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PVP XL/ CL/ Cross Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: PVP XL/ CL/ Cross 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
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    Specifications
    HS Code 740256
    Product Name PVP XL/CL/Cross (Crospovidone) Pharma Grade API for Tablet/Capsule/Granule and Oral/Injectable Dosage Forms
    Chemical Identity Crosslinked polyvinylpyrrolidone (polyvinylpolypyrrolidone)
    Cas Number 9003-39-8
    Molecular Formula (C6H9NO)n
    Molecular Weight Repeat Unit 111.14 g/mol
    Physical Appearance White to off-white, free-flowing, hygroscopic powder
    Odor And Taste Odorless and nearly tasteless
    Solubility In Water Insoluble in water; rapidly swells without forming a true solution
    Solubility In Organic Solvents Practically insoluble in ethanol, isopropyl alcohol, ether, and most common organic solvents
    Ph Of Aqueous Suspension 5.0 to 8.0 for a 1% w/v suspension
    Degree Of Crosslinking High, forming an insoluble polymer network suitable for XL, CL, and cross-linked grades
    Swelling Behavior Swells substantially in aqueous media, enabling rapid tablet/capsule disintegration
    Stability Profile Stable under normal pharmaceutical storage conditions and chemically stable across pH 1 to 12
    Particle Size Characteristics XL grade has relatively larger particles; CL and Cross grades have controlled fine particles for uniform performance
    Parenteral Suitability Injectable-grade is manufactured with controlled bioburden and low endotoxin levels
    Functional Role In Dosage Forms Acts as a superdisintegrant, binder, pore-forming agent, and dissolution enhancer in tablets, capsules, granules, and parenteral formulations
    Storage Property Should be stored in a tightly closed container, protected from excess moisture and heat

    As an accredited PVP XL/ CL/ Cross 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 PVP XL/CL cross-linked pharma API supplied in 25 kg sealed drums, double poly-lined, ideal for oral and injectable dosage forms.
    Container Loading (20′ FCL) A 20′ FCL loaded with Pharma Grade PVP in sealed containers, ensuring safe transport, stability, and contamination-free delivery.
    Shipping Shipped in sealed, moisture-resistant containers to preserve PVP XL/CL/Cross Pharma Grade API integrity for tablet, capsule, granule, injection, oral, and injectable use. Protect from humidity, light, and extreme temperatures. Includes safety data sheets, batch traceability, and compliant pharmaceutical labeling for global transport.
    Storage Store PVP XL/CL/Cross Pharma Grade in a cool, dry, well-ventilated area below 25°C. Keep containers tightly sealed to protect against moisture and humidity. Avoid exposure to direct sunlight and excessive heat. Use clean handling equipment to prevent contamination. Suitable for oral and injectable formulations when stored under recommended conditions.
    Shelf Life Shelf life is typically 36 months when stored in a cool, dry place in original, sealed containers.
    Application of PVP XL/ CL/ Cross Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    Direct compression of orally disintegrating tablet formulations with crospovidone relies on wicking-driven disintegration rather than polymer swelling, because the crosslinked homopolymer of 1-ethenylpyrrolidin-2-one is insoluble in water and does not form a viscous gel layer. Crospovidone Type A is loaded at 4–8 wt% in mannitol-based ODT matrices; Type B is substituted where a finer particle size is required for blend homogeneity under low-dose API conditions. The compendial control framework for these ODT products includes USP <701> disintegration testing with purified water at 37±2 °C, USP <1216> friability testing where tablet hardness is maintained between 25 N and 40 N, and ICH Q3D elemental impurity risk assessment because the disintegrant is a manufacturing aid rather than a purified API. FDA CDER guidance for orally disintegrating tablets specifies a recommended in vitro disintegration threshold of 30 s; production batches on rotary tablet presses at 40–80 rpm with a compression force of 8–15 kN show that exceeding 15 kN can push disintegration time beyond the 30 s limit by collapsing the pore network, particularly when the ODT contains high-fragmenting sugar alcohols. Blending is carried out in bin blenders at 10–15 rpm for 15–20 min before extragranular magnesium stearate is added at 0.5–1.0 wt% and mixed for 2–3 min, after which the material is tableted directly without granulation. Terminal product categories include antihistamine, antiemetic, phosphodiesterase-5 inhibitor, and neuropsychiatric orally disintegrating tablets; injectable use is excluded because the insoluble crosslinked particles cannot meet USP <788> subvisible particulate matter limits for parenterals.

