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Bovine Bile extract Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: Bovine Bile extract 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 817862
    Productname Bovine Bile Extract Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    Source Bovine bile
    Apigrade Pharma Grade
    Dosageforms Tablet, Capsule, Granule, Injection
    Administrationroutes Oral, Injectable
    Appearance Brownish-yellow to greenish-brown powder or extract
    Activeconstituents Bile acids and bile salts including cholic acid and deoxycholic acid
    Solubility Soluble in water and alcohol; partially soluble in organic solvents
    Assay Typically ≥ 50% total bile acids or as per pharmacopoeial specification
    Ph 6.0–8.5 for 1% aqueous solution
    Lossondrying ≤ 5.0%
    Heavymetals ≤ 20 ppm
    Microbiallimit Total aerobic microbial count ≤ 10^3 CFU/g; absence of specified pathogens
    Sterility Sterile grade available for injectable use; non-sterile for oral solid dosage forms
    Storage Store in a cool, dry, well-ventilated place protected from light and moisture
    Shelflife 24 months from date of manufacture when stored properly
    Packaging Double-lined polyethylene bags inside fibre drums or as per customer requirement
    Qualitystandard Complies with applicable pharmacopoeial or customer specification
    Therapeuticcategory Cholagogue, choleretic, digestive aid
    Casnumber 8008-63-7

    As an accredited Bovine Bile extract 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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    Application of Bovine Bile extract Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    High-Shear Wet Granulation of Bovine Bile Extract and the Binder Viscosity Plateau at 25°C

    Bovine bile extract pharma grade is a heterogeneous animal-derived material containing conjugated cholic and deoxycholic acids, residual phospholipids, and minor bilirubin-related pigments. It is not a single chemical entity, so tablet formulation must be designed around a manufacturer-specified total bile acid content, moisture, and TSE documentation under EMA/410/01 Rev. 3 and Ph. Eur. 5.2.8. High-shear wet granulation is selected for immediate-release choleretic tablets when the extract loading reaches 35–60 wt% of the core mass. In a representative 250 mg core containing 100 mg extract, povidone K30 is added as a 5% aqueous binder solution at a dry binder level of 3 wt%. The granulator is operated with an impeller speed of 300–500 rpm and a chopper speed of 1500–3000 rpm; endpoint is controlled by torque or power draw rather than fixed time because the extract becomes pasty when the binder volume exceeds the wet mass saturation point. The wet mass is milled through a 1.5 mm screen and dried in a fluid-bed dryer with inlet air at 55–65°C until loss on drying is held at 2.0–3.5%. Extragranular croscarmellose sodium at 3 wt%, microcrystalline cellulose at 20 wt%, magnesium stearate at 0.5 wt%, and talc at 1 wt% are added after dry screening; lubrication is limited to 2 min to avoid hydrophobic film formation. Compression on a rotary press at 12–18 kN produces a hardness range of 50–80 N and disintegration below 15 min under USP <701> or Ph. Eur. 2.9.1. Dissolution testing under USP <711> or Ph. Eur. 2.9.3 requires a medium selected after pH-solubility profiling, because unconjugated bile acid fractions can precipitate below pH 4.0; a product-specific Q value is established rather than a universal monograph limit. The dried tablet cores are film-coated with an HPMC-based system to 3 wt% weight gain for taste masking. The terminal product is an immediate-release oral tablet for choleretic or lipotropic use. Direct compression is generally avoided at extract loadings above 25 wt% because the cohesive fines raise the angle of repose above 40° and produce segregation in the feed frame.

    Why Hard Capsule Filling Requires Moisture Control Below aw 0.35 Before Paddle Feeder Transfer?

