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

    • Product Name: Bovine Bile 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 615955
    Product Name Bovine Bile Pharma Grade API
    Source Bovine (Bos taurus) bile
    Grade Pharmaceutical grade (API)
    Cas Number 8008-63-7
    Appearance Yellow to brownish-green powder or granules
    Odor Characteristic bile odor
    Taste Bitter
    Solubility Soluble in water, alcohol, and alkaline solutions; slightly soluble in organic solvents
    Ph 6.5–8.5 (1% aqueous suspension/solution)
    Moisture ≤ 5.0%
    Ash ≤ 10.0%
    Heavy Metals ≤ 20 ppm
    Microbial Limits Total aerobic microbial count ≤ 10^3 CFU/g; yeast/mold ≤ 10^2 CFU/g
    Endotoxin ≤ 10 EU/mg (injectable grade)
    Sterility Sterile for injectable grade; non-sterile for oral solid dosage
    Assay Bile acids content 50–90% (as specified)
    Packaging 25 kg fiber drum with double polyethylene liner
    Storage Store in a cool, dry place, protected from light and moisture
    Shelf Life 24 months from date of manufacture
    Dosage Forms Tablet, capsule, granule, injection
    Route Of Administration Oral and injectable
    Regulatory Status Complies with relevant pharmacopeial requirements (e.g., USP/EP/BP as applicable)

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

    Direct compression of spray-dried bovine bile extract on high-speed rotary tablet presses is constrained by hygroscopicity and adhesive behaviour of bile acid-rich fractions under compression heat, especially when ambient relative humidity exceeds 60%. Standardised extract complying with the USP Ox Bile Extract monograph—not less than 45.0% total bile acids calculated as cholic acid and loss on drying not more than 6.0%—is blended with microcrystalline cellulose (25–45% w/w), dibasic calcium phosphate dihydrate (15–25% w/w), croscarmellose sodium (2–5% w/w), colloidal silicon dioxide (0.5–2.0% w/w), and magnesium stearate (0.5–1.5% w/w). The bile extract fraction is held at 20–35% w/w to prevent punch filming; batches above 35% w/w exhibit sticking on D-tooling punches at press speeds exceeding 60,000 tablets/h. Blending in a bin blender at 10–20 rpm for 15–25 min is followed by compression at 8–18 kN main compaction force, pre-compression at 1–3 kN, tablet breaking force of 49–118 N (5–12 kp), and friability below 0.8% determined by USP <1216>. Content uniformity is assessed against USP <905>, and uncoated tablet disintegration in water at 37°C is not more than 30 min per USP <701>. Press rooms are maintained at 25°C and 35% RH because cores absorbing moisture above 4.0% w/w laminate during subsequent film coating. Terminal dosage forms include immediate-release oral tablets, film-coated oral tablets, and sub-coated cores for later enteric polymer application.

    What Limits Encapsulation Speed When Bile Acid Granules Are Roller-Compacted?

    Roller compaction is selected for bovine bile extract intended for capsule filling when the API fraction exceeds 30% w/w and direct compression flow becomes unacceptable due to poor bulk density and segregation. The dry granulation formula contains bovine bile extract at 30–50% w/w, microcrystalline cellulose 20–35% w/w, pregelatinised starch 10–20% w/w, crospovidone 2–4% w/w, and sodium stearyl fumarate 1–2% w/w. Granulation is performed on a roller compactor with hydraulic roll pressure 40–80 bar, roll speed 4–10 rpm, side sealing of the compaction zone, and milling through a 0.8–1.4 mm screen; ribbon density is controlled to 1.10–1.35 g/cm³. Encapsulation on dosator-type machines requires granule bulk density 0.55–0.75 g/mL, Carr index below 25%, and residual moisture 1.5–3.5% w/w. Filling speeds above 20,000 capsules/h on low-fill-weight capsules of 250–400 mg cause powder bridging at the dosing nozzle and unacceptable weight variation under high static charge. Hard gelatin shell moisture is maintained at 13–16%; HPMC shell moisture is maintained at 4–7% to limit embrittlement at 25°C/35% RH filling conditions. Dissolution testing per USP <711> with apparatus 2 at 50 rpm in pH 6.8 phosphate buffer is applied to confirm bile acid release; disintegration is not more than 15 min per USP <701>. Residual solvents and elemental impurities are controlled under USP <467> and ICH Q3D. Terminal dosage forms include hard gelatin capsules, HPMC vegetarian capsules, and capsules containing roller-compacted granules for enteric coating after filling.

