| HS Code | 537094 |
| Product Name | Mannogem XL Mannitol |
| Brand Name | Mannogem XL |
| Manufacturer | SPI Pharma |
| Chemical Name | D-Mannitol |
| Synonyms | Mannite; D-Mannite |
| Cas Number | 69-65-8 |
| Einecs Number | 200-711-9 |
| Molecular Formula | C6H14O6 |
| Molecular Weight | 182.17 g/mol |
| Grade | Pharma Grade API |
| Pharmacopoeia Compliance | USP/NF, EP, JP, BP |
| Appearance | White crystalline powder |
| Assay | 98.0% to 102.0% (dried basis) |
| Melting Point | 166°C to 170°C |
| Solubility | Freely soluble in water; practically insoluble in ethanol and ether |
| Water Content | ≤0.5% |
| Ph | 5.0 to 8.0 (10% solution) |
| Heavy Metals | ≤10 ppm |
| Residue On Ignition | ≤0.1% |
| Specific Rotation | +23° to +25° |
| Endotoxin | ≤0.04 EU/mg |
| Bioburden | ≤100 CFU/g |
| Route Of Administration | Oral and Injectable |
| Dosage Forms | Tablet, Capsule, Granule, Injection |
| Storage | Store in a well-closed container at controlled room temperature |
As an accredited Mannogem XL Mannitol 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 remains the preferred manufacturing route for moisture-sensitive actives because it eliminates the granulation drying step that can accelerate hydrolysis and oxidative degradation. Mannogem XL is charged into a bin blender after geometric premixing with the active and 0.5–1.0 wt% magnesium stearate or sodium stearyl fumarate. In immediate-release mono-layer tablet matrices, the mannitol fraction is typically 60–90 wt% of the core, with 2–5 wt% crospovidone or croscarmellose sodium as disintegrant and 0–15 wt% microcrystalline cellulose as compaction aid. The terminal product is a non-hygroscopic tablet for oral administration, commonly used for antihistamines, antacids, and vitamin C formulations where amine-containing actives would otherwise undergo Maillard browning with lactose. The powder is compressed on an instrumented rotary tablet press with 10 mm standard concave B-tooling. Precompression force is set between 2 and 6 kN, and main compression force is adjusted to achieve tablet breaking force of 80–150 N. Hardness is measured according to USP <1217>, disintegration according to USP <701>, and dissolution according to USP <711>. Friability should remain below 1.0% after 100 revolutions in a USP <1216> friabilator.
Compliance for oral direct compression grades requires conformance to the USP Mannitol monograph, PhEur 1235, JP Mannitol, and ICH Q3D elemental impurities. Because mannitol is non-reducing and non-hygroscopic, it is preferred over lactose in high-humidity zones above 60% RH. However, mannitol compact tensile strength is lower than that of microcrystalline cellulose; a pure mannitol tablet may require high main compression force and can exhibit capping if the powder is over-lubricated. Magnesium stearate levels above 1.5 wt% may reduce tensile strength and prolong disintegration. If friability exceeds 1.0%, formulators reduce the mannitol fraction to 70–80 wt% or add 10–20 wt% microcrystalline cellulose. The material should be stored below 25°C and protected from moisture excursions; although mannitol is non-hygroscopic, high relative humidity above 80% can cause surface water uptake and flow variation.
On high-speed dosator-type capsule fillers, the bulk powder must maintain consistent density and low adhesion to stainless steel contact surfaces. Mannogem XL is blended with 0.25–1.0 wt% sodium stearyl fumarate or magnesium stearate and directly filled into hard gelatin or HPMC capsules at fill weights from 100 mg to 800 mg depending on capsule size. The terminal product is an immediate-release hard-shell capsule for acid-sensitive actives, probiotic powders, or pediatric sprinkle formulations. The material’s low hygroscopicity at 25°C/75% RH reduces softening of gelatin capsules and minimizes moisture migration from the shell to the fill. The filled capsules are tested by USP <701> for disintegration and USP <711> for dissolution. Capsule weight uniformity is monitored according to USP <905> uniformity of dosage units.
Compliance for capsule premix should include compendial mannitol monograph release and ICH Q3D elemental impurity assessment. Because mannitol has a negative heat of solution, it can impart a cooling mouthfeel when the capsule contents are suspended or chewed; this is often used in antacid and mouth ulcer formulations. The low bulk density and free-flowing character make it suitable for gravity and dosator filling, but dust generation becomes problematic when loss on drying falls below 0.2% or when the powder is over-dried. Filling suites are typically held at 20–45% RH; electrostatic charge can cause powder sticking to capsule shells and weight variation. If flow is insufficient, 0.5–1.0 wt% colloidal silicon dioxide may be added, but this can reduce the dissolution rate of poorly soluble actives. Published data for specific Mannogem XL capsule fill weight limits on dosator nozzles is limited; process capability studies on the target machine are required before scale-up.
