Products

2-Pyrrolidone Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: 2-Pyrrolidone Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    Specifications
    HS Code 515221
    Product Name 2-Pyrrolidone Pharma Grade API
    Chemical Name 2-Pyrrolidinone
    Synonyms 2-Pyrrolidone; alpha-Pyrrolidone; Butyrolactam
    Cas Number 616-45-5
    Ec Number 210-483-1
    Molecular Formula C4H7NO
    Molecular Weight 85.11 g/mol
    Appearance Colorless to slightly yellow clear liquid or low-melting solid
    Assay Purity ≥99.0%
    Grade Pharma Grade / API
    Pharmacopoeia Compliance USP/Ph. Eur./JP as applicable
    Solubility Miscible with water, ethanol, ether, chloroform, and benzene
    Melting Point 25.5 °C
    Boiling Point 245 °C
    Density 1.12 g/cm³ at 25 °C
    Refractive Index 1.487 at 20 °C
    Ph 6.0–8.5 (10% aqueous solution)
    Moisture ≤0.5% (Karl Fischer)
    Heavy Metals ≤10 ppm
    Residual Solvents Complies with ICH Q3C
    Flash Point 129 °C (closed cup)
    Viscosity 13.3 mPa·s at 25 °C
    Logp -0.85
    Storage Conditions Store in a tightly closed container in a cool, dry place, protected from moisture
    Shelf Life 24 months (typical)
    Packaging 25 kg/drum, 200 kg/drum, or as per customer requirement
    Dosage Forms Tablet, capsule, granule, injection
    Route Of Administration Oral and injectable
    Application Used as a pharmaceutical solvent, solubilizer, and penetration enhancer in oral and injectable formulations

    As an accredited 2-Pyrrolidone Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing
    Shipping
    Storage
    Application of 2-Pyrrolidone Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    In wet granulation of high-dose, poorly compressible BCS II active pharmaceutical ingredients, 2-pyrrolidone is incorporated at 5–15% w/w of the granulating fluid to dissolve povidone K30 or copovidone and to form a slow-evaporating binder bridge across primary particles. The granulating fluid is introduced into a high-shear mixer with impeller tip speed 4–8 m/s and side chopper speed 1,500–3,000 rpm; end point is accepted only when impeller torque or power draw rises 15–25% above the dry-mix baseline. Because the boiling point of 2-pyrrolidone is 245 °C and its vapor pressure is substantially lower than water, the wet mass does not surface-dry during extended granulation, which reduces large granule fragmentation but also shifts the residual solvent burden to the drying step. Production drying is performed in a fluid-bed processor with inlet air temperature 55–65 °C and product temperature 35–45 °C until loss on drying reaches 1.5–2.5% w/w; however, 2-pyrrolidone is not removed to below process capability at this stage. A subsequent static tray drying step under vacuum at 25–35 kPa and 50–60 °C for 4–8 h is required to reduce residual solvent. Batch records often show residual 2-pyrrolidone plateaus above 0.1% w/w if the granulate bed is not milled before the vacuum step; therefore, an oscillator or cone mill fitted with a 1.0–1.5 mm screen is used before final drying. Tablet compression of the resulting granulate is performed on a rotary tablet press with precompression 5–8 kN and main compression 15–25 kN for tablets in the 300–500 mg mass range; tablets are accepted when hardness is 80–150 N, friability is ≤0.8% after 100 rotations per USP <1216>, and disintegration per USP <701> completes within 15 min for immediate-release film-coated tablets. The residual solvent specification must be justified because 2-pyrrolidone is not assigned a harmonized PDE in ICH Q3C; a marketing authorization file must therefore carry a tox-qualified in-house limit under the residual solvent framework. The granulation fluid is not suitable for effervescent compositions, because the hygroscopic character of 2-pyrrolidone raises moisture sensitivity and the low evaporation rate compresses drying capacity.

