| HS Code | 902294 |
| Product Name | Pharmacel 112 Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable |
| Brand | Pharmacel |
| Grade | 112 |
| Manufacturer | DFE Pharma |
| Product Type | Pharmaceutical excipient / pharma grade microcrystalline cellulose |
| Chemical Name | Microcrystalline cellulose |
| Cas Number | 9004-34-6 |
| Einecs Number | 232-674-9 |
| Molecular Formula | (C6H10O5)n |
| Molecular Weight | Variable, typically about 36,000 Da |
| Appearance | White to off-white, odorless, tasteless, fine crystalline powder |
| Particle Size | Nominal mean particle size approximately 100 µm |
| Moisture Content | ≤1.5% (low moisture grade) |
| Loss On Drying | ≤1.5% |
| Bulk Density | 0.28–0.33 g/cm³ |
| Tapped Density | 0.35–0.45 g/cm³ |
| Ph | 5.0–7.5 (10% aqueous suspension) |
| Solubility | Insoluble in water, ethanol, and ether |
| Water Soluble Substances | ≤0.25% |
| Residue On Ignition | ≤0.05% |
| Pharmacopoeia Compliance | USP/NF, Ph. Eur., JP |
| Functional Category | Binder, diluent, disintegrant, compression aid |
| Dosage Forms | Tablet, capsule, granule, injection, oral, injectable |
| Route Of Administration | Oral and injectable |
| Storage Conditions | Store in a cool, dry, well-ventilated area; protect from moisture |
| Shelf Life | Typically 24–36 months when stored properly |
| Packaging | 25 kg paper bags or fiber drums with inner polyethylene liner |
As an accredited Pharmacel 112 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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Dosator-based capsule filling machines require powder bed uniformity and bulk density stability to achieve fill weight coefficient of variation below 3.0% at production speeds exceeding 100,000 capsules per hour. The addition ratio for API in the final encapsulated powder blend typically falls between 1% w/w and 40% w/w, with the remainder composed of diluents, disintegrants, and lubricants. Pre-encapsulation processing includes sieving through a 500–1000 µm mesh, blending in a diffusion mixer, and lubrication with 0.25–0.75% w/w magnesium stearate. Powder flow is characterized by USP <1174> compressibility index, with acceptable Carr index between 15–25 and flow rate above 10 g/s through a 15 mm orifice. Dosator pin compression ratio is adjusted to 2.0:1 to 3.5:1 based on bulk density, which should remain between 0.30 g/mL and 0.80 g/mL. Ambient humidity above 60% RH increases API moisture uptake and static charge, causing powder bridging in hoppers and fill weight drift. Terminal product type is a hard gelatin or HPMC capsule for oral administration. Compliance standards include USP <905> for capsule weight variation, USP <711> for dissolution release, and ICH Q3C(R8) for residual solvent limits. Published data for Pharmacel 112 capsule fill weight parameters is limited; the values cited represent typical bounds for directly compressible APIs with similar particle size and flow characteristics.
During high-shear wet granulation of oral solid dosage forms, impeller and chopper action densifies API with binder solution until a target granule size distribution is achieved, typically 0.125–0.5 mm after milling. The addition ratio for the active ingredient in wet granulation feed ranges from 1% w/w to 30% w/w, with binder such as povidone or hydroxypropyl cellulose added at 2–5% w/w relative to dry powder mass. Endpoint determination is performed by monitoring impeller torque or power consumption; over-granulation occurs when wet mass moisture exceeds 20% w/w, leading to densified granules with prolonged dissolution, while under-granulation below 10% w/w moisture yields friable granules and tablet capping. Scale-up from laboratory to production granulators requires maintaining constant impeller tip speed between 5 m/s and 20 m/s to replicate endpoint torque. Drying is carried out in a fluid bed dryer with inlet air temperature of 50–70°C until loss on drying is below 2–5% w/w, followed by milling through a 1.0–1.6 mm screen. Terminal product type is a film-coated tablet or granule for reconstitution or encapsulation. Compliance standards include USP <786> for sieve analysis, USP <711> for dissolution, and ICH Q3C(R8) for residual organic solvents. Published data for Pharmacel 112 wet granulation endpoint parameters is limited; the cited ranges reflect general pharmaceutical wet granulation practice.