Wet granulation is applied when the active has low bulk density, poor flow, or high segregation tendency. Mannogem XL is granulated in a high-shear granulator or fluid-bed granulator with 2–5 wt% binder such as povidone K30 or hydroxypropyl cellulose dissolved in water or a water–isopropanol mixture. The mannitol fraction in the granule formulation generally ranges from 50 to 90 wt%, together with the active, 1–3 wt% disintegrant, and binder solution. The wet mass is passed through a 0.8–2.0 mm screen and dried at 40–60°C in a fluid bed or tray dryer to a final moisture content below 0.5 wt%. The dried granules are milled through a 0.8–1.25 mm screen and blended with 0.5–1.5 wt% lubricant before tablet compression or sachet filling. Terminal products include oral granules, sachets for electrolyte replacement, and tablets prepared by wet granulation.
Compliance is governed by the compendial mannitol monograph, ICH Q3D, and USP <701> disintegration where applicable. Because mannitol is non-reducing, aqueous granulation can be performed with primary amine actives without browning; this is a distinct advantage over lactose monohydrate. Drying temperatures must be kept below 70°C to avoid partial melting and granule hardening, which can reduce compressibility. If residual moisture exceeds 0.8%, granules may stick to tablet punches or cause sachet clumping. For sachet filling, fill weight control is typically within ±5% of target; the granule particle size distribution is controlled by sieve analysis according to USP <786> analytical sieving.
Parenteral mannitol is typically supplied as a 20% w/v aqueous solution for intravenous infusion after compounding, aseptic filtration through a ≤0.22 µm membrane, and terminal steam sterilization at 121°C for 15 minutes. Mannogem XL, when released against endotoxin and particulate requirements, functions as the active pharmaceutical ingredient in such presentations. The terminal product is an osmotic diuretic indicated for the reduction of intracranial pressure, cerebral edema, and intraocular pressure; each 100 mL contains 20 g mannitol in Water for Injection. The solution is hyperosmolar, with a calculated osmolality of approximately 1,098 mOsmol/L. The pH is adjusted to 4.5–7.0 with hydrochloric acid or sodium hydroxide. The fill is performed in glass or polyolefin containers; PVC containers require compatibility evaluation due to potential plasticizer extraction.
Compendial compliance for the injectable product includes USP <1> Injections, USP <788> Particulate Matter in Injections, USP <85> Bacterial Endotoxins, and PhEur 2.6.14 bacterial endotoxin testing. Storage at 20–25°C is required because mannitol solutions can crystallize at lower temperatures; if crystals form, the container is warmed and agitated until the crystals redissolve before administration. Use of an in-line 0.22 µm filter during infusion is standard practice when the product is withdrawn from a large-volume container. The solution must be visually inspected and withheld if it is not clear or if particulate matter is visible.
| Compendial parameter | Reference method | Application-relevant control |
|---|---|---|
| Assay (mannitol, anhydrous) | USP Mannitol monograph | 96.0–101.5% on dried basis |
| Melting range | USP <741>, PhEur 2.2.14 | 166–170°C |
| Specific rotation | USP <781>, PhEur 2.2.7 | +23.0 to +25.0° |
| Loss on drying | USP <731> | ≤0.5% |
| Sorbitol | PhEur HPLC method | ≤2.0% |
| Reducing sugars | PhEur colorimetric method | ≤0.3% |
| Bacterial endotoxins (parenteral) | USP <85>, PhEur 2.6.14 | Meets parenteral product monograph limit |
| Particulate matter | USP <788> | Meets large-volume parenteral limits |
For oral liquid and powder-for-oral-solution formats, the dissolution sequence is typically performed in purified water at 20–25°C under propeller stirring at 200–500 rpm. Mannogem XL is added slowly to avoid agglomeration; the terminal solution contains 5–20% w/v mannitol together with buffer salts, flavor, and an intense sweetener. The finished product includes unit-dose powder sachets and multi-dose oral solutions for laxative, urinary alkalinization, or electrolyte use. The non-cariogenic and non-reducing properties are relevant when the solution is administered long-term. The solution is filtered through 5 µm or finer filters and filled into amber glass or PET bottles. Microbiological quality is controlled according to USP <1111> acceptance criteria for nonsterile pharmaceutical products.