    Liquid-Filled Hard Capsule Fill Solvent and Shell Compatibility Limits

    For liquid-filled hard capsules, 2-pyrrolidone is used as a co-solvent in fill formulations at 10–25% w/w in combination with PEG 400, propylene glycol, medium-chain triglycerides, or glycerol monooleate. The function is to maintain the active pharmaceutical ingredient in molecular dispersion during capsule shell penetration and disintegration, while the high boiling point prevents rapid evaporation from the fill dosing nozzle. Capsule filling machines operating with positive displacement pistons at 30–45 °C require fill viscosity in the range 100–1,000 mPa·s to avoid splashing and ensure fill weight variability below ±3% RSD. At 2-pyrrolidone concentrations above 20% w/w, gelatin shell softening is observed due to plasticization; hypromellose shells show less deformation but may exhibit retarded dissolution if the fill contains more than 15% w/w water. Band sealing is performed with a gelatin solution at 55–60 °C, and filled capsules are tested for leakage under vacuum at −50 kPa for 5 min. Dissolution testing per USP <711> uses 900 mL of pH 1.2 hydrochloric acid or pH 6.8 phosphate buffer at 37 ± 0.5 °C with paddle speed 50 rpm; samples are analyzed by HPLC with UV detection. When the fill contains 2-pyrrolidone, the dissolution medium may show a transient co-solvent effect that increases the apparent release rate for poorly water-soluble actives; this effect must be distinguished from true dissolution by using a precipitation-inhibiting surfactant in the medium only if specified in the monograph. Batch-to-batch variation in gelatin shell moisture, usually 13–16% w/w, interacts with fill hygroscopicity; dry-shell capsules with moisture below 12% w/w become brittle during banding. Production batches therefore require storage of empty capsules at 20–25 °C and 40–50% RH for at least 24 h before filling. Terminal products include lipid-soluble vitamins, poorly soluble cardiovascular actives, and BCS II weak bases that are degraded in conventional aqueous granulation.

    Extrusion-spheronization of poorly soluble actives into multiparticulate granules requires a wetting phase that remains plastic during the residence time in the extruder barrel; a binder phase containing 2-pyrrolidone at 3–10% w/w of the dry powder mass is added to microcrystalline cellulose, lactose monohydrate, and the active. The wet mass is processed through a twin-screw extruder with a length-to-diameter ratio of 25:1, screw speed 100–200 rpm, and die plate aperture 0.8–1.2 mm. The extrudate is transferred to a spheronizer run at 800–1,200 rpm for 2–5 min until spheroid aspect ratio falls below 1.2. The low vapor pressure of 2-pyrrolidone prevents evaporative cooling and surface crusting, but it also means that the spheroids retain solvent after a standard fluid-bed drying step at 50–60 °C for 20–30 min. A vacuum drying stage at 10–20 kPa and 45–55 °C for 4–6 h is required to bring residual 2-pyrrolidone below the internal release threshold. Drying curves typically exhibit a biphasic pattern: free water is removed rapidly, followed by a slow desorption phase controlled by granule pore structure; milling through a 0.8 mm screen before the vacuum stage shortens the second phase. The resulting pellets are filled into hard gelatin capsules or sealed into sachets for reconstitution. Dissolution testing per USP <711> is used with a pH 6.8 buffer and 50 rpm basket or paddle; enteric-coated pellets require an acid stage at pH 1.2 for 2 h followed by buffer stage at pH 6.8. Loss on drying per USP <921> is controlled to ≤1.5% w/w for capsule-filled pellets. Trace elemental impurities are controlled per ICH Q3D; the supplier must provide a risk assessment covering Class 1, 2A, and 2B elements, and oral dosage acceptance limits are calculated from the permitted daily exposure and daily dose. Pellets produced with 2-pyrrolidone are not recommended for highly water-soluble actives that undergo solvent-mediated particle growth in the wet mass, because the prolonged liquid residence creates a recrystallization path; dry granulation or direct compression is preferable for such actives.

    How Does 2-Pyrrolidone Function in Injectable Co-Solvent Systems for Poorly Water-Soluble APIs?