When moisture-sensitive APIs are processed without aqueous granulation, roller compaction densifies dry blends through counter-rotating rollers, with roll pressure maintained between 2 kN/cm and 10 kN/cm and roll speed between 2 rpm and 10 rpm to produce ribbons of 0.8–1.2 g/cm³ density. The addition ratio for the active ingredient in roller compaction feed is typically 10% w/w to 50% w/w, with the remainder composed of filler, disintegrant, and dry binder. After compaction, ribbons are milled through an oscillating granulator equipped with 1.0–2.0 mm screens, and the resulting granules are lubricated with 0.25–1.0% w/w magnesium stearate before compression or encapsulation. Ribbon density is monitored by USP <616> tapped density method, with target granule porosity between 10% and 25% to ensure sufficient compressibility during tablet formation. Process bottlenecks include ribbon sticking to roll surfaces when API exhibits high hygroscopicity at relative humidity above 60%, requiring pre-drying of the blend. Terminal product type is a tablet or capsule for oral administration. Compliance standards include USP <1174> for powder flow, USP <616> for bulk density, and ASTM E2500-20 for equipment qualification. Published data for Pharmacel 112 roller compaction behavior is limited; the cited parameter ranges reflect typical dry granulation processing for APIs with similar moisture sensitivity.Parenteral dosage form manufacturing for lyophilized injectable products requires API dissolved in water for injection at concentrations from 0.1 mg/mL to 100 mg/mL, with pH adjusted using 0.1 N hydrochloric acid or sodium hydroxide to maintain stability within the range specified by ICH Q6A accelerated stability data. Sterile filtration through a 0.22 µm polyvinylidene fluoride or polyethersulfone membrane is validated by ASTM F838-20 bacterial retention testing, and filtrate is aseptically filled into Type I glass vials within ISO 14644-1:2015 Class 5 laminar airflow. Lyophilization cycle parameters include freezing at shelf temperature of -40°C to -50°C for 2–4 hours, primary drying at shelf temperature -20°C to -30°C under vacuum of 50–150 mTorr for 24–48 hours, and secondary drying at 20–30°C for 4–12 hours until residual moisture is below 1–3% w/w. For ready-to-use injectable solutions, osmolality is adjusted to 280–320 mOsm/kg with sodium chloride or dextrose per USP <785>. Terminal product type is a lyophilized powder for reconstitution with sterile diluent or a ready-to-use injectable solution. Compliance standards include USP <1> for injections, USP <71> for sterility tests, USP <85> for bacterial endotoxins, and USP <788> for particulate matter. Published data for Pharmacel 112 lyophilization behavior is limited; the cited cycle parameters represent typical freeze-drying conditions for small-molecule injectable APIs.
