| HS Code | 187953 |
| Product Name | Phenobarbital Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable |
| Api Name | Phenobarbital |
| Pharmaceutical Grade | Pharma Grade API |
| Cas Number | 50-06-6 |
| Molecular Formula | C12H12N2O3 |
| Molecular Weight | 232.24 g/mol |
| Iupac Name | 5-ethyl-5-phenyl-1,3-diazinane-2,4,6-trione |
| Synonyms | Phenobarbitone |
| Appearance | White or almost white crystalline powder |
| Assay | 99.0% to 101.0% on dried basis |
| Solubility | Slightly soluble in water; soluble in ethanol, ether, and chloroform |
| Melting Point | 174 to 178 degrees Celsius |
| Pka | 7.4 |
| Logp | 1.47 |
| Dosage Form Suitability | Tablet, capsule, granule, injection |
| Route Of Administration | Oral and injectable |
| Storage Conditions | Store in a tightly closed, light-resistant container at controlled room temperature |
| Packaging | Double polyethylene bags inside fiber drum or as per customer specification |
| Shelf Life | Typically 24 to 60 months depending on packaging and storage conditions |
| Pharmacopoeia Compliance | USP, EP, BP, JP, or specified standard |
| Regulatory Status | Controlled substance; prescription only; subject to applicable narcotic and psychotropic regulations |
As an accredited Phenobarbital 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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Direct compression of phenobarbital Pharma Grade API into uncoated immediate-release tablets is constrained by low-dose content uniformity, particle size distribution, and lubricant sensitivity. The crystalline active substance is de-agglomerated through a conical mill fitted with a 0.50 mm rasping screen, after which the milled fraction is controlled to a typical d50 of 20–40 µm and a d90 not exceeding 100 µm. Blending is performed in a bin blender at 10–12 rpm for 15–20 minutes with microcrystalline cellulose, pregelatinized starch, croscarmellose sodium, and colloidal silicon dioxide. Magnesium stearate is introduced as a final lubricant at 0.5–1.0 wt% and mixed for no more than 3 minutes because extended lubrication creates a hydrophobic film that retards dissolution and increases inter-tablet variability. Blend uniformity testing follows USP <905> with an acceptance value of ≤15 for dosage strengths of 15 mg or 30 mg, while the assayed blend RSD is conventionally maintained below 4.0% before compression. Tablets are compacted on a rotary press equipped with forced feed frames, with target hardness of 6–8 kp and friability not more than 1.0% according to USP <1216>. Dissolution is evaluated under USP <711> using Apparatus 2 at 50 rpm in 900 mL of purified water or dilute hydrochloric acid as designated in the USP Phenobarbital Tablets monograph, with sampling at 30 min, 45 min, and 60 min. This route is unsuitable when ambient humidity exceeds 60% RH without pre-drying because static charge on the micronized particles alters flow and segregation behavior.
Aqueous high-shear granulation becomes necessary when the API particle size is heavily reduced and direct compression no longer provides acceptable flow or blend homogeneity. The barbiturate powder is first mixed with lactose monohydrate and maize starch in a high-shear granulator; a binder solution of povidone K30 at 5% w/w in purified water is metered over 4–6 minutes, with total liquid addition typically reaching 20–25% w/w of the dry charge. The endpoint is determined by impeller power draw and visual mass consistency rather than time alone, because under-granulation produces friable granules, while over-granulation yields dense agglomerates that resist tablet disintegration. Wet mass is transferred to a fluid-bed dryer operating at an inlet air temperature of 60–70 °C and a product temperature ceiling of 45 °C, then dried to a residual moisture content of 1.5–2.5% w/w for tablet compression and 2.5–3.5% w/w for granule sachet filling. Milling through a 1.0 mm screen produces a granule fraction with a d50 of 150–250 µm, which is then blended with extragranular crospovidone and magnesium stearate before compression or sachet fill. Dissolution delay is commonly observed when the granular moisture content falls below 1.5% w/w, because hydrophobic surface domains on the API reduce wetting in aqueous media. If a hydroalcoholic binder solution is substituted for aqueous povidone, residual ethanol must be controlled according to ICH Q3C Option 2 limits for Class 3 solvents, and the drying profile must be extended to avoid solvent pockets that can collapse on compression.