Compliance for oral liquids requires conformance to the mannitol monograph, ICH Q3D, and FDA 21 CFR 180.25 where the material functions as a food additive in oral dosage forms. Mannitol provides a cooling sensation because the enthalpy of solution is negative; this can improve palatability of electrolyte solutions. The sweetness contribution is approximately half that of sucrose on a weight basis, so formulations frequently include 0.05–0.2 wt% sucralose or sodium saccharin. Mannitol is stable to autoclaving at neutral pH; acidic formulations should be evaluated for reducing sugar formation during shelf life. The powder must be protected from moisture to prevent caking, although mannitol has low hygroscopicity. Published data for long-term palatability stability in specific commercial oral solutions is limited; organoleptic testing on each formulation is required.
In freeze-dried injectable formulations, mannitol is co-dissolved with the active at 5–15% w/v and filled into type I glass vials before lyophilization. Mannogem XL acts as a crystalline bulking agent, producing a firm cake and improving vial appearance. The terminal product is a lyophilized powder for injection reconstituted with Water for Injection or 0.9% sodium chloride before use. The lyophilization cycle includes freezing at −40°C or lower, optional annealing at −20°C to complete mannitol crystallization, primary drying at −20 to −10°C shelf temperature under vacuum, and secondary drying at 25–35°C. The crystallized mannitol does not protect the active by vitrification; thermosensitive biologics require a disaccharide such as sucrose or trehalose in addition to mannitol.
The final cake is stored at controlled room temperature and must meet USP <1> sterility, USP <85> bacterial endotoxins, and moisture limits below 1.0% by USP <921> Karl Fischer titration. Residual solvent must meet USP <467> if organic solvents are used in the formulation. Vial appearance, moisture, and reconstitution time are monitored batch-to-batch. Mannitol crystallization during freezing can cause vial breakage if the fill volume is too high or freezing is too rapid; annealing at −20°C reduces this risk. Mannitol fractions above 15% w/v may lead to cake collapse or uneven drying and are generally avoided. Compliance with EU GMP Annex 1 applies to aseptic lyophilization operations.
Orally disintegrating tablets are often formulated with mannitol as the principal diluent because of its fast dissolution in saliva and negative heat of solution, which produces a cooling effect in the mouth. The matrix contains 60–95 wt% Mannogem XL, 3–8 wt% superdisintegrant such as crospovidone or croscarmellose sodium, and a lubricant at 0.5–1.5 wt%. The terminal product is a dosage form that disintegrates in the oral cavity without water, intended for pediatric, geriatric, or dysphagic patients. The tablets are compressed on rotary tablet presses with low compression force to produce breaking force of 20–50 N; higher force reduces porosity and slows saliva penetration. Disintegration time is measured by USP <701> and should be below 60 seconds for an ODT; friability is tested by USP <1216> and often exceeds 0.5%, so packaging with desiccant and hard blister is required.
Compliance follows compendial mannitol monographs, ICH Q3D, and dissolution testing by USP <711> where the tablet contains an active. The high mannitol fraction can cause sticking to punches at low humidity; tooling with chromium nitride coating or external lubrication may be used. If the tablet is produced by lyophilization rather than compression, the mannitol solution is dosed into blister pockets and freeze-dried to form a porous wafer. The compressed ODT has higher mechanical strength but slower disintegration than the lyophilized wafer. Mannitol crystallinity and particle size influence mouthfeel; fine grades may dissolve quickly but reduce flow, whereas coarse grades improve flow but slow disintegration. Published data for the exact Mannogem XL particle-size effect on ODT disintegration is limited; formulators should screen batches on the target tablet press.
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Mannogem XL Mannitol Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable is a spray-dried D-mannitol released against the current Mannitol monographs of USP-NF, Ph.Eur., and JP. The chemical identity is established by infrared absorption and specific optical rotation, with molecular formula C6H14O6, molecular weight 182.17 g/mol, CAS 69-65-8, and specific optical rotation between +23.0° and +25.0° under Ph.Eur. 2.2.7. Assay is controlled within 96.0–101.5% on the dried basis under USP-NF and 98.0–102.0% under Ph.Eur. by liquid chromatography with refractive index detection. The product is a white, free-flowing powder intended for direct compression tablet manufacture, capsule filling, granule processing, and — following dissolution in Water for Injection, filtration, and terminal sterilization — as the active pharmaceutical ingredient in osmotic diuretic injections. Loss on drying is ≤0.5% at 105°C for 2 h; residue on ignition is ≤0.1%; chloride, sulfate, and reducing sugar levels remain below compendial thresholds. The grade is non-sterile as supplied and does not carry a depyrogenation claim in the unprocessed state.