| Application Context | Standard Code | Test Designation | Critical Parameter |
|---|---|---|---|
| Direct compression tablet | USP <905> | Uniformity of Dosage Units | Acceptance value ≤ 15 |
| Direct compression tablet | USP <1062> | Tablet Compression Characterization | Compaction force vs. hardness |
| Capsule filling | USP <1174> | Powder Flow | Carr index 15–25 |
| Capsule filling | USP <711> | Dissolution | Release at 30–60 min |
| Wet granulation | USP <786> | Analytical Sieving | Granule size 0.125–0.5 mm |
| Wet granulation | USP <711> | Dissolution | Release profile vs. formulation |
| Dry granulation | USP <616> | Bulk Density | 0.30–0.80 g/mL |
| Dry granulation | USP <1174> | Powder Flow | Flow rate > 10 g/s |
| Lyophilized injectable | USP <71> | Sterility Tests | No growth in 14 days |
| Lyophilized injectable | USP <85> | Bacterial Endotoxins | ≤ 5 EU/kg for parenteral |
| Lyophilized injectable | USP <788> | Particulate Matter | ≥ 10 µm: ≤ 25 per container; ≥ 25 µm: ≤ 3 per container |
| Sustained-release matrix tablet | USP <711> | Dissolution | Apparatus 2, 50–100 rpm |
In hydrophilic matrix tablet manufacturing, sustained-release oral matrix tablets are combined with hypromellose at polymer ratios from 10% w/w to 40% w/w, where API loading above 30% w/w reduces matrix gel integrity and accelerates drug release beyond the intended 12–24 hour profile. The addition ratio for the active ingredient in hydrophilic matrix formulations is typically 5% w/w to 50% w/w, with polymer grade selection based on viscosity from 100 mPa·s to 100,000 mPa·s as measured by USP <911> viscosity method. Processing involves dry blending of API, polymer, and filler, followed by lubrication with 0.5–1.0% w/w magnesium stearate and direct compression on a rotary press with main compression force adjusted to achieve tablet hardness of 80–150 N. Terminal product type is an oral sustained-release tablet intended for once-daily or twice-daily administration. Compliance standards include USP <711> for dissolution with Apparatus 2 at 50–100 rpm, USP <905> for content uniformity, and ICH Q3D(R2) for elemental impurities. Published data for Pharmacel 112 sustained-release matrix performance is limited; the cited ranges reflect typical hydrophilic matrix formulation practice.
| Application Context | API Addition Ratio | Primary Equipment | Terminal Product Type |
|---|---|---|---|
| Direct compression | 0.5–50% w/w | Rotary tablet press, bin blender | Immediate-release tablet |
| Capsule filling | 1–40% w/w | Dosator capsule machine, diffusion mixer | Hard gelatin or HPMC capsule |
| Wet granulation | 1–30% w/w | High-shear granulator, fluid bed dryer | Film-coated tablet or granule |
| Dry granulation | 10–50% w/w | Roller compactor, oscillating granulator | Tablet or capsule |
| Lyophilized injectable | 0.1–100 mg/mL | Lyophilizer, aseptic filling line | Lyophilized powder for injection |
| Sustained-release matrix | 5–50% w/w | Rotary tablet press, diffusion mixer | Sustained-release tablet |
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Pharmacel 112 is a spray-dried microcrystalline cellulose grade distributed under the product descriptor “Pharmacel 112 Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable.” The descriptor is a trade-level designation; in formulation practice the material functions as a compendial filler-binder-disintegrant rather than an active pharmacological ingredient. The substance is produced by controlled acid hydrolysis of purified α-cellulose pulp, followed by neutralization, washing, mechanical attrition, and spray drying. The manufacturing route generates low-moisture, porous, largely spherical particles with a nominal mean particle size of 100 µm as determined by laser diffraction under Ph. Eur. 2.9.31 / USP <429>. The product meets the current microcrystalline cellulose monographs of USP-NF, Ph. Eur., and JP.
The grade is differentiated from general-purpose microcrystalline cellulose by a supplier-tightened loss-on-drying limit of ≤ 3.0%, compared with the compendial limit of ≤ 5.0%. That reduction in moisture is the principal reason the grade is specified for moisture-sensitive active pharmaceutical ingredients. The degree of polymerization is controlled to not more than 350. The pH of an aqueous dispersion is 5.0–7.0 when measured by Ph. Eur. 2.2.3 / USP <791>. Residue on ignition is ≤ 0.1% by Ph. Eur. 2.4.16 / USP <281>. Conductivity is ≤ 75 µS/cm by Ph. Eur. 2.2.38 / USP <645>. The typical bulk density is 0.30–0.34 g/cm³ by Ph. Eur. 2.9.34 / USP <616>. These properties are relevant to both solid oral dosage forms and injectable suspensions because they define the material’s purity, ionic load, and water content before processing.