    In parenteral vehicles, 2-pyrrolidone is evaluated as a co-solvent at 10–40% v/v in purified water-for-injection together with propylene glycol, PEG 400, or mannitol as tonicity agent. The co-solvent effect raises the saturation solubility of poorly water-soluble neutral APIs, while the high dielectric constant of the medium reduces ion-pair formation in glass vials. Terminal sterilization is performed by autoclaving at 121 °C for 15 min; formulations should be screened for hydrolytic degradation of 2-pyrrolidone at pH values below 3.0 or above 9.0. The pH of the final admixture is adjusted to 5.5–7.0 with 0.1 N hydrochloric acid or sodium hydroxide, and osmolality is adjusted to 280–320 mOsm/kg with mannitol or sodium chloride. Filtration through a 0.22 µm sterilizing-grade polyvinylidene fluoride membrane is performed at 20–25 °C under differential pressure below 1.0 bar; flux is inversely related to viscosity, and batches with 2-pyrrolidone at 40% v/v may display viscosity values that require filter area scaling of 1.5–2.0× relative to aqueous solutions. Particulate matter is controlled per USP <788>: for small-volume injectables, light obscuration counts must not exceed 6,000 particles ≥10 µm and 600 particles ≥25 µm per container. Endotoxin content is controlled per USP <85> using a validated limulus amebocyte lysate test with a limit derived from the maximum bolus dose; the solvent supplier must provide a certificate stating endotoxin below the method threshold. The terminal product is packed in Type I borosilicate glass ampoules or vials with butyl rubber stoppers and is administered by intramuscular or slow intravenous injection. Because dilution of the co-solvent in plasma causes a sharp drop in solubility, in-vitro precipitation testing is performed by mixing the formulation with simulated plasma at 37 °C under agitation at 100 rpm; the resulting particle size is measured by dynamic light scattering, and precipitation below 250 nm is regarded as a pass indicator for injectable screening. Published data for specific 2-pyrrolidone-containing injectable formulations is limited; preformulation work should therefore include free fraction studies because solvent binding can shift the apparent log P of the active.

    ApplicationCritical controlStandard/codeTypical range or limit
    Tablet wet granulationResidual solvent after vacuum tray dryingUSP <467> / ICH Q3CNo harmonized PDE; tox-qualified in-house limit required
    Liquid-filled hard capsuleFill viscosity at 35 °CUSP <911>100–1,000 mPa·s
    Oral granules/pelletsLoss on dryingUSP <921>≤1.5% w/w
    Injectable co-solventParticulate matter ≥10 µm / ≥25 µmUSP <788>6,000 / 600 per container for SVI
    Softgel capsuleShell loss on dryingUSP <731>6–10% w/w
    Oral solutionPreservative efficacyUSP <51>Category 1 acceptance criteria

    When 2-Pyrrolidone Replaces Ethanol in Soft Gelatin Capsule Fill Media

    Soft gelatin capsule fill formulations that contain ethanol often require explosion-proof processing and can produce shell embrittlement through rapid moisture loss; when 2-pyrrolidone replaces ethanol at 5–20% w/w of the fill mass, the fill remains liquid at die roll temperature and the shell moisture balance is more stable. Fill mixtures typically combine 2-pyrrolidone with PEG 400, propylene glycol, and polyvinylpyrrolidone K17 or K30; the active is dissolved at 40–60 °C under nitrogen to prevent oxidative degradation of oxygen-sensitive APIs. The fill mass is deaerated under vacuum at −80 kPa for 30–60 min, and the bubble-free liquid is pumped to a rotary die encapsulation machine with spreader boxes held at 40–50 °C. Gelatin ribbon thickness is controlled at 0.8–1.0 mm; ribbon moisture is measured by near-infrared at 30–40% w/w before die roll sealing. Because 2-pyrrolidone has strong hydrogen-bonding capacity, fill-shell interaction favors migration of water from the shell to the fill, which can increase shell brittleness if the fill water activity is below 0.2; therefore, fill formulations are conditioned to a water activity of 0.45–0.65 before encapsulation. Drying of softgel capsules is performed in a tumble dryer at 20–25 °C and 20–30% RH for 12–24 h, followed by a final tray drying stage until shell loss on drying reaches 6–10% w/w per USP <731>. The terminal product is a sealed soft gelatin capsule for oral use; dissolution testing per USP <711> employs the paddle method at 50 rpm in 900 mL of 0.1 N hydrochloric acid containing 0.5% w/v sodium lauryl sulfate if justified by sink conditions. Visual leakage is evaluated by pressing capsules between filter paper for 24 h at 40 °C and 75% RH; a pass requires no oily halo. The main process constraint is that 2-pyrrolidone cannot be used above 20% w/w in highly filled softgels intended for storage in PVC blisters, because the solvent can migrate into the PVC film and alter the sealing lacquer.

