the API is dissolved before processing; the micronized fraction is used in direct compression or low-shear blending when particle size reduction is critical for dissolution. Because aripiprazole is practically insoluble in water, dissolution rate in pH 1.2 and pH 4.5 media depends strongly on particle surface area; compendial release tests do not set a numeric D90, and the formulation scientist must establish a target and correlate it with dissolution profiling.
On production-scale encapsulators with dosator or tamping pin stations, cohesive micronized API without granulation tends to produce fill weight variability because of inconsistent powder bed density in the hopper. Dry granulation using a roller compactor with roll pressure of 20–60 kN and gap 1.5–3.0 mm, followed by oscillating sieve milling to produce granules with a D50 of 200–500 µm, shifts the powder from a cohesive flow regime to free-flowing granules but may reduce surface area slightly if over-compacted. Over-lubrication with magnesium stearate above 1.0% by weight can produce hydrophobic films over the high-energy API surfaces and reduce dissolution; a lubricant-mixing time study is required.
High-shear wet granulation is commonly used for low-dose aripiprazole tablets, where micronized API is added at 2–10 mg per unit dose. The process is performed in a high-shear mixer with an impeller tip speed of 5–12 m/s and a chopper speed of 1500–3000 rpm; the binder solution, typically povidone K30 at 5% w/v, is added to a predetermined wet mass endpoint. Drying in a fluid-bed dryer at product temperature 50–60 °C is preferred to avoid polymorph conversion and to achieve final granule moisture between 1.0% and 2.0%. Over-granulation increases granule density and reduces tablet porosity, which slows disintegration below the 15 min acceptance threshold of USP <701> in typical tablet formulations. Tablet compression on a rotary press is operated between 10 kN and 25 kN with target hardness of 60–120 N; the exact values depend on tooling size and formulation. Capsule filling of granules is performed on dosator or tamping-pin machines with target fill weight RSD not more than 3.0%.
Granule sachet processing uses the same granulation route but requires final moisture below 2.0% and storage in high-moisture-barrier laminates. Differential scanning calorimetry of the crystalline form shows a melting endotherm near 139 °C, but the exact onset depends on polymorph purity and heating rate. Thermal exposure during drying must remain well below this temperature; hot-melt extrusion is generally not used for aripiprazole solid oral formulations because of thermal and solubility constraints, and published data for this specific configuration is limited.
Injectable-grade aripiprazole is supplied with low bioburden and low endotoxin. For short-acting intramuscular solution, the API is dissolved in an acidified aqueous vehicle; terminal membrane filtration through 0.22 µm sterilizing-grade filters is performed after dissolution. The dissolution step must control pH because the free base has low aqueous solubility at neutral pH and a pKa of approximately 7.6; if the pH drifts above the target range during compounding, reprecipitation can occur and plug sterilizing filters. Particulate matter in the finished drug product is tested according to USP <788> using light obscuration; subvisible particle counts must remain below 6000 particles per container at ≥10 µm and 600 particles per container at ≥25 µm. These limits apply to the finished drug product, not the API, but the API filter-clogging behavior and insoluble particulate burden are critical input attributes.
For long-acting injectable suspension, particle size is controlled by wet-media milling in a recirculating bead mill with yttria-stabilized zirconia beads of 0.3–0.5 mm. The target D50 is typically 2–5 µm and D90 below 20 µm as measured by laser diffraction; published data for this specific configuration is limited, so the target must be linked to syringeability, content uniformity, and release profile. The suspension cannot be terminally sterilized by dry heat or steam because particle aggregation and Ostwald ripening may occur; aseptic manufacturing with USP <71> sterility testing is used. The API is not sterile by default; it is low-bioburden and is processed aseptically or sterilized in the final dosage form. Bacterial endotoxin limits are established according to the K/M calculation in USP <85>, with the final API limit tightened for long-acting high-dose products.
| Dosage form route | Preferred API grade | Representative equipment | Critical API-related failure mode |
|---|---|---|---|
| Tablet direct compression | Micronized | Rotary tablet press with forced feeder | Segregation and weight variation due to cohesive powder |
| Capsule filling | Granulated or dry-compacted | Dosator/tamping-pin encapsulator | Fill weight variation from poor granule flow |
| Granule sachet | Wet-granulated micronized | High-shear mixer and fluid-bed dryer | Over-granulation and slow dissolution |
| Short-acting intramuscular solution | Non-micronized | Stainless steel compounding vessel and sterilizing-grade 0.22 µm membrane filter | Filter clogging from pH shift and reprecipitation |
| Long-acting injectable suspension | Wet-milled injectable grade | Recirculating bead mill and aseptic filling line | Particle aggregation and Ostwald ripening under terminal heat |
Compared with research-grade aripiprazole, the pharma grade is differentiated by residual solvent documentation, elemental impurity controls under ICH Q3D, replicate XRPD polymorphism, and the availability of a Type II US FDA drug master file. Compared with other atypical antipsychotic APIs such as olanzapine, risperidone, or quetiapine, aripiprazole has a distinct receptor binding profile and a different pH-solubility curve; it cannot be substituted on a mass basis in a formulation without redevelopment. Within aripiprazole suppliers, differences in particle geometry, surface energy, trace solvent profile, and polymorphic minor-form content produce measurable differences in blend flow, content uniformity, and dissolution even when compendial release tests are satisfied. The non-micronized and micronized grades therefore require separate validation batches and separate dissolution specifications for each intended dosage form.