| Parameter | Method | Pharmacel 112 Acceptance or Typical Value |
|---|---|---|
| Identification by infrared absorption | Ph. Eur. 2.2.24 / USP <197> | Positive |
| Loss on drying | Ph. Eur. 2.2.32 / USP <731> | ≤ 3.0% |
| Residue on ignition | Ph. Eur. 2.4.16 / USP <281> | ≤ 0.1% |
| pH of aqueous dispersion | Ph. Eur. 2.2.3 / USP <791> | 5.0–7.0 |
| Conductivity | Ph. Eur. 2.2.38 / USP <645> | ≤ 75 µS/cm |
| Degree of polymerization | Compendial monograph | ≤ 350 |
| Mean particle size D50 | Ph. Eur. 2.9.31 / USP <429> | 100 µm nominal |
| Bulk density | Ph. Eur. 2.9.34 / USP <616> | 0.30–0.34 g/cm³ typical |
Regulatory filings should identify the material by its compendial monograph and manufacturer. The FDA Inactive Ingredient Database lists microcrystalline cellulose for oral and injectable routes, but route-specific maximum potency levels must be checked for the intended dosage form because the injection route has more restrictive limits. The product is not an active pharmaceutical ingredient; it is a pharmacopoeial excipient used to build the tablet, capsule, granule, or injectable suspension matrix.
In direct compression, the material is blended with an active and lubricant and fed through a rotary tablet press. The combination of porous particle morphology and plastic deformation under pressure contributes to compact formation at applied forces commonly used on production machines. On a 16-station rotary press, compression forces between 5 kN and 25 kN typically produce tablets with acceptable hardness, but the exact force depends on active load and punch geometry. Published data for this specific configuration is limited. The material is not brittle in the manner of lactose monohydrate; it consolidates by plastic flow, which reduces capping tendency but increases ejection force if lubricant levels are too low. Magnesium stearate at 0.25–1.0 wt% is commonly used. Mixing with hydrophobic lubricants beyond 5 min may reduce tablet tensile strength because the lubricant coats the plastic-deforming surfaces.
Flow into the die is influenced by the particle size. A D50 of 100 µm offers lower surface area and better flow than a 50 µm grade, but less flow than an 180 µm grade. In direct compression, segregation of active particles should be monitored when the active particle size differs greatly from the microcrystalline cellulose. For low-dose products, geometric blending or pre-milling may be required. The material’s bulk density of 0.30–0.34 g/cm³ supports consistent die fill, but head height and feed-frame speed must be optimized to avoid overdosing in deep fill cams.
For capsule filling on dosator or tamping-pin machines, the low-moisture grade reduces wetting of the powder bed and may improve lubrication of the dosator. However, static charge can increase at very low relative humidity below 20%. Adjustment of filling machine humidity to 40–60% RH is a typical control. The powder should not be exposed to conditions above 60% RH; moisture gain will raise the loss on drying and reduce the low-moisture benefit. Loss on drying should be verified by Ph. Eur. 2.2.32 / USP <731> before and after holding steps.
Wet granulation with Pharmacel 112 requires a liquid addition endpoint established by torque or power draw rather than fixed water addition, because the same powder lot may show small shifts in water absorption. In a high-shear mixer, purified water or an aqueous binder solution is added until the wet mass reaches a plastic, cohesive state. A typical water range is 25–35 wt% of the dry mix for microcrystalline cellulose-based formulations, but published data for this specific configuration is limited. Overgranulation leads to hard granules that resist compression and can produce capping; undergranulation produces weak, friable granules that segregate on the press. The granule is then dried in a fluid-bed dryer at inlet air temperature 40–60 °C to a target loss on drying of 1.5–3.0%. Drying above 60 °C is not necessary for this grade and may overdry the granule, increasing electrostatic charging and reducing compactibility. After drying, the granules are passed through a 0.8–1.2 mm screen. The D50 of the milled granule is typically larger than the starting material, so final blend flow and compression behavior must be re-evaluated.
Dry granulation by roller compaction is also feasible. The material may be compacted into ribbons at roll pressures from 3–8 MPa and milled to granules. The low-moisture characteristic is an advantage when the active is sensitive to hydrolysis; no aqueous binder is introduced. Ribbon density and granule porosity must be controlled because overcompaction reduces the remaining binding capacity of the granules. Published data for this specific configuration is limited.