    Oral solution and reconstituted suspension vehicles containing 2-pyrrolidone at 2–10% w/v are used as a solubilizing fraction in sugar-free or alcohol-free pediatric and geriatric formulations. The solvent is mixed with purified water, sorbitol, glycerol, and sodium benzoate at 0.1–0.2% w/v; pH is adjusted to 4.5–6.0 with citric acid or sodium citrate. The manufacturing sequence includes heating the solvent phase to 40–50 °C to dissolve the active, then cooling to 20–25 °C before mixing with the aqueous preservative phase to avoid local precipitation. The solution is filtered through a 5 µm clarification filter and filled into amber Type III glass bottles with child-resistant closures. Terminal heating is avoided for heat-labile actives; when required, the solution is pasteurized at 80 °C for 30 min. The main stability risk is chemical degradation of the solvent under strongly acidic or basic conditions; amide ring opening is promoted below pH 3.0 and above pH 9.0, so a buffered pH range is mandatory. Reconstitution of dry powder for oral solution using 2-pyrrolidone-containing diluent is performed at 25–30 °C with manual shaking for 15–30 s; the resulting preparation should pass a 0.5 mm sieve according to the pharmacopeial monograph. Microbiological quality is controlled per USP <51> antimicrobial effectiveness testing or Ph. Eur. 5.1.3, and a preservative efficacy test is required if the formulation is multi-dose. The terminal product is an alcohol-free oral solution or reconstituted suspension intended for dose-flexible administration.

    Free Quote

    Competitive 2-Pyrrolidone Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8615365186327 or mail to admin@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8615365186327

    Email: admin@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    The product designated 2-Pyrrolidone Pharma Grade, CAS 616-45-5, molecular formula C4H7NO, molar mass 85.10 g/mol, is a cyclic lactam liquid supplied for pharmaceutical formulation in tablet, capsule, granule, and injectable processes. Commercial model designation is supplier-specific; procurement specifications generally use the descriptor “2-Pyrrolidone for pharmaceutical use” or “2-Pyrrolidone parenteral grade” plus a drug master file identifier, rather than a standardized model number. The material is normally classed as an excipient or processing aid in regulatory filings, even when trade documentation uses the term API-grade to indicate GMP manufacturing under ICH Q7 and compendial purity rather than pharmacological activity. For oral solid dosage forms, 2-pyrrolidone is typically used as a granulation solvent for povidone-based binder systems, a coating solvent component, or a liquid-fill co-solvent for hard capsules. For injectable development, it is used as a non-aqueous carrier or co-solvent for poorly water-soluble active pharmaceutical ingredients. The specification profile, residual solvent behavior, and handling requirements differ markedly from common solvents such as ethanol, dimethyl sulfoxide, and N-methyl-2-pyrrolidone.

    Why Does 2-Pyrrolidone Solidify at Ambient Storage Temperatures?

    The melting range of the neat compound is 24–25 °C at 101.3 kPa. A warehouse maintained below 20 °C therefore produces partial or complete crystallization, which prevents reliable drum withdrawal through standard top-pour dispensing lines. In manufacturing, drums are conditioned in a forced-air cabinet at 35–40 °C for at least 24 h before decanting into a jacketed stainless steel vessel. A nitrogen overlay at 50–100 mbar positive pressure is recommended to limit atmospheric moisture uptake because the liquid is hygroscopic. Partial re-melting alone is insufficient: water can stratify in the melt phase, and multiple freeze-thaw cycles can raise localized water content through condensation. Complete homogenization with recirculation through a 10 µm in-line filter is therefore required before sampling for water analysis.