| Critical granule attribute | Tablet compression target | Sachet filling target | Test or equipment basis |
|---|---|---|---|
| Residual moisture | 1.5–2.5% w/w | 2.5–3.5% w/w | Halogen moisture analyzer, USP <731> |
| Granule d50 | 150–250 µm | 180–250 µm | Sieve analysis, laser diffraction |
| Compression hardness | 6–8 kp | Not applicable | Hardness tester, USP <1217> |
| Dissolution acceptance | Meet USP monograph | Disperse in 50 mL water without floating | USP <711>, visual dispersion test |
Low-dose phenobarbital capsules are filled with a pre-blend in which the API is diluted with lactose monohydrate or a co-processed microcrystalline cellulose carrier, then lubricated with magnesium stearate at 0.5–1.0 wt%. Powder stratification is the primary risk during encapsulation because the API has a higher particle density than many common fillers and can migrate toward the bottom of the powder bed under vibration. Weight variation alone is therefore insufficient for dose assurance; filled capsules are assayed by USP <905> with an acceptance value of ≤15 for dosage strengths at or below 30 mg. Dosator-type encapsulators require a bulk density above 0.45 g/mL and a flow function coefficient greater than 4.0 to maintain consistent plug formation, whereas tamping-pin machines tolerate higher fines content but can exacerbate stratification if the dosing disk speed is not controlled. For hydroxypropyl methylcellulose capsule shells, dissolution testing is performed under USP <711> with the USP Phenobarbital Capsules monograph medium; gelatin shells must be protected from high humidity because moisture uptake above 13–14% w/w increases the risk of shell softening and delayed release. Capsule fill weights for a 15 mg dose are normally confined to a range of 120–180 mg, depending on the excipient density and the required volumetric fill, and any change in lactose source requires re-validation of the stratification profile because particle morphology affects segregation kinetics.
Injectable phenobarbital is manufactured as the sodium salt to increase aqueous solubility, and the solution is typically buffered to a pH of 9.0–10.0 because the free acid precipitates when pH drops below the pKa region of approximately 7.3. The formulation is aseptically filtered through a 0.22 µm PVDF sterilizing filter and filled into Type I borosilicate glass vials or ampoules under ISO 14644-1 Class 5 conditions, with nitrogen overlaying used to reduce oxidative headspace degradation. Terminal steam sterilization at 121 °C for 15 minutes is not always feasible for every solvent and closure system, because the combination of propylene glycol, water, and elastomeric closures can produce pH drift or extractables that compromise free-acid solubility and closure integrity. Aseptic processing therefore remains the dominant strategy for this molecule when the solvent matrix is non-aqueous or when ampoule headspace prevents uniform steam penetration. Release testing must include sterility per USP <71>, bacterial endotoxins per USP <85>, particulate matter per USP <788>, and container closure integrity per USP <660>. pH, assay, related substances, and visible particulate matter are monitored across the shelf life because phenobarbital sodium in solution is susceptible to hydrolytic degradation when exposed to heat and free water.
| Test attribute | Acceptance criterion or limit | Standard basis |
|---|---|---|
| Sterility | No growth after 14 days | USP <71> |
| Bacterial endotoxins | Not more than 0.5 EU/mg or product-specific monograph | USP <85> |
| Subvisible particulates ≥ 10 µm | Not more than 6000 per container | USP <788> |
| Subvisible particulates ≥ 25 µm | Not more than 600 per container | USP <788> |
| Container closure integrity | No microbial ingress or dye penetration | USP <660>, USP <1207> |
Extemporaneous oral suspension preparation in hospital pharmacies uses phenobarbital API as a fine powder that is first levigated with glycerin or propylene glycol before incorporation into a preserved aqueous vehicle. Because the free acid is hydrophobic and wets poorly in water alone, direct addition to simple syrup produces floating aggregates and dose inaccuracy. The compounding procedure therefore wets the powder with a small volume of glycerin at a ratio of 1:1 to 1:2, then gradually incorporates a vehicle containing sodium carboxymethyl cellulose or sorbitol. The suspension is packaged in amber polyethylene terephthalate containers and stored at 2–8 °C; under USP <795>, the beyond-use date for a preserved water-containing oral liquid is not more than 14 days when refrigerated. pH adjustment with citric acid or sodium citrate is avoided unless a stability study demonstrates that free-acid precipitation risk remains acceptable, because a shift below pH 8.0 can reduce solubility and change sedimentation behavior. Shaking before each dose is required, and the dose withdrawn must be measured with a calibrated oral syringe rather than a household spoon to maintain dose accuracy within ±10% of the labelled amount.