    Why Split Intragranular and Extragranular Crospovidone Is Used in High-Dose Wet Granulation

    When an immediate-release tablet formula exceeds 500 mg total weight, wet granulation is frequently selected to improve flow and compressibility, but crospovidone can lose part of its capillary wicking capacity if it is exposed to excessive wet massing and drying. The standard split-loading strategy places 2–4 wt% crospovidone intragranularly before granulation and 2–5 wt% extragranularly after drying, so that the intragranular fraction creates internal porosity while the extragranular fraction disrupts the intergranule bond network at the tablet surface. Dissolution control is anchored to USP <711> apparatus II or I with release limits defined in the product-specific monograph, while residual moisture is monitored against the crospovidone loss-on-drying specification and ICH Q3C residual solvent requirements. In production-scale high-shear granulators with vertical bowls, typical impeller speeds run between 300 rpm and 600 rpm, chopper speeds between 1500 rpm and 3000 rpm, and wet massing times of 2–5 min; the granulated mass is then transferred to a fluid bed dryer with inlet air at 60–70 °C and product temperature held at 35–45 °C until LOD reaches 1.5–3.0%. Extended wet massing beyond 5 min has been observed to reduce crospovidone efficiency, producing tablets that pass hardness testing but fail disintegration because the agglomerated granules encapsulate the disintegrant in a slowly eroding matrix. Milling through a 0.8–1.0 mm screen and final blending with the extragranular crospovidone are followed by tablet compression to 60–100 N hardness for conventional immediate-release products. Terminal product categories include antihypertensive, antidiabetic, and antiretroviral tablets in which high-dose APIs require wet granulation to control flow and segregation.

    Table 1. Crospovidone loading windows and corresponding process controls across six oral solid dosage formats.

    Dosage formatTypical crospovidone loadingCritical process parameterTest designation
    Orally disintegrating tablet4–8 wt%Compression force 8–15 kNUSP <701>; FDA CDER 30 s
    High-dose wet granulated tablet2–4 wt% intragranular; 2–5 wt% extragranularWet massing time 2–5 min; LOD 1.5–3.0%USP <711>
    Hard gelatin / HPMC capsule2–5 wt%Granule bulk/tapped density ratio; plug porosityUSP <701>; USP <616>
    Roller compacted tablet3–6 wt%Ribbon solid fraction below 0.75USP <701>; USP <1216>
    Effervescent / dispersible tablet1–3 wt%Processing humidity <30% RHPh. Eur. 2.9.1; USP <701>
    Sublingual / buccal tablet5–10 wt%Tablet hardness 10–20 N; porosity retentionUSP <701>; USP <1216> justified range

    Roller Compaction Ribbon Density and the Re-Expansion Limit of Crospovidone

    Dry granulation by roller compaction subjects crospovidone to high mechanical stresses that reduce its native porosity, making ribbon solid fraction the controlling variable for subsequent tablet disintegration. Crospovidone is incorporated at 3–6 wt% before compaction because it also functions as a dry binder that improves ribbon strength without introducing a swelling polymer network. Ribbon solid fraction is calculated from ribbon envelope density and true density; development-scale studies indicate that crospovidone retains adequate re-expansion when the ribbon solid fraction remains below 0.75, whereas higher fractions can close accessible pores and produce granules with insufficient channel formation after recompression. Roller compactor settings are typically selected at hydraulic pressures between 40 bar and 70 bar, roll speeds of 2–5 rpm, and roll gaps of 2–3 mm, followed by oscillating milling through a 0.8–1.25 mm screen. The milled granules are blended with a lubricant and compressed on rotary equipment to hardness values specified by USP <1216> friability limits and USP <701> disintegration requirements. A process conflict arises when higher roll pressure is used to improve granule density and tablet weight uniformity: the resulting 0.78–0.82 solid fraction ribbons can trigger disintegration failures above 15 min for high-dose formulations because the crospovidone particles have already undergone irreversible pore collapse. Published data for this specific configuration is limited, but manufacturing-scale batch records commonly show that crospovidone-containing roller compacted products require lower roll pressures than those using sodium starch glycolate as the sole disintegrant. Terminal products include high-dose NSAIDs, metformin hydrochloride, and electrolyte tablets in which direct compression is not feasible due to poor flow or high unit weight.