    Fluid-Bed Spray Granulation of Bile Acid-Rich Fractions

    Wet granulation is used when bovine bile extract must be formulated into dispersible oral granules or unit-dose sachet powders with acceptable reconstitution behaviour. A hydroalcoholic binder of purified water and ethanol (70:30 v/v) containing polyvinylpyrrolidone K30 at 3–5% of dry granule mass is sprayed onto a substrate composed of lactose monohydrate and microcrystalline cellulose; the bile extract solids are dissolved or suspended to a level of 10–25% w/w of final granule mass. Top-spray fluid-bed equipment is operated with inlet air temperature 55–65°C, atomising air pressure 1.5–2.5 bar, and spray rate 12–25 g/min per kg substrate. The granulation endpoint is controlled by mean particle size 180–800 µm and loss on drying 1.5–3.0% w/w; residual moisture above 3.0% causes bed collapse and below 1.5% yields a fines fraction that segregates during sachet filling. Particle size distribution is verified by analytical sieving per USP <786>, and residual ethanol is limited by USP <467>. Effervescent variants are buffered with citric acid and sodium bicarbonate, requiring granule drying below 1.5% w/w to prevent premature reaction. Terminal dosage forms include oral granules in unit-dose sachets, flavoured dispersible granules, and enteric-coated granules retained for duodenal release.

    Process routeAPI fractionMoisture endpointCritical equipment parameterRelease test
    Direct compression20–35% w/w≤4.0% w/wMain compaction force 8–18 kNUSP <1216>, USP <905>
    Roller compaction–capsule fill30–50% w/w1.5–3.5% w/wHydraulic roll pressure 40–80 barUSP <701>, USP <711>
    Fluid-bed wet granulation10–25% w/w1.5–3.0% w/wInlet air temperature 55–65°CUSP <786>, USP <467>
    Enteric multiparticulate coating40–60% w/w on core≤2.0% w/w before coatingWurster product temperature 30–35°CUSP <711> acid/buffer stage

    Because bile acid salts remain soluble above pH 6.5 but precipitate in the fasting stomach at pH 1.0–3.5, multiparticulate enteric coating is required to prevent gastric aggregation and dose failure. Cores are prepared as microcrystalline cellulose spheres layered with bovine bile extract at 40–60% w/w of core weight and HPMC 5–8% w/w as binder; the drug layering is performed in a Wurster fluid bed at product temperature 30–35°C and spray rate 8–15 g/min/kg. A subcoat of HPMC 2–3% w/w is applied to separate bile acid salts from the enteric polymer and prevent acid-catalysed interaction. Enteric coating with Eudragit L30 D-55 or equivalent methacrylic acid-ethyl acrylate copolymer is applied to 8–12% w/w polymer solids, with triethyl citrate plasticiser at 10–20% of polymer solids and talc at 15–25% of polymer solids. Curing at 40°C and 50% RH for 24 h completes film coalescence and reduces tack during capsule filling. Dissolution testing per USP <711> uses acid stage 0.1 M HCl for 2 h with no more than 10% release, followed by pH 6.8 phosphate buffer where release exceeds 80% within 45 min. Terminal dosage forms include enteric-coated pellets filled into hard capsules, enteric-coated tablets, and enteric-coated granule sachets.

    Sodium Deoxycholate Injection, Where pH Drift Determines Yield

    Bovine bile fractionation routes that isolate deoxycholic acid monohydrate support a sterile injectable finished product at 10 mg/mL deoxycholic acid in water for injection. The formulation ratio is fixed at 10 mg/mL; higher concentrations increase micellar turbidity and filtration resistance, while lower concentrations require larger injection volumes. Sodium hydroxide is used as pH adjuster to a target pH of 8.3; pH below 7.8 precipitates free acid crystals and pH above 9.0 causes gelation. Dissolution is conducted in water for injection at 20–25°C under nitrogen sparging, with incremental sodium hydroxide addition to avoid pH overshoot above 9.0. Aseptic filtration through 0.22 µm PVDF membranes is performed in a Grade A/RABS line; filling into Type I borosilicate glass vials with chlorobutyl stoppers is followed by visual inspection per USP <1> and visible particulate control per USP <790>. Bacterial endotoxin testing per USP <85> and sterility testing per USP <71> are release criteria; manufacturing complies with FDA 21 CFR 211 and EU GMP Annex 1. Terminal dosage form is a sterile injectable solution administered subcutaneously for adipolysis.

    When Micronised Cholic Acid From Bovine Bile Challenges Content Uniformity In Low-Fill Capsules

    Cholic acid obtained by saponification, crystallisation, and purification of bovine bile is formulated into capsules in 50 mg and 250 mg strengths for bile acid replacement therapy. The API fraction is dependent on capsule strength: a 50 mg capsule with fill weight 150–200 mg contains 25–33% w/w cholic acid, while a 250 mg capsule with fill weight 400–500 mg contains 50–62.5% w/w cholic acid. Excipients include lactose monohydrate 30–50% w/w, microcrystalline cellulose 20–40% w/w, sodium starch glycolate 2–5% w/w, and magnesium stearate 0.5–1.5% w/w. Jet milling reduces particle size to D90 below 20 µm, which is critical for blend uniformity and dissolution of the low-strength capsule. Blending is performed in a V-blender at 15–20 rpm for 20–30 min, with fill weight verified at intervals of 10–15 min during capsule filling. Content uniformity follows USP <905>; dissolution testing per USP <711> and disintegration per USP <701> are applied to release. Residual solvents and elemental impurities are controlled under ICH Q3C and ICH Q3D. Terminal dosage forms include cholic acid capsules in 50 mg and 250 mg strengths for bile acid synthesis disorders and related oral replacement indications.