    The dynamic viscosity at 25 °C is approximately 13.3 mPa·s, roughly eight times the viscosity of N-methyl-2-pyrrolidone at the same temperature. This difference affects filter sizing, pump selection, and mixing time in 2-pyrrolidone-containing systems. At 35–40 °C, the viscosity decreases sufficiently for low-shear transfer and high-shear mixing, but the jacket temperature should remain below 60 °C to avoid accelerated ring-opening hydrolysis. The vapor pressure is approximately 0.001 kPa at 20 °C; the closed-cup flash point is approximately 129 °C, which is higher than that of ethanol but still demands solvent-handling controls. This combination of low vapor pressure and high boiling point near 245 °C means the solvent does not flash off during ordinary processing and may remain as a residual solvent unless the downstream drying step is specifically engineered.

    Specification Bounds, Water Activity, and Residual Solvent Control

    Because a dedicated 2-pyrrolidone monograph is not present in all compendia, batch release often relies on general chapters under the applicant’s specification. The following representative acceptance profile is drawn from vendor technical data sheets for parenteral-grade material; the registered limits in a given file may be tighter.

    TestMethodRepresentative acceptance
    AppearanceVisualClear, colorless to pale yellow liquid; solidifies below 25 °C
    AssayGC with internal standard, USP<621>≥99.5%
    WaterKarl Fischer, USP<921>≤0.10%
    ColorASTM D1209≤20 APHA
    Residue on ignitionUSP<281>≤0.05%
    Heavy metalsUSP<232>/<233>≤10 ppm
    Residual solventsUSP<467>Conforms to ICH Q3C option selected in the drug master file
    EndotoxinUSP<85>≤0.25 EU/mL for parenteral grade
    Particulate matterUSP<788>Compliance demonstrated in final preparation; not always an incoming solvent test

    Assay by gas chromatography with an internal standard is used because the impurity profile may contain residual starting materials such as gamma-butyrolactone and ring-opening products. Water content is a critical quality attribute not only for assay but also for the stability of moisture-sensitive actives; water ingress above 0.10% increases the risk of hydrolysis to 4-aminobutyric acid during storage. Heavy metals and residue-on-ignition limits are relevant to injectable grades because the solvent may contact actives that are sensitive to metal-catalyzed oxidation. Residual solvent testing per USP<467> applies to the finished dosage form, but the solvent source can be controlled by a vendor residual-solvent profile that demonstrates the absence of Class 1 solvents and limits Class 2 solvents.

    In tablet and capsule processing, 2-pyrrolidone is typically introduced as part of a binder solution rather than as a dry component. A common design uses povidone or copovidone dissolved at 5–15 wt% solids in a solvent phase containing 2-pyrrolidone and water or ethanol. In a high-shear granulator equipped with torque and power-draw sensors, the end point is controlled by impeller power and product temperature rather than by solvent volume alone. Because the vapor pressure is near 0.001 kPa at 20 °C, residual solvent does not flash off during wet massing; vacuum tray drying at 60–70 °C and 10–20 kPa may require cycle times of 8–24 h for a 5–10 kg bed depth, depending on granule size distribution. Headspace gas chromatography per USP<467> should be used to confirm the residual level in granules or finished tablets. Liquid-filled hard capsules require fill weight calculations based on the solvent density of approximately 1.11 g/mL; capsule shell compatibility is also critical because the hygroscopic solvent can transfer water to the gelatin or HPMC shell and alter brittleness. Capsule sealing and storage at 15–25 °C and ≤40% RH should be qualified by moisture vapor transmission rate testing per ASTM E96-22 or equivalent, and by seal strength testing. Unlike povidone, which is a polymer that provides mechanical tablet strength at 2–5 wt% of the formulation, 2-pyrrolidone is a mobile liquid and does not act as a dry binder; its function is to dissolve or deliver the actual binder and other functional excipients.