    Hard capsule filling with bovine bile extract at 40–50 wt% in size 0 HPMC capsules is controlled primarily by water activity rather than by total moisture alone. At aw 0.35 or below, the powder bed remains free-flowing and transfers through the paddle feeder into dosator tubes with minimal fill weight drift. Above aw 0.35, the hygroscopic extract begins to form interparticle liquid bridges, the angle of repose rises above 40°, and the dosator pins compact the wet powder instead of cutting a uniform plug. The representative blend contains microcrystalline cellulose 30 wt%, lactose monohydrate 20 wt%, sodium starch glycolate 2 wt%, colloidal silicon dioxide 1 wt%, and sodium stearyl fumarate 1 wt%. The pre-blend is dried in a vacuum oven at 40°C under reduced pressure until water activity is ≤0.35 or Karl Fischer moisture is ≤2.0% by USP <921> or Ph. Eur. 2.5.12. The dried blend is passed through a 0.8 mm screen and loaded directly into a dosator-type capsule filler. A representative fill weight of 300 mg delivers 120 mg extract per capsule, with uniformity of dosage units controlled under USP <905> or Ph. Eur. 2.9.40 and an acceptance value ≤15.0. HPMC capsules are preferred over gelatin because the extract contains residual phospholipids that can accelerate gelatin cross-linking when stored above 25°C/60% RH. The terminal product is a hard capsule for bile acid supplementation or digestive support. Sodium stearyl fumarate is used instead of magnesium stearate because the extract’s acidic fractions can de-lubricate the dosage form at extended mixing times.

    Because the compendial test set changes across oral and injectable forms, the following matrix is applied during batch release.

    Dosage formCritical attributeMethod/standardOperational boundary
    Immediate-release tabletDisintegrationUSP <701> / Ph. Eur. 2.9.1≤15 min in water at 37°C for uncoated cores
    Immediate-release tabletDissolutionUSP <711> / Ph. Eur. 2.9.3Product-specific Q; medium chosen after pH-solubility study
    Hard capsuleUniformity of dosage unitsUSP <905> / Ph. Eur. 2.9.40Acceptance value ≤15.0
    Hard capsuleWater contentUSP <921> / Ph. Eur. 2.5.12≤2.0% or water activity ≤0.35
    Oral granules/sachetMass uniformityUSP <905> / Ph. Eur. 2.9.5Acceptance value ≤15.0 for single-dose sachets
    Oral granules/sachetParticle size distributionUSP <786> / Ph. Eur. 2.9.38D50 180–250 µm
    Lyophilised injectionBacterial endotoxinsUSP <85> / Ph. Eur. 2.6.14Default IV upper boundary 5 EU/kg/h via Ph. Eur. 5.1.10
    Lyophilised injectionSub-visible particulate matterUSP <788> / Ph. Eur. 2.9.19≥10 µm: ≤6000; ≥25 µm: ≤600 per container

    Fluid-bed top-spray granulation of a 45 wt% bovine bile extract composition with lactose monohydrate 30 wt% and pregelatinized starch 15 wt% using a 5% povidone K30 solution sprayed at 8–12 g/min per 2.0 kg batch yields granules with D50 180–250 µm when the inlet air temperature is held at 60°C ± 5°C and the product temperature is kept at 32–36°C. The terminal unit is a single-dose sachet containing 1.0 g granules for reconstitution in 10 mL water; xanthan gum 0.3 wt% and sucralose 0.15 wt% are dry-mixed into the granule blend as suspending and taste-masking agents. The process boundary is the spray rate: below 8 g/min the bed dewets and generates fines below 75 µm that segregate in the holding hopper, while above 12 g/min binder accumulates around the nozzle and causes local defluidization. Loss on drying of the finished granules is held at ≤1.5% to prevent compaction and caking in high-density polyethylene stick packs during storage at 25°C/60% RH. Uniformity of mass is tested under USP <905> or Ph. Eur. 2.9.5 with an acceptance value ≤15.0; particle size is controlled by USP <786> or Ph. Eur. 2.9.38 sieve analysis. The terminal product is an oral granule for bile acid supplementation in patients who cannot swallow intact tablets or capsules; the reconstituted suspension must be administered immediately after shaking because the surface-active bile salts generate persistent foam.