    In hard gelatin and HPMC capsule fills containing poorly soluble APIs, delayed release can occur when the powder plug compacts during storage or transport at 40–60% RH, producing a capsule-shaped mass that erodes slowly in dissolution media. Crospovidone is added at 2–5 wt% to capsule granules or pellets to create hydrophilic channels at the plug surface, with the addition position determined by whether the capsule formulation is produced by fluid-bed top spray granulation or extrusion-spheronization. Fluid-bed granulation for capsule fills is conducted with inlet air at 55–70 °C, product temperature of 35–45 °C, and spray rate adjusted to maintain a stable fluidization regime; the dried granules are then filled into hard gelatin or HPMC capsules using dosator or tamping pin equipment at 20–25 °C and controlled humidity below 40% RH. The relevant control framework includes USP <701> disintegration for capsules, USP <711> dissolution for the final product, USP <616> bulk and tapped density measurements to detect plugging risk, and 21 CFR 211.110 in-process control requirements for blend uniformity and moisture. Crospovidone does not swell to the same degree as sodium starch glycolate, so its function in capsule plugs is less dependent on expansion under low water availability and more dependent on the distribution of insoluble, non-gelling particles within the plug structure. If the granule bulk/tapped density ratio or Carr index indicates poor flow, the capsule fill can segregate during encapsulation, leaving portions of the batch with insufficient crospovidone to disrupt the plug. Terminal product categories include antibiotic, antiviral, and cardiovascular hard capsule formulations where granulation is used to improve API dissolution and capsule filling performance.

    Effervescent and dispersible tablet manufacture imposes a water-free operating window because free moisture initiates acid-base reaction in the powder blend, leading to premature gas release and tablet surface defects. Crospovidone is used at 1–3 wt% in these systems not as a swelling agent but as a non-gelling wick that accelerates liquid penetration after the tablet is dropped into water, where the dispersion medium temperature may be as low as 15 °C. Processing is carried out at <30% RH, with sodium bicarbonate and citric or tartaric acid granulated or sized separately before dry blending with crospovidone, a lubricant, and sweetener; tablet compression is performed at 12–18 kN to produce hardness values of 40–70 N without initiating plastic deformation that delays water uptake. Disintegration control follows Ph. Eur. 2.9.1 and USP <701>, with effervescent products expected to disperse in 200 mL of water at 15–25 °C within 120 s, while ICH Q3C residual solvent testing is applied when non-aqueous granulation fluids are used. A processing conflict arises in direct compression effervescent tablets because magnesium stearate levels above 1.0 wt% can reduce water penetration, yet insufficient lubrication at high press speeds increases sticking to embossed tooling; crospovidone is therefore blended before lubrication and the lubricant mixing time is kept below 5 min. Terminal product types include effervescent analgesic, vitamin C, electrolyte replacement, and dispersible tablet formulations intended for oral suspension or solution administration.

    When Sublingual Tablet Hardness Drops Below 15 N, Crospovidone Type B Becomes the Controlling Disintegrant

    At compression forces below 10 kN, sublingual and buccal tablets made with mannitol and crospovidone can exhibit capping or edge failure if the disintegrant distribution is not optimized, because the low hardness range of 10–20 N leaves limited interparticle bonding to maintain tablet integrity. Crospovidone Type B is loaded at 5–10 wt% in these formulations, and the finer particle size provides a larger number of particles per unit mass to create a continuous capillary network without requiring high compression force. The process uses direct compression with pre-compression to remove air, main compression force between 3 kN and 8 kN, and rotary press speeds typically limited to 20–40 rpm to reduce lamination tendency. Disintegration is measured by USP <701> with purified water at 37±2 °C, while Ph. Eur. 2.9.1 is used for orodispersible or sublingual products in the European market; friability is tested by USP <1216> but low-hardness sublingual tablets often operate at values above the conventional 1.0% limit, requiring a justified range based on packaging and handling studies. The operational boundary is narrow: if hardness exceeds 20 N, the capillary pore volume decreases and disintegration may rise above 60 s, while hardness below 10 N increases breakage during blister packaging and patient handling. Crospovidone Type B is preferred over Type A in this application because the smaller particle size improves mouthfeel and reduces grittiness after disintegration, a factor that is not addressed by compendial disintegration tests but is critical for sublingual patient acceptability. Terminal product categories include antianginal, antiallergic, antiemetic, and hormone replacement sublingual or buccal tablets where rapid transmucosal absorption requires fast and reproducible disintegration in the oral cavity.