    When 2-Pyrrolidone Replaces N-Methyl-2-Pyrrolidone in Injectable Formulation

    Injectable development sometimes evaluates 2-pyrrolidone as a lower-vapor-pressure, higher-flash-point alternative to N-methyl-2-pyrrolidone for solubilizing poorly water-soluble actives. The replacement is not drop-in. The unsubstituted lactam contains an N–H donor that increases self-association and dynamic viscosity, and its melting range near 25 °C can complicate cold-room handling and filter transfer lines. Co-solvent systems containing 10–30% v/v 2-pyrrolidone have been reported in formulation literature, but each formulation requires nonclinical local tolerance and systemic exposure justification because there is no default ICH Q3C permitted daily exposure for this solvent in injectable products. The final preparation must meet USP<788> particulate matter limits, and the incoming solvent should be controlled for endotoxin by USP<85>. Sterile filtration through a 0.2 µm membrane must be validated in the actual drug product because 2-pyrrolidone can alter membrane wetting, flux, and extractables. At 25 °C, the higher viscosity may reduce filtration throughput relative to ethanol-water systems, so temperature-controlled filtration at 35–40 °C is sometimes used when the active and excipients are thermally stable.

    Hydrolysis of 2-pyrrolidone to 4-aminobutyric acid is acid- and base-catalyzed and becomes significant at elevated temperatures. In aqueous vehicles above 80 °C, ring opening can generate an amine that shifts pH and may interact with acid-containing actives. Pre-formulation stability screens should therefore include pH drift studies under nitrogen at 25 °C and 60 °C; a drift exceeding 0.5 pH units over 14 days may indicate that the system should be processed at lower temperature or formulated with reduced water content. Terminal sterilization by autoclaving at 121 °C is not automatically suitable for 2-pyrrolidone-containing parenterals; if degradation is unacceptable, aseptic filtration should be evaluated. The compound is hygroscopic and must be stored under nitrogen in closed containers; repeated opening of drums in humid areas can increase water content and promote hydrolysis.

    The table below compares typical physical properties relevant to solvent substitution. The values are drawn from standard solvent reference tables and supplier technical data sheets; they do not by themselves establish regulatory acceptability.

    Property2-PyrrolidoneN-Methyl-2-pyrrolidoneDimethyl sulfoxideEthanol
    CAS616-45-5872-50-467-68-564-17-5
    Molar mass85.10 g/mol99.13 g/mol78.13 g/mol46.07 g/mol
    Melting point24–25 °C-24 °C18.5 °C-114 °C
    Boiling point at 101.3 kPa245 °C202 °C189 °C78.3 °C
    Dynamic viscosity at 25 °C13.3 mPa·s1.67 mPa·s1.99 mPa·s1.1 mPa·s
    ICH Q3C classificationNot assigned as Class 1 or Class 2Class 2, PDE 5.3 mg/dayClass 3Class 3

    The comparison table does not constitute a regulatory approval matrix. A substitution from N-methyl-2-pyrrolidone or dimethyl sulfoxide to 2-pyrrolidone requires reformulation because viscosity, drying rate, membrane permeability, and residual solvent acceptance limits differ. In particular, N-methyl-2-pyrrolidone is an ICH Q3C Class 2 solvent with a formal PDE of 5.3 mg/day, whereas 2-pyrrolidone is not assigned the same Class 2 limit; its residual level must be qualified by the sponsor. Compared with ethanol, 2-pyrrolidone is not removed by conventional tray drying under ambient airflow and requires active vacuum and elevated temperature. Compared with dimethyl sulfoxide, 2-pyrrolidone has a higher melting point and higher viscosity, which may complicate low-temperature processing but can reduce solvent odor and reduce the severity of evaporative cooling in spraying operations.

    For sterile injectable manufacture, the maximum amount of residual 2-pyrrolidone in the finished product is controlled by the safety qualification of the formulation, not by a general pharmacopoeial monograph limit. If the product is used as a granulation or coating solvent, the same principle applies: USP<467> provides the analytical platform, but acceptance limits are route-specific and should be derived from the applicable ICH Q3C guidance or the sponsor’s nonclinical package. Manufacturers should also evaluate degradation to 4-aminobutyric acid by stressed stability studies at 40 °C/75% RH and 60 °C dry heat, especially for oral granules and injectable solutions stored in semi-permeable containers. Contact with strong acids, strong bases, or oxidizing agents should be avoided unless the resulting degradation products are fully characterized and controlled by the release specification.

    Top