    Shifting From Oral Blend to Lyophilised Injectable Powder Replaces USP <905> With USP <788>

    Parenteral use of bovine bile extract imposes a different control set from oral granulation. The extract is dissolved in Water for Injections at 20–25°C, and the solution is adjusted to pH 7.0–7.4 with dilute sodium hydroxide or phosphate buffer to keep conjugated bile salts ionized. The solution is prefiltered through a 0.45 µm polypropylene membrane and sterilized through a 0.22 µm PVDF membrane. Because bile salts are surface-active, the filter train is operated at a constant differential pressure below 0.8 bar to reduce micellar gel formation at the membrane surface. The filtered solution is filled into Type I glass vials and lyophilized: freezing to −40°C at 0.5°C/min, primary drying at −20°C shelf temperature and 100 µbar chamber pressure for 24 h, secondary drying at 20°C until Karl Fischer moisture is ≤1.0%. The dry cake is reconstituted with 0.9% NaCl or Water for Injections immediately before administration. Compendial controls shift to USP <788> or Ph. Eur. 2.9.19 for sub-visible particles: counts must not exceed 6000 per container at ≥10 µm and 600 per container at ≥25 µm for small-volume parenterals. Bacterial endotoxin limits are calculated under USP <85> or Ph. Eur. 2.6.14 using the default intravenous threshold of 5 EU/kg/h under Ph. Eur. 5.1.10, adjusted for maximum dosing rate. Elemental impurity limits follow ICH Q3D for the parenteral route. Because free bile acids are membrane-active surfactants, injectable development requires product-specific in vitro hemolysis testing; the critical micelle concentration of sodium deoxycholate in isotonic saline at 25°C is commonly reported in the 2–6 mM range, but the crude bovine extract contains phospholipids and other amphiphiles that shift this aggregation boundary. Published data for this specific configuration is limited, and no oral-grade safety inference is acceptable. TSE control follows EMA/410/01 Rev. 3 and Ph. Eur. 5.2.8. The terminal product is a sterile lyophilised powder for injection, intended for reconstitution under aseptic conditions and not for terminal steam sterilization.

    When Enteric Coating Thickness Falls Below 7 mg/cm², Acid Uptake in the Stomach Triggers Premature Bile Acid Release

    Delayed-release tablet cores containing bovine bile extract are coated with Eudragit L 30 D-55 aqueous dispersion plasticized with triethyl citrate at 20% w/w dry polymer and talc at 50% w/w dry polymer. The side-vented coating pan is operated with inlet air at 45°C, product temperature 28–32°C, and spray rate 3–6 g/min/kg pan load until the coating weight gain reaches 8–10 mg/cm²; curing at 40°C for 2 h completes film coalescence. If coating thickness falls below 7 mg/cm², acid-stage testing in 0.1 M HCl shows more than 10% release within 2 h, indicating penetration through edge defects or surface porosity. This premature release exposes the gastric mucosa to bile acid fractions and removes the intended duodenal delivery. The acid-stage test uses USP <711> or Ph. Eur. 2.9.3 with 750 mL of 0.1 M HCl for 2 h; the buffer stage continues in phosphate buffer pH 6.8, where the methacrylic acid copolymer dissolves and release is evaluated against a product-specific acceptance criterion. Tablet cores from the wet-granulated route are compressed at 12–18 kN and the uncoated surface roughness is held below 0.8 µm Ra to prevent coating pinholes. The terminal product is a duodenal-release choleretic tablet intended to reduce gastric irritation and deliver bile extract to the proximal small intestine.

    Roller compaction of a 60 wt% bovine bile extract blend with microcrystalline cellulose 25 wt%, crospovidone 5 wt%, and magnesium stearate 0.5 wt% at roll force 6–8 kN/cm produces ribbons with a density of 0.8–1.2 g/cm³ when the pre-blend water activity is held below 0.35. Above 8 kN/cm the ribbons split along the axial plane and the subsequent milled granules contain excessive fines that increase tablet capping on a rotary press running at 30–60 rpm and 10–15 kN compression force. The dry granulation route is reserved for moisture-sensitive formulations in which wet granulation darkens the extract or shifts the conjugated bile acid profile; it removes the aqueous binder addition and reduces the drying thermal load. Ribbons are milled through a 1.0 mm screen, and the retained granule fraction between 125 µm and 500 µm is preferred for die filling. The final blend is compressed into tablets or filled into capsules. The dry-granulated material typically shows loss on drying ≤2.0%, angle of repose 35–40°, and acceptance value under USP <905> or Ph. Eur. 2.9.40 below 15. Terminal products are oral solid dosage forms for bile acid replacement in which the manufacturer must validate that dry granulation does not reduce bile acid assay through shear-induced segregation of phospholipid-rich fractions. Published data on the shear sensitivity of whole bovine bile extract is limited, so ribbon density and granule particle size must be correlated with assay and dissolution on a batch-specific basis.