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    Certification & Compliance
    More Introduction

    PVP XL/ CL/ Cross Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable is a crosslinked polyvinylpyrrolidone family supplied as a white to off-white hygroscopic powder or friable flakes. The XL designation refers to a standard coarse crospovidone grade, while CL denotes a finer crosslinked povidone grade. Both are practically insoluble in water, ethanol, and methylene chloride and are produced by crosslinking 1-ethenylpyrrolidin-2-one; the Cross descriptor identifies the crosslinked homopolymer backbone. In tablet, capsule, and granule applications, these grades are used as disintegrants at 2% w/w to 5% w/w. For injection and oral liquid formulations, the crosslinked polymer is not used; instead, soluble low-K-value linear povidone grades such as K12 and K17 are supplied because they dissolve in water and can be filtered through 0.22 µm or 0.45 µm filters. The term API in the trade descriptor does not convert crospovidone or povidone into an active moiety for most monographed applications; compendial status remains that of a pharmaceutical excipient.

    The product family is controlled against the Crospovidone monograph in USP/NF and PhEur for PVP XL and PVP CL, and against the Povidone monograph for linear K12 and K17 when oral or injectable grade is ordered. Batch release typically includes infrared identification, nitrogen content, loss on drying, sulfated ash, pH of an aqueous suspension, water-soluble substances, vinylpyrrolidone monomer, peroxides, and sieve analysis. For injectable-grade linear povidone, bacterial endotoxin release per USP <85> and subvisible particulate control per USP <788> are added when the finished parenteral is tested. The crosslinked crospovidone grades are not suitable for injection because insoluble swellable particles cannot be removed by terminal sterilizing filtration and would exceed particulate limits in the finished product.

    Material handling differs among the grades. PVP XL has lower dusting and better flow in direct-compression blends, while PVP CL can be more electrostatic and requires humidity control below 60% RH to prevent agglomeration on punch faces. The material should be stored in tightly closed containers at controlled room temperature; extended exposure to high humidity increases moisture content and can reduce wicking efficiency. Crosslinked povidone is nonionic and compatible with most common filler-binder systems, but it should not be blended with strong oxidizing agents because residual peroxide species can accelerate oxidation of sensitive actives such as simvastatin or conjugated estrogens.

    Compendial release tests for PVP XL/CL crospovidone and injectable linear povidone grades
    TestLimit or RangeStandard or Method
    AppearanceWhite to off-white powder or friable flakesVisual
    IdentificationInfrared absorption matches referenceUSP <197K>, PhEur 2.2.24
    Nitrogen content, dried basis11.0–12.8%PhEur 2.5.33
    Loss on drying≤5.0%USP <731>, PhEur 2.2.32
    Sulfated ash / residue on ignition≤0.1%USP <281>, PhEur 2.4.14
    pH, 1% aqueous suspension5.0–8.0USP <791>, PhEur 2.2.3
    Water-soluble substances≤1.5%USP/NF, PhEur
    Vinylpyrrolidone monomer≤10 ppmUSP/NF, PhEur
    Peroxides, as H₂O₂≤400 ppmPhEur
    Sieve fraction, Type A / Type BMonograph-defined particle size limitsUSP <786>, PhEur 2.9.38
    Elemental impuritiesPDE limits by route of administrationICH Q3D, USP <232>/<233>
    Bacterial endotoxins, injectable linear povidone only≤0.25 EU/mg or supplier specificationUSP <85>

    How Does Crosslinked Povidone Reduce Disintegration Time in Compressed Tablets?