Granule-based sachet presentations are manufactured for patients who cannot swallow tablets or capsules and require dose titration in small increments. The granulation process is adjusted so that the final milled fraction has a d50 of 180–250 µm, because coarser granules remain undispersed in soft food, while finer granules become hygroscopic and sticky during sachet filling. Sachet fill weights for phenobarbital doses of 10 mg or 15 mg are typically kept above 200 mg to allow accurate volumetric dosing and to reduce relative error from weighing tolerances. Each sachet is filled under controlled humidity not exceeding 40% RH, and the package laminate must provide a moisture vapor transmission rate below 0.1 g/m²/day to prevent granule agglomeration. Content uniformity is verified by USP <905> on the filled sachets, while the dispersed granule formulation is tested for pH, sedimentation volume, and redispersibility after storage. When the granules are intended to be sprinkled onto acidic soft food, dissolution testing is performed in 0.1 N hydrochloric acid at 37 ± 0.5 °C using USP <711> Apparatus 2 to confirm that the release rate is not adversely altered by food-related pH. The granule route also avoids the high osmolality burden seen with some oral liquid vehicles, but it is not appropriate for patients with acute seizure emergencies because release from the granule matrix is not sufficiently rapid to replace parenteral therapy.
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Phenobarbital Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable is the free acid form of 5-ethyl-5-phenylpyrimidine-2,4,6(1H,3H,5H)-trione, CAS 50-06-6, molecular formula C12H12N2O3, relative molecular mass 232.24 g mol-1. The product descriptor functions as the model identifier and specifies a compendial-grade active pharmaceutical ingredient supplied as a white or almost white crystalline powder for solid oral dosage forms and, when supported by route-specific endotoxin, particulate matter, sterility, and stability data, sterile injectable presentations. It is not interchangeable with reagent-grade phenobarbital, technical intermediates, or the sodium salt derivative, because those products lack the full pharmacopeial release specification, residual solvent control, elemental impurity limits, controlled particle-size distribution, and GMP documentation required for pharmaceutical manufacturing.
The API is manufactured and released under GMP expectations established in 21 CFR 210, 21 CFR 211, and ICH Q7. The certificate of analysis includes lot-specific values for assay, related substances, loss on drying, residue on ignition, elemental impurities, residual solvents, particle size, and microbial quality. The grade designation does not assign a proprietary model number; the supplier’s certificate of analysis defines the release version by compendial monograph, edition, and intended route of administration. Because the product descriptor includes tablet, capsule, granule, injection, oral, and injectable uses, the release specification for a given lot must be selected by the most stringent route unless the receiving manufacturer verifies all parameters.
Release against the current USP/NF and Ph. Eur. Phenobarbital monographs requires conformance to identity, assay, melting range, loss on drying, residue on ignition, related substances, and residual solvent standards. The assay range and drying limits are harmonized across many pharmacopeial regions, but residual solvent and impurity acceptance criteria can differ by monograph edition. Elemental impurities are controlled under ICH Q3D and USP 232/USP 233; microbial quality for nonsterile oral applications is controlled under USP 61 and USP 62.