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    Certification & Compliance
    More Introduction

    Bovine Bile Extract Pharma Grade API is a dried, purified bovine bile preparation supplied as a yellowish-brown amorphous powder or granular solid under product code BBE-PH-210 for oral solid dosage forms and BBE-PH-410 for injectable-grade applications. The material is not a single molecular entity; it is a natural multi-component mixture of conjugated and unconjugated bile acids, primarily glycocholic acid, taurocholic acid, cholic acid, and deoxycholic acid, together with minor fatty acid soaps, bile pigments, residual proteins, and insoluble cell debris. Pharmacopoeial control is based on total cholic acid equivalents because conjugated bile salts are hydrolyzed during the assay and reported as cholic acid. Industrial release uses high-performance liquid chromatography on a C18 column with an acetonitrile–phosphate buffer mobile phase at pH 3.0, quantifying cholic acid, glycocholic acid, taurocholic acid, deoxycholic acid, and chenodeoxycholic acid against external standards. Typical release data for model BBE-PH-210 show total bile acids as cholic acid in the range of 50.0–60.0%, with cholic acid between 40.0–55.0% and deoxycholic acid not more than 15.0% on the dried basis. The material is sourced under veterinary inspection from animals fit for human consumption and is controlled under TSE/BSE risk-minimization criteria described in EMA/410/01 Rev. 3 and Regulation (EC) No 1069/2009.

    The API is intended for use as a digestive surfactant in oral pancreatic enzyme replacement formulations, as an ingredient in tablets, capsules, and granules for oral suspension, and as a starting material for sterile injectable formulations where bile salt action is indicated. It is distinguished from technical-grade ox bile powder by the enforcement of elemental impurity limits per USP <232> and USP <233>, residual solvent limits per USP <467> and ICH Q3C, and microbial enumeration per USP <61>, USP <62>, and corresponding Ph. Eur. general chapters. Because the extract is a colloid-forming amphiphile mixture, its pharmaceutical behavior is governed less by molecular purity than by the ratio of free cholic acid to conjugated bile salts, the insoluble-matter fraction, and the micellar state after dissolution.

    What specification markers define a pharma-grade bovine bile extract?

    The release and stability specification is a matrix of pharmacopoeial tests rather than a single assay. The following table lists a typical manufacturer’s release specification for model BBE-PH-210; where a pharmacopoeial general chapter exists, it is cited as the control method. The injectable-grade model BBE-PH-410 applies additional endotoxin and sub-visible particulate controls.

    AttributeAcceptance criterionTest method / standardAdditional control
    AppearanceYellowish-brown to pale brown amorphous powder, free from visible foreign matterVisual inspectionColor comparator may be used
    IdentificationRetention times match cholic acid, glycocholic acid, taurocholic acid, and deoxycholic acid standardsHPLC-DAD; system suitability per USP <621>Unknown peaks >0.10% rejected for injectable grade
    Total bile acids as cholic acid50.0–60.0%HPLC-UV; USP <621>Dried basis
    Cholic acid40.0–55.0%HPLC-UVDried basis
    Deoxycholic acid≤15.0%HPLC-UVSum of free and conjugated forms
    Loss on drying≤5.0%USP <731> / Ph. Eur. 2.8.17105°C to constant weight
    Sulfated ash≤6.0%USP <281> / Ph. Eur. 2.4.14Indicates mineral residues
    Heavy metals≤20 ppmUSP <231> / Ph. Eur. 2.4.8Elemental impurities per ICH Q3D for injectable grade
    Arsenic≤2 ppmUSP <211> / Ph. Eur. 2.4.2Limits test
    Total aerobic microbial count≤1000 CFU/gUSP <61> / Ph. Eur. 2.6.12Bioburden before terminal sterilization
    Escherichia coli / SalmonellaAbsent in 10 gUSP <62> / Ph. Eur. 2.6.13Pathogen exclusion
    Bacterial endotoxins≤0.5 EU/mgUSP <85> / Ph. Eur. 2.6.14Applies to BBE-PH-410
    Residual solventsEthanol ≤5000 ppm; acetone ≤5000 ppm; Class 3 solvents per ICH Q3CUSP <467> headspace GCSolvents used in preparation
    Particle size, oral gradeD90 ≤150 µm; D50 50–90 µmLaser diffraction per ISO 13320-1:2020Wet dispersion in 0.1% polysorbate 80