    Tablet disintegration is accelerated by liquid uptake through particle wicking and by strain recovery of deformed crospovidone domains after compression. Coarse XL grades with median particle size near 100–130 µm create low-tortuosity channels through the tablet matrix. Fine CL grades with median particle size below 75 µm distribute more uniformly around active pharmaceutical ingredient particles but can fill interparticulate voids under high compression, increasing the distance water must travel before wetting the core. In USP <701> disintegration testing with purified water at 37 ± 2 °C, immediate-release tablets containing 2–5% w/w crospovidone typically disintegrate within 1–5 min; the exact time depends on tablet hardness, porosity, filler solubility, and compression profile.

    Crospovidone does not form a continuous viscous gel in contact with water, unlike sodium starch glycolate or hypromellose. The wicking structure remains porous, so drug release is less likely to be retarded by a viscous gel layer. On rotary tablet presses, a coarse XL grade at 4% w/w in a direct-compression dicalcium phosphate anhydrous formula can maintain disintegration below 3 min, but tablet friability may exceed 1.0% if main compression force is pushed above 18 kN. A fine CL grade at the same use level reduces friability but may extend disintegration time when lubricant blending is longer than 5 min in a bin blender at 24 rpm because the fine particles adsorb lubricant and become less effective at wicking. Production batches should be evaluated at a precompression force of 2–5 kN to prevent capping without densifying the tablet enough to destroy wicking channels.

    In hard gelatin and hydroxypropyl methylcellulose capsule fill formulations, PVP XL and PVP CL are dry-blended at 2–4% w/w to prevent plug formation and maintain dissolution from the capsule plug. The crosslinked polymer absorbs gastrointestinal fluid at the capsule ends and creates pores in the plug, but its water-insoluble character does not retard capsule shell opening. For lipid or semi-solid capsule fill formulations, crospovidone is not recommended because it settles in high-viscosity vehicles without uniform wetting; colloidal silicon dioxide or fumed silica is preferred for viscosity control. In powder-in-capsule direct fill, fine CL grades may segregate less than coarse XL grades when bulk density differences exceed 0.2 g/mL, but both require periodic uniformity checks because low-bulk-density excipients can increase weight variability in high-speed dosators.

    Sieve Fraction and Hydration Capacity in USP/NF Type A and Type B Crospovidone

    USP/NF Crospovidone monograph separates Type A and Type B by particle size distribution. Type A retains a larger fraction above 75 µm, while Type B passes a greater fraction through a 75 µm sieve. The coarser Type A material, generally aligned with the PVP XL grade, has a typical bulk density of 0.25–0.40 g/mL and a hydration capacity of 4–7 g water/g polymer. The finer Type B material, often associated with low-fine CL variants, has a higher surface area per unit mass. Particle size is determined by analytical sieving per USP <786> or PhEur 2.9.38, and by laser diffraction per USP <429>. Hydration capacity is measured as grams of water retained per gram of dry polymer after centrifugation under fixed conditions; it is not an equilibrium swelling ratio because a portion of the water is held in interparticulate capillaries and is lost under compression.

    The larger particles of PVP XL generate visible porosity in tablets, which aids disintegration but can reduce tensile strength at low compression. PVP CL fills smaller voids and improves surface appearance but can slow water penetration if the tablet is over-lubricated. Grade choice is not based only on median particle size; span, fines content below 10 µm, and hygroscopicity after storage at 40 °C and 75% RH are equally important. Hygroscopicity of crospovidone at 25 °C and 80% RH is moderate compared with sodium starch glycolate. Moisture uptake above 5% w/w may lower the yield pressure of the polymer, reducing its ability to recover after compression. If tablets are packed in PVC blister without desiccant, disintegration time can increase over shelf life. Supplier certificates should report loss on drying and not just water activity, because surface water determines wicking and internal water determines plasticization.