| Quality attribute | Acceptance criterion or control | Reference |
|---|---|---|
| Appearance | White or almost white crystalline powder | USP/NF, Ph. Eur. visual examination |
| Identification | IR absorption spectrum conforms to reference; retention time matches standard | USP 197, Ph. Eur. 2.2.24 |
| Assay | 98.0–101.0% C12H12N2O3 on dried basis | USP/NF Phenobarbital monograph titration |
| Melting range | 174–178 °C | USP 741 |
| Loss on drying | ≤0.5% | USP 731, 105 °C for 2 h |
| Residue on ignition | ≤0.1% | USP 281 |
| Elemental impurities | Class-based limits by route and allowed daily exposure | USP 232, USP 233, ICH Q3D |
| Residual solvents | ICH Q3C category limits | USP 467, Ph. Eur. 2.4.24 |
| Related substances | Individual and total impurities per current monograph | Ph. Eur. 2.2.29, USP 621 |
| Microbial quality, nonsterile oral | TAMC ≤103 CFU/g, TYMC ≤102 CFU/g, absence of Escherichia coli | USP 61, USP 62 |
Because the product descriptor includes multiple routes, a single API lot can be used for both oral solid and injectable processing only when the manufacturer has verified injectable-specific controls. Blending, sampling, and environmental controls in the API facility must prevent endotoxin introduction. For injectable applications, the absence of a bacterial endotoxin result from the supplier is not affirmative evidence of suitability; the finished product manufacturer must establish a route-appropriate endotoxin limit under USP 85 and validate the depyrogenation and sterile processing train.
Direct compression performance of the free acid form is governed by particle-size distribution, bulk density, tapped density, and the derived compressibility index and Hausner ratio under USP 1174. A compressibility index below 25% is classified as passable and is normally needed to maintain weight uniformity on rotary tablet presses with forced feeders. Above 30%, flow is classified as poor, and bridge or rathole formation can occur in transfer hoppers and bin blenders. Production-scale batch records for brittle, low-moisture APIs show that capping and lamination are commonly attributed to excessive fines or insufficient precompression; the specific compression force threshold is formulation-dependent and must be established during process development. Where the API lot has a high fines fraction, blending time is restricted to prevent over-blending and demixing. In bin blenders of 600 L to 1200 L working capacity, baffle geometry, fill level, and transfer-line free-fall distance are adjusted to maintain blend uniformity.
Granulation is used when direct compression is not feasible. In wet granulation, the free acid API is pre-blended with microcrystalline cellulose and crospovidone before addition of a povidone solution in a high-shear granulator. Granulation endpoint is controlled by impeller power consumption and torque; fluid-bed drying is performed at inlet air temperatures supported by ICH Q1A stability data to limit hydrolytic degradation. High-shear granulation with sodium bicarbonate, sodium carbonate, or other alkaline agents should be avoided because ionization of the free acid can alter granule dissolution, compressibility, and tablet hardness. Dry milling after granulation is controlled by laser diffraction under USP 429; D10, D50, and D90 values are reported in the certificate of analysis or development report when a specific particle-size distribution is required for content uniformity or dissolution control.
For injectable presentations, the API must meet bacterial endotoxin limits defined by dose, route, and the administered volume under USP 85. Particulate matter in the final product is controlled under USP 788 for subvisible particles, and sterility of the finished product is demonstrated by USP 71. The manufacturing process uses a sterility assurance level of 10-6. For a free acid API with very slight aqueous solubility, the injectable formulation is prepared by pH adjustment to form the sodium salt in situ or by use of a non-aqueous vehicle. pH measurement follows USP 791; the target pH is established by solubility and stability studies. Sterile filtration through a 0.22 µm membrane is common for formulations that are not suitable for terminal steam sterilization. Aseptic filling is conducted in a ISO 14644-1 Class 5 environment with Grade A conditions under EudraLex Volume 4 Annex 1. Autoclave cycles may be considered only where thermal stability data demonstrate absence of impurity increase and pH drift.