    For oral solid dosage forms, the powder exhibits poor flow and hygroscopicity. Angle of repose typically exceeds 40°, and the compressibility index by USP <1174> falls between 25% and 35%, indicating passable-to-poor flow. Direct compression is therefore restricted to low-dose formulations in which the extract is spray-dried onto a mannitol or dibasic calcium phosphate carrier. Wet granulation is the standard route for tablet and capsule strengths containing more than 100 mg of extract per unit, because the binder matrix normalizes particle density and reduces segregation of the heterogeneous bile-derived solids.

    Tablet and capsule processing windows for bile acid-salt mixtures

    High-shear wet granulation of BBE-PH-210 uses a 5.0% w/w povidone K-30 binder solution prepared in purified water, with binder solution viscosity measured at 8–15 mPa·s on a Brookfield LV spindle at 60 rpm and 25°C. The binder is added at 5–10% of dry granulate mass in a high-shear mixer with impeller tip speed of 3–8 m/s and chopper speed of 1500–3000 rpm for 3–5 min. Granule moisture after fluid-bed drying with inlet air at 60–75°C and outlet air at 35–45°C is controlled to 1.5–2.5%. Milling through a 1.0 mm mesh is followed by blending with 0.02–0.05% butylated hydroxyanisole as antioxidant, 0.5–1.0% colloidal silicon dioxide as glidant, and 1.0–2.0% sodium stearyl fumarate as lubricant. Magnesium stearate above 1.0% is avoided because bile salts can interact with divalent cations and increase disintegration time or cause localized gelation.

    Compression is performed on a rotary tablet press using D-tooling with precompression of 8–15 kN and main compression of 20–45 kN. Tablet hardness is maintained at 60–120 N, friability at ≤0.8% per USP <1216>, and disintegration time at ≤15 min in water at 37°C per USP <701>. Ejection force should remain below 8 kN to avoid punch filming. When the granule moisture exceeds 2.5%, sticking to upper punches becomes a batch-rejection risk. Capsule filling on dosator or tamping-pin equipment requires encapsulation suites maintained below 40% RH, because the powder can increase moisture by 3–5% after 24 h at 25°C/75% RH. Fill weight variation is controlled to ≤5.0% per USP <905>. For granules in sachets, fluid-bed spray granulation using a Wurster insert with inlet temperature 65–75°C, spray rate 15–25 mL/min/kg, and final moisture ≤2.0% yields bulk density of 0.45–0.60 g/mL and tapped density of 0.55–0.75 g/mL, with Carr index ≤20%.

    Dissolution testing for tablets is conducted with USP apparatus II paddle at 75 rpm in 900 mL phosphate buffer at pH 6.8. Because unconjugated bile acids are poorly soluble at low pH, formulations containing 5–10% sodium bicarbonate or sodium carbonate provide a buffered microclimate and reduce variability. A release threshold of Q ≥75% at 45 min is typical for immediate-release oral solid dosage forms, but published data for this specific extract configuration is limited, and dissolution correlation should be generated batch-wise rather than extrapolated from single-entity bile acid monographs.