    Comparative functional profile for PVP XL, PVP CL, and linear povidone K12/K17
    PropertyPVP XLPVP CLLinear Povidone K12/K17
    Solubility in waterPractically insolublePractically insolubleFreely soluble
    Compendial identityCrospovidone Type ACrospovidone Type BPovidone K-value
    Primary functionTablet/capsule disintegrantLow-fine disintegrantBinder, stabilizer, lyophilization aid
    Typical oral use level2–5% w/w2–5% w/w0.5–5% w/w
    Typical injectable use levelNot applicableNot applicable1–10% w/v for K12/K17
    Particle size characterD50 100–130 µmD50 20–40 µmK-value 12 or 17
    Liquid uptake4–7 g/g4–7 g/gForms solution
    Sterile filterabilityNot filterableNot filterableFilterable through 0.22 µm membrane if solution viscosity permits

    Granulation Processing Windows Are Narrower Than Direct Compression Batches

    In high-shear wet granulation, crospovidone is usually split between the intragranular and extragranular fractions. The intragranular fraction helps granule formation and provides internal wicking after drying; the extragranular fraction gives immediate liquid uptake at the tablet surface. A total crospovidone content of 4% w/w split as 2% intragranular and 2% extragranular is a common starting point for acetaminophen and ibuprofen formulations. The intragranular fraction can lose swelling capacity if the wet mass is over-granulated beyond endpoint torque. In a high-shear granulator with impeller speed 300 rpm and chopper speed 1,500 rpm, granulation endpoint commonly occurs within 2–5 min; beyond this window, the crosslinked polymer particles become coated with binder solution and cannot re-establish rapid water uptake after compression. Addition of extragranular crospovidone after dry milling can restore disintegration time to below 5 min in USP <701> testing.

    Roller compaction and slugging impose similar constraints. If roll force exceeds 20 kN/cm of roll width, crospovidone particles deform plastically and lose the strain recovery that drives tablet disintegration. Granule porosity after milling is a better predictor of disintegration than total crospovidone concentration. Production-scale batch records show disintegration drift when a fine CL grade is substituted for a coarse XL grade without adjusting compression force and granule size distribution; the smaller particles fill void spaces and increase tablet tensile strength at equal main compression. A change in crospovidone grade is therefore not a direct drop-in substitution and requires re-optimization of lubricant level, granule moisture, and compression profile.

    When Injectable-Grade Linear Povidone K12/K17 Replaces Crosslinked Grades in Parenteral Formulations

    The crosslinked PVP XL and PVP CL grades are excluded from injectable, ophthalmic, and sterile fluid applications because they are insoluble and elevate subvisible particulate counts. Linear povidone K12 and K17 are water-soluble and can be included in oral solutions, injections, and lyophilized products as stabilization aids. The Povidone monograph specifies K-value, nitrogen content, and moisture limits for these soluble grades; injectable-grade material adds a bacterial endotoxin specification, often ≤0.25 EU/mg for high-purity supply or ≤2.5 EU/g depending on finished dose and manufacturer release protocol. Endotoxin is determined by USP <85> or PhEur 2.6.14. Particulate quality of the finished parenteral is assessed by USP <788> and PhEur 2.9.19. Because linear povidone solutions increase viscosity, terminal filtration through 0.22 µm or 0.45 µm membranes must be validated under production flow rates; membrane fouling can occur at high polymer concentration or low temperature.

    For freeze-dried injections, K12 at 1–5% w/v can function as a bulking agent or stabilizer, but it is not a cryoprotectant in the same class as trehalose or sucrose. The glass transition temperature of an amorphous povidone-containing lyophilized cake is lowered by residual moisture; vials should be sealed with cake moisture below 1.0%. High-molecular-weight PVP K90 is generally avoided in parenterals because of higher solution viscosity and slower renal clearance. PVP XL and PVP CL cannot be used in injectable suspensions as suspending agents because they fail insoluble particulate limits and cannot be depyrogenated by dry heat without discoloration. Differences from other products therefore center on solubility, particle size, and regulatory monograph: crospovidone is an insoluble disintegrant, whereas linear povidone is a soluble binder and stabilizer.

    In oral liquid preparations, povidone K12 and K17 are used as viscosity modifiers and crystallization inhibitors at concentrations below 5% w/v; above 10% w/v the solution becomes tacky and difficult to pump in high-speed filling lines. The soluble polymer can also inhibit precipitation of poorly soluble actives through hydrogen bonding and hydrophobic interactions, but it is not a substitute for cyclodextrin or surfactant-based solubilization. These oral liquid applications are not interchangeable with crosslinked PVP XL/CL, which would sediment and not dissolve.

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