Laser diffraction analysis under ISO 13320-1:2020 on a dry dispersion module yields typical particle-size distributions with D10 45–65 µm, D50 110–130 µm, and D90 220–270 µm. The residual coarse fraction above 500 µm is below 1%, limiting segregation during hopper discharge and tablet die filling. Bulk density by USP <616> Method I ranges from 0.42 to 0.48 g/cm³, tapped density from 0.48 to 0.56 g/cm³, giving a Carr compressibility index of 16–20% and Hausner ratio of 1.19–1.25. Powder flow at ambient relative humidity 30–50% typically shows angle of repose 32–38° using a fixed-funnel apparatus. Free moisture content remains below 0.5% when stored in sealed polyethylene-lined fiber drums at 25°C and 60% relative humidity. Open exposure above 75% relative humidity should be limited to short transfer intervals because surface moisture adsorption can raise the loss-on-drying value without deliquescence.
Scanning electron micrographs reveal a spheroidal, hollow-particle morphology with internal void spaces created by rapid droplet dehydration. Mercury intrusion porosimetry, where reported, shows total pore volume between 0.05 and 0.15 mL/g and median pore diameter 0.5–1.5 µm. This porosity reduces elastic recovery after unloading and helps prevent capping in deep concave tooling. X-ray powder diffraction confirms the material consists predominantly of the β polymorph, with melting endotherm onset at 164–167°C by differential scanning calorimetry at 10°C/min under nitrogen. These physical properties are not assay values; they are process-relevant indicators monitored through supplier change control.
Conventional crystalline mannitol, produced by recrystallization from aqueous or solvent systems, consists of dense angular particles that consolidate poorly under direct compression unless a binder is added. Spray-dried Mannogem XL particles are porous agglomerates of microcrystalline domains; this architecture increases available contact area during compaction and improves tensile strength without raising disintegration time. On an instrumented rotary tablet press operating at 50 rpm and compaction pressure 120–180 MPa, placebo compacts from a 2% magnesium stearate blend exhibit tablet hardness values in the 80–120 N range, whereas a fine crystalline mannitol powder of comparable particle size yields 40–70 N under identical conditions. The difference is attributed to greater plastic deformation and particle fragmentation from the spray-dried pore structure.
Heckel analysis of compression data at 50–200 MPa gives a mean yield pressure of approximately 120–150 MPa, indicating intermediate plastic deformation; compactibility is less than microcrystalline cellulose but greater than conventional crystalline mannitol. At compaction pressures above 250 MPa, tablet density reaches a plateau and elastic recovery increases, raising the risk of lamination. Lubricant sensitivity is moderate: when magnesium stearate levels exceed 2.0% w/w and blend mixing time exceeds 5 min, tensile strength may fall by 30–50% because the hydrophobic lubricant coats the porous particle surfaces. Sodium stearyl fumarate at 1.0–2.0% w/w has been reported to reduce this sensitivity. Disintegration times for direct-compression tablets containing crospovidone at 3–5% are typically 10–20 min in purified water at 37°C according to USP <701>.
| Parameter | Mannogem XL | Crystalline mannitol powder | Test method |
|---|---|---|---|
| Particle D50 | 110–130 µm | 20–50 µm | Laser diffraction, ISO 13320-1:2020 |
| Bulk density | 0.42–0.48 g/cm³ | 0.55–0.70 g/cm³ | USP <616> Method I |
| Carr compressibility index | 16–20% | 28–35% | USP <616> |
| Loss on drying | ≤0.5% | ≤0.5% | USP <731> |
| Typical direct compression tablet hardness at 150 MPa | 80–120 N | 40–70 N | Instrumented rotary press, USP <1217> |
Because mannitol does not present a reactive reducing carbonyl group under normal pharmaceutical conditions, Mannogem XL does not participate in Maillard browning with primary amine drugs or amino acid excipients. This behavior contrasts with lactose monohydrate and permits use in amine-containing formulations where lactose is contraindicated. The negative heat of solution of mannitol, approximately -121 kJ/kg, confers an endothermic cooling sensation on oral disintegration and should be considered when designing chewable or orally disintegrating tablets. The spray-dried grade retains this thermodynamic property; direct-compression tablet hardness is achieved without co-processed binders such as copovidone or starch, reducing total excipient burden.