    Injectable processing of bovine bile extract requires stricter control than oral solid dosage. Model BBE-PH-410 is processed to reduce bacterial endotoxins to ≤0.5 EU/mg and to control sub-visible particles; it is not terminally sterilized in the dry state. The preferred route is aseptic dissolution in water for injection containing phosphate buffer to pH 7.0–7.5, followed by membrane clarification through 0.22 µm polyethersulfone filters. Mixed bile salts form micelles above approximately 2–8 mM, which increases filter throughput but can solubilize hydrophobic residues from the extract. Filter capacity is typically 10–20 L/m² for a 0.5% w/v solution at 25°C. Because the extract contains bile pigments and minor proteins, steam sterilization at 121°C for 15 min may increase solution color and raise free cholic acid by 2–5% of total bile acids via hydrolysis of glycine and taurine conjugates. Therefore liquid formulations intended for terminal sterilization should include a narrower initial cholic acid range and an assayed post-sterilization degradation profile.

    Difference vectors against single-entity bile acids, synthetic detergents, and other source species

    Compared with pharmacopoeial ursodeoxycholic acid of 98.0–102.0% purity and synthetic sodium deoxycholate of ≥98.0% purity, bovine bile extract is a deliberately heterogeneous API. Its primary regulatory identity is total cholic acid equivalents, not a single molecular purity. This creates a fundamentally different control strategy: the extract is standardized to a range, whereas single-entity APIs are controlled to tight purity windows. The extract also contains conjugated bile salts, which alter ionization, surfactant behavior, and thermal stability relative to unconjugated synthetic bile acids.

    AttributeBBE-PH-210 / BBE-PH-410Ursodeoxycholic acidSynthetic sodium deoxycholatePorcine bile extract
    Primary assayTotal cholic acid equivalents 50.0–60.0%; cholic acid 40.0–55.0%UDCA 98.0–102.0% on dried basisSodium deoxycholate ≥98.0%Total bile acids 40.0–55.0%
    Conjugation patternGlycocholic and taurocholic conjugates dominate; free cholic acid presentUnconjugatedUnconjugatedGlycine conjugates dominate; lower taurine fraction
    Primary pharmaceutical useDigestive surfactant; choleretic; injectable after purificationSpecific hepatobiliary therapyMicellar solubilizer; injection-grade detergentDigestive aid; enzyme supplement
    Critical control pointsCholic acid ratio, residual solvents, endotoxin, microbial limits, insoluble matterRelated substances, residual solventsRelated substances, endotoxin for injectionMicrobial burden, bile acid profile, heavy metals
    Typical oral dosage-form technologyWet granulation preferred; direct compression limitedDirect compression feasible after spray dryingNot routinely tableted as primary APICapsule or tablet blends

    Porcine bile extract differs from bovine bile extract in the relative abundance of glycine-conjugated bile acids and a lower taurine-conjugate fraction, which can affect solubility at acid pH and the dose-response behavior in pancreatic enzyme formulations. Ovine bile extract is less common in pharmaceutical use and may contain a different cholic acid-to-deoxycholic acid ratio. The pharma-grade bovine material is therefore specified by source species and by a defined window for cholic acid and deoxycholic acid, rather than by total bile acids alone.

    When terminal sterilization or alternative processing routes are required for liquid presentations

    Terminal steam sterilization of bile extract solutions is complicated by thermal degradation and precipitation. At pH 6.0, unconjugated deoxycholic acid may precipitate after cooling to 4–8°C; at pH 8.0, micelles are more stable but Type I glass vials may show surface delamination after prolonged exposure. If 121°C for 15 min is not feasible because of conjugate hydrolysis, sterile filtration through 0.22 µm polyethersulfone followed by aseptic filling into Type I glass vials is used, with media-fill qualification per EU GMP Annex 1 and USP <1116>. Lyophilization of a 1.0% w/v solution in 2% mannitol produces a brittle cake; the reconstituted solution can exceed sub-visible particle limits if the primary drying ramp exceeds 0.5°C/min. Published data for this specific bovine bile extract configuration is limited; filter capacity, lyophilization cycles, and post-sterilization cholic acid ratio must be validated per batch rather than extrapolated from single-entity bile salt solutions or porcine-derived extracts.

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