Endotoxin control in the API synthesis requires depyrogenated equipment, water-for-injection rinses for product-contact surfaces, and controlled bioburden before crystallization. The oral solid grade is not automatically acceptable for injection merely because the same chemical entity and assay are present; the supplier and receiving manufacturer must define separate acceptance criteria for endotoxin, bioburden, extraneous particles, and container-closure residues. Published development reports for phenobarbital free acid in terminal sterilization of aqueous injection vehicles are limited; therefore, terminal sterilization of the specific formulation cannot be assumed and must be validated experimentally.
| Parameter | Oral solid application | Injectable application | Standards |
|---|---|---|---|
| Bacterial endotoxins | Not routinely tested unless specified by the dosage form | Limit established by dose; product must meet endotoxin acceptance criterion | USP 85 |
| Particulate matter | Controlled through blending and subsequent de-lumping; not typical for bulk oral API | Final product meets subvisible particle counts for small-volume injection | USP 788 |
| Sterility | Not required | Mandatory finished product test | USP 71 |
| Particle-size control | Flow, compression, and content uniformity focus | Dissolution, syringeability, and filterability focus | USP 429, USP 1174 |
| Residual solvents | ICH Q3C limits | ICH Q3C limits with sterile processing constraints | USP 467 |
| Elemental impurities | ICH Q3D oral permitted daily exposure | ICH Q3D parenteral permitted daily exposure | USP 232, USP 233 |
Residual solvent control is governed by ICH Q3C and USP 467. Class 1 solvents are controlled at levels such as benzene 2 ppm, carbon tetrachloride 4 ppm, and 1,2-dichloroethane 5 ppm. Class 2 solvents are limited according to the permitted daily exposure, and Class 3 solvents are controlled to general limits appropriate to the manufacturing route. The API should not be stored or processed near strong oxidizers, strong acids, or strong bases; alkaline hydrolysis of the barbituric acid ring may occur at high pH and generate degradation products that alter assay and related substance profiles. Storage in tight, light-resistant containers at controlled room temperature 20–25 °C with USP 659 allowances for excursions to 15–30 °C is required. Moisture exposure from condensation or prolonged open handling changes powder flow and can reduce blend uniformity in solid dosage processing.
Phenobarbital is controlled under the US Controlled Substances Act Schedule IV and the Single Convention on Psychotropic Substances Schedule IV. Imports, exports, storage, distribution, and recordkeeping require security controls and documentation under 21 CFR 1304, 21 CFR 1305, and 21 CFR 1312. These regulatory requirements are independent of pharmacopeial quality and must be included in site master files and supplier quality agreements. The API should be handled only by qualified personnel under controlled substance procedures; inventory reconciliation and periodic stock audits are part of GMP and controlled substance compliance.
Differences from other products are route-dependent and chemical-form-dependent. Phenobarbital sodium, CAS 57-30-7, is the water-soluble salt used for aqueous injections and oral solutions. The free acid product is not directly interchangeable with the sodium salt on a weight basis because the salt form has a different relative molecular mass, dissolution rate, hygroscopicity, and particle-size behavior. Reagent-grade phenobarbital may be supplied without GMP release, without full related-substance testing, and with higher heavy metal content; it is unsuitable for pharmaceutical manufacturing. Technical intermediates may contain process impurities not controlled by a pharmacopeial monograph. The descriptor Phenobarbital Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable therefore identifies a controlled, compendial-grade free acid with multi-route potential. It does not guarantee that every lot is automatically suitable for every route; the receiving manufacturer must verify route-specific attributes and validate each finished dosage form.
On production-scale rotary tablet presses, capping and lamination have been observed when poor powder compressibility is combined with inadequate precompression; this is a common failure mode for brittle, low-moisture APIs with compressibility index above 30%. Batch-to-batch variability in particle-size distribution after milling can shift fill volume in dosator capsule machines, so supplier certificates of analysis should include D10, D50, and D90 values by laser diffraction under USP 429. High-shear granulation with alkaline binders should be avoided because conversion of part of the free acid to the sodium salt alters dissolution, compactibility, and granule hardness. These processing boundaries define the practical limits of the product across tablet, capsule, granule, and injection applications and must be controlled through supplier quality agreements, route-specific release, and process validation rather than assumed from the API grade designation alone.