For fluid-bed granulation using top-spray, a binder such as polyvinylpyrrolidone K30 at 2–4% w/w can be sprayed onto a fluidized bed of Mannogem XL at inlet air temperature 50–60°C and product temperature 25–32°C. The spray-dried particles exhibit reduced overwetting compared with fine crystalline mannitol, but overgranulation can occur if spray rate exceeds 20–25 g/min/kg of bed material. Final granules should be milled through a 0.8 mm screen and blended with extragranular disintegrant before compression. On a high-shear granulator with a 25 L bowl and chopper speed of 1500 rpm, addition of water or an aqueous binder to Mannogem XL proceeds rapidly because the spray-dried agglomerates exhibit high internal porosity. A binder solution added at 10–15% w/w can produce granules with mass mean diameter 250–500 µm after wet milling through a 1.0 mm screen. The wet mass should be dried to a final moisture content below 1.0% before tableting; residual moisture above this threshold has been associated with picking and sticking on tooling in batches run on a 16-station rotary press. Batch-to-batch variation in D50 is typically controlled within ±10 µm of the release target. This level of control permits use of continuous direct compression lines without real-time mass-flow correction; formulations with low-dose APIs below 1% can achieve blend uniformity at 99–101% of label claim when the API is micronized and geometrically diluted in a bin blender.
For parenteral presentations, Mannogem XL is the same chemical entity as the active ingredient in Mannitol Injection USP, typically formulated as a 20% w/v aqueous solution. The API is non-sterile as supplied; therefore, the finished product must be prepared by dissolving the powder in Water for Injection, clarifying through a 0.45 µm prefilter, sterilizing through a 0.22 µm membrane, and terminal sterilizing at 121°C for 15 min according to a validated cycle. Manufacture of the injectable solution involves dissolution at 60–70°C with continuous agitation; the solution is cooled to 25°C and adjusted to pH 5.0–6.0 with hydrochloric acid or sodium hydroxide. Calculated osmolarity for a 20% w/v solution is approximately 1098 mOsmol/L, exceeding physiological osmolarity and producing the osmotic diuretic effect. The finished solution is filled into polyolefin or polyvinyl chloride containers under nitrogen to limit oxidative degradation; mannitol itself is highly resistant to oxidation, but trace metal ions from container closures can catalyze discoloration if present above 0.1 ppm iron.
Bacterial endotoxin control follows USP <85>; the limit is calculated from the maximum adult dose as 5.0 EU/kg for general parenteral products and 0.2 EU/kg for intrathecal routes, with the API typically specified at an endotoxin level not exceeding 0.5 EU/g to allow terminal sterilization and dilution margin. Particulate matter in the final solution must meet USP <788> for large-volume injections; subvisible particle counts above 10 µm and 25 µm are therefore monitored after reconstitution. Mannitol solutions exhibit a negative heat of dilution and may crystallize if stored at reduced temperatures; containers showing crystals should be warmed to 37°C and inspected for complete dissolution before administration. The solution is incompatible with whole blood and should not be admixed with blood products because hypertonic mannitol produces red cell crenation.
| Control parameter | Standard or method designation | Release criterion |
|---|---|---|
| Identification by infrared absorption | USP <197>, Ph.Eur. 2.2.24 | Concordant with reference spectrum |
| Specific optical rotation | Ph.Eur. 2.2.7 | +23.0° to +25.0° |
| Assay (dried basis) | HPLC-RI, Ph.Eur. 2.2.29 | 98.0–102.0% |
| Loss on drying | USP <731> | ≤0.5% |
| Residue on ignition | USP <281> | ≤0.1% |
| Bacterial endotoxins (injectable) | USP <85> | Calculated from dose; API target ≤0.5 EU/g |
| Particulate matter (final injection) | USP <788> | Large-volume injection limits |
| Elemental impurities | ICH Q3D; USP <232>/<233> | Option 1 limits |
| Residual solvents | USP <467> | Class 3 limits |
Dry granulation by roller compaction at roll pressure 4–8 kN/cm and screen size 0.8–1.25 mm may be used when direct compression is not feasible for high-dose tablets. Capsule filling with dosator-type machines benefits from the narrow particle-size distribution; fill weight variability for size 1 hard gelatin capsules is typically within ±3% at speeds of 30,000–60,000 capsules/h when the powder bed is maintained at 40–60% relative humidity. The resulting granules retain compactibility but exhibit a slight increase in fines below 75 µm; this fraction should be limited to 15–20% to avoid segregation during compression. Published data for high-dose mannitol granules containing more than 60% API are limited, and formulation-specific tabletability must be confirmed on an instrumented press before scale-up.