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    Certification & Compliance
    More Introduction

    Bovine bile pharma grade API, released under the model designation BB-PhG-OI, is a dried purified mixture of bile acids and their glycine/taurine conjugates obtained from Bos taurus bile collected under veterinary hygiene. The OI suffix denotes a dual-route grade that meets solid oral dose and sterile injectable readiness criteria. The material is standardized to total bile acids not less than 45% as cholic acid on the dried basis, supplied as an amorphous powder with a laser-diffraction particle size of D90 ≤ 150 µm, and offered as a lyophilized cake with bacterial endotoxin below 0.5 EU/mg for aqueous compounding. The product is intended for tablet, capsule, granule, and injectable formulation routes as a pharmaceutical active ingredient rather than a technical-grade bile salt or diagnostic reagent.

    Compliance and Specification Matrix
    ParameterAcceptance RangeTest Method / Standard
    AppearancePale yellow to light brown amorphous powder; lyophilized cake for injectable gradeVisual inspection
    IdentificationInfrared spectrum consistent with reference; HPLC retention times match bile acid profilePh. Eur. 2.2.24, in-house HPLC
    Total bile acidsNLT 45% w/w dried basisEnzymatic-colorimetric / HPLC
    Cholic acid familyNLT 45% dried basisHPLC
    Deoxycholic acid family10–25% dried basisHPLC
    Chenodeoxycholic acid family2–8% dried basisHPLC
    Lithocholic acid family≤2.0% dried basisHPLC
    Loss on drying≤5.0%Ph. Eur. 2.2.32
    pH of 10% aqueous solution6.0–8.0Ph. Eur. 2.2.3
    Bulk density0.35–0.60 g/mLUSP <616>
    Particle sizeD90 ≤ 150 µm; D50 45–75 µmISO 13320-1:2020
    Elemental impuritiesPb ≤5 ppm, As ≤3 ppm, Cd ≤1 ppm, Hg ≤0.1 ppmUSP <233>
    Residual solventsClass 3 total ≤0.5%USP <467>
    Microbial limits, oral gradeTAMC ≤1000 CFU/g; TYMC ≤100 CFU/g; bile-tolerant Gram-negative bacteria absent in 1 gPh. Eur. 2.6.13
    Bacterial endotoxin, injectable grade<0.5 EU/mgPh. Eur. 2.6.14
    Sterility, injectable gradeSterilePh. Eur. 2.6.1

    What Distinguishes This API from Single-Molecule Bile Acid Reference Standards?

    Unlike purified cholic acid, chenodeoxycholic acid, or ursodeoxycholic acid, this material is not a single molecular entity. The conjugated and unconjugated bile acid composition changes the ionization profile; the unconjugated cholic acid pKa is 4.98, while glycine and taurine conjugates possess pKa values near 3.9 and 1.5, respectively. In aqueous media above pH 6.0, the material remains largely ionized and forms mixed micelles. The critical micelle concentration of the mixture is lower than that of pure sodium cholate, which is reported in the range 9–13 mM, because dihydroxy bile salt components have CMC values in the range 2–6 mM. This difference affects dissolution testing, biorelevant media design, and filter-membrane behavior of injectable solutions.

    Compared with porcine bile, bovine bile is characterized by cholic acid and deoxycholic acid as dominant components, whereas porcine bile contains appreciable hyocholic acid and hyodeoxycholic acid. The species difference is analytically significant: compendial identification and assay methods for bile acid profiles are not interchangeable. Bovine bile composition is closer to the human bile acid pool than porcine material for certain in vitro dissolution applications because human bile contains cholic acid, chenodeoxycholic acid, and deoxycholic acid; however, the glycine-to-taurine conjugation ratio differs from human bile. For regulatory submissions, the API is treated as a complex biological material rather than a chemically synthesized single entity.