Injectable suspension processing imposes additional requirements. The material is not suitable for intravenous administration unless a specific finished-product safety case has been validated; particulate cellulose can pose an embolic hazard by the intravenous route. For intramuscular or subcutaneous suspension formulations, it may serve as a suspending agent and viscosity modifier. Batch release should include bacterial endotoxin testing by Ph. Eur. 2.6.14 / USP <85>. The finished product must meet its specific bacterial endotoxin limit and sterility standard. Terminal sterilization by moist heat at 121 °C for 15 min may be applied, but the effect on suspension viscosity, particle aggregation, and resuspendability must be evaluated. The particle size distribution of the injectable suspension should be controlled by the finished-product specification; the excipient D50 of 100 µm may require milling or homogenization if smaller particle size is needed for syringeability through fine needles. Published data for this specific configuration is limited.
Pharmacel 112 differs from the 50 µm grade primarily in particle size. The smaller grade has higher specific surface area and can produce higher compact hardness at equivalent compression force, but it exhibits poorer flow and greater dusting. Pharmacel 112 is therefore selected when direct compression or capsule filling requires adequate flow without the need for wet granulation. Compared with a standard 100 µm grade, the main difference is the tighter moisture limit of ≤ 3.0%. The standard grade is acceptable for many formulations, but the low-moisture variant is intended for actives that degrade by hydrolysis or interact with water. The coarse 180 µm grade provides better flow but lower compactibility; it may not be appropriate for low-dose blends because segregation risk increases with larger particle size. The following table summarizes the practical differences.
| Grade | Nominal D50 | Moisture Limit | Primary Differentiation |
|---|---|---|---|
| Pharmacel 101 | 50 µm | ≤ 5.0% | Higher surface area, higher compactibility, lower flow |
| Pharmacel 102 | 100 µm | ≤ 5.0% | General-purpose direct compression |
| Pharmacel 112 | 100 µm | ≤ 3.0% | Low-moisture, moisture-sensitive actives |
| Pharmacel 200 | 180 µm | ≤ 5.0% | High flow, lower compactibility |
These comparisons are based on nominal supplier data; lot-to-lot variation requires verification against current technical datasheets. Compared with lactose monohydrate, Pharmacel 112 provides plastic deformation and partial disintegration, whereas lactose is brittle and water-soluble; this changes the disintegration mechanism. Compared with dibasic calcium phosphate dihydrate, microcrystalline cellulose has lower density and better compactibility but can retain moisture. Selection among these fillers is governed by active stability, flow, compaction profile, and disintegration requirements.
Substitution should not be treated as a simple drop-in. The reduced initial moisture of ≤ 3.0% lowers the water load entering the formulation, but it does not remove the need for environmental control. If the powder is held in open containers at relative humidity above 60%, moisture uptake can occur within hours and erode the advantage. Pre-drying in a fluid-bed dryer at 40–50 °C until loss on drying is below 3.0% is recommended before direct compression of moisture-sensitive actives. The formulation pH should remain within 5.0–7.0; strongly acidic or alkaline conditions can depolymerize cellulose and alter the degree of polymerization. Oxidation by strong oxidizing agents should also be avoided because it can reduce molecular weight and change compressibility. The substitution from standard MCC to Pharmacel 112 may require adjustment of lubricant concentration and compression force, because lower residual water reduces the plasticizing effect of moisture and can slightly reduce compactibility. Tablet hardness, friability per USP <1216> or Ph. Eur. 2.9.7, and disintegration time per USP <701> / Ph. Eur. 2.9.1 should be re-qualified after substitution.
In capsule products, moisture-sensitive actives in the same formulation may be protected by the low-moisture excipient, but desiccant requirements in the final pack should be determined by stability studies under ICH Q1A conditions. The low-moisture grade does not eliminate the need for barrier packaging; it reduces the water contribution from the excipient fraction only. Published data for this specific configuration is limited.