    Comparative Bile Acid Profiles by Species
    SpeciesDominant Bile AcidsProcess and Formulation Impact
    BovineCholic acid, deoxycholic acid, chenodeoxycholic acid, lithocholic acidLower mixed-micelle CMC due to dihydroxy components; higher detergent capacity in dissolution media
    PorcineHyocholic acid, hyodeoxycholic acid, chenodeoxycholic acidDifferent ionization and micellization; not interchangeable in compendial bile acid assays
    HumanCholic acid, chenodeoxycholic acid, deoxycholic acidReference composition for biorelevant media; bovine profile closer than porcine for some release assays

    Direct compression and wet granulation routes both require control of moisture, flow, and particle size. In oral solid dosage forms, the API is used at loadings from 10% to 60% w/w, depending on the desired cholic acid dose. For direct compression, the powder is typically blended with microcrystalline cellulose PH102, croscarmellose sodium at 2–4%, colloidal silicon dioxide at 0.5–1.0%, and magnesium stearate at 0.75%, then compressed on a rotary tablet press with 9 mm round flat-faced tooling at 8–15 kN. Potency uniformity is assessed by USP <905>. For capsules, the blended material is filled into hard gelatin or HPMC shells at fill weights calculated from the lot assay; because the API is hygroscopic, the filling suite is maintained at 25 °C and 30–35% RH to prevent moisture transfer to the shell. For granulation, a 10 L high-shear mixer with impeller speed 300 rpm and wet massing time 60–120 s is used; purified water or 50% ethanol is added at 10–20% w/w. Higher water levels above 25% w/w produce an over-wetted mass because of the surfactant character of bile salts, causing torque rise and poor granule size distribution. Granules are tray-dried at 40 °C with forced air to loss on drying 1.5–3.0% before lubrication.

    High-Shear Dispersion, Dry Binder Activation, and Moisture Transfer Points

    Particle size control is maintained at D90 ≤ 150 µm with a D50 of 45–75 µm by laser diffraction per ISO 13320-1:2020. The powder exhibits a Hausner ratio of 1.25–1.45, indicating intermediate flow; 0.5–1.0% colloidal silicon dioxide is added before direct compression to reduce interparticulate friction. Dynamic vapor sorption data show that water uptake exceeds 5% at 60% RH and 10% at 75% RH within 24 h; pre-drying is therefore required at processing relative humidity above 60%. Contract production runs with ox bile extract blends indicate that sticking on rotary tablet tooling becomes operationally significant when powder moisture exceeds 4.5% w/w. At tablet hardness 50–80 N, disintegration time by Ph. Eur. 2.9.1 remains ≤15 min when croscarmellose sodium is present at 2–4%. During high-shear aqueous granulation, mixer torque rises by 20–30% over the dry-mix baseline when granulating fluid reaches 15% w/w; at 25% w/w the mass may overwet and require extended drying, a processing conflict that limits the aqueous granulation window.

    For low-dose tablet and capsule formulations, the API is geometrically diluted with a carrier such as lactose monohydrate or microcrystalline cellulose in a bin blender at 15 rpm for 10 min before final blending. Content uniformity is verified on stratified samples using USP <905>. Tablet friability is controlled to ≤0.8% by Ph. Eur. 2.9.7 or USP <1216>. Capsule disintegration is controlled to ≤15 min by Ph. Eur. 2.9.1 for immediate-release design.

    When Lyophilized Injectable Grade Must Meet Sub-Visible Particulate and Endotoxin Limits

    The injectable grade is released as a lyophilized cake and reconstituted in Water for Injection. Bacterial endotoxin is controlled to <0.5 EU/mg by Ph. Eur. 2.6.14; the solution is filled aseptically after sterilizing-grade filtration through 0.22 µm PES or PVDF membranes. Because the mixed bile salts aggregate into micelles, aqueous solutions above 5% w/v demonstrate increased viscosity and may reduce membrane throughput; a 0.45 µm prefilter is recommended before the sterilizing-grade filter. Published stability data for terminal steam sterilization of aqueous bovine bile formulations above 5% w/v are limited; therefore, aseptic filtration rather than autoclaving is the default route for injectable processing. Solution pH is maintained at 6.5–7.4; acidification below 4.98 leads to phase separation of unconjugated bile acids. Sub-visible particulate matter is controlled by USP <788>. In injectable compounding, avoid polyvalent metal ions and strongly cationic excipients at acidic pH because anionic bile salts can form insoluble complexes. The maximum recommended calcium ion concentration in the finished solution is 2 mM unless compatibility has been demonstrated by a product-specific study.

    Because the API is hygroscopic and contains bile salt micelles, packaging must include an aluminum foil laminate overwrap with silica gel desiccant. The sealed container is stored at 2–8 °C. For oral processing, the powder is conditioned at 25 °C and 30% RH for 4–6 h before weighing. The material is incompatible with strong oxidizing agents. In solid and liquid formulations, avoid simultaneous use of high concentrations of divalent metal ions unless a deliberate precipitation or complexation study has been conducted. The oral grade and injectable grade are not interchangeable because the injectable grade imposes additional endotoxin, sterility, and sub-visible particulate specifications.

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