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

    • Product Name: OX 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 471948
    Product Name OX Bile Extract Pharma Grade API
    Synonyms Ox Bile Extract; Oxgall; Bile Extract; Purified Ox Bile; Bovine Bile Extract
    Grade Pharma Grade / API Grade
    Dosage Forms Tablet; Capsule; Granule; Injection
    Routes Of Administration Oral; Injectable
    Source Bovine (ox) bile
    Appearance Brownish-yellow to greenish-brown powder
    Odor Characteristic bile odor
    Taste Bitter
    Solubility Soluble in water; partially soluble in ethanol; practically insoluble in ether
    Ph 6.0 to 8.0 (aqueous solution)
    Assay Total bile acids typically 45.0% to 55.0% calculated as cholic acid
    Identification Positive bile acid identification by TLC or HPLC
    Loss On Drying ≤ 5.0%
    Residue On Ignition ≤ 10.0%
    Heavy Metals ≤ 20 ppm
    Microbial Limits Total aerobic microbial count ≤ 10^3 CFU/g; yeast and mold ≤ 10^2 CFU/g; E. coli absent
    Sterility Sterile for injectable grade; non-sterile for oral solid dosage grade
    Endotoxin ≤ 0.25 EU/mg for injectable grade
    Storage Store in tight, light-resistant containers at controlled room temperature; protect from moisture
    Shelf Life 24 to 36 months when stored as directed
    Cas Number 8008-63-7
    Einecs Number 232-369-0
    Packaging Fiber drum with double polyethylene liner; sterile pack for injectable grade
    Regulatory Status Manufactured under cGMP; USP/NF, EP, or customer specification as applicable
    Animal Derived Yes
    Bse Tse Risk Controlled bovine source; TSE/BSE statement available

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

    Granular ox bile extract with a compacted particle size distribution is transferred from double polyethylene-lined drums into a calibrated cone mill fitted with a 0.5 mm round-hole screen; oversize aggregates retained above 0.8 mm are returned to the mill until the entire batch passes the screen. Direct-compression blends containing 150–300 mg of ox bile extract per unit are prepared by pre-blending the milled API with colloidal silicon dioxide at 0.5% w/w and microcrystalline cellulose for 10 minutes in a 600 L V-blender at 25 rpm. Croscarmellose sodium is then added and mixed for an additional 8 minutes. Magnesium stearate 0.25–0.5% w/w is introduced last and mixed for only 2 minutes at 15 rpm, because prolonged lubrication reduces tablet tensile strength and increases disintegration variability in direct-compression formulations of this API. The final blend is compressed on an instrumented rotary press with 10.5 mm round flat-faced bevel-edge tooling. Compression force is adjusted to achieve crush strength between 49 N and 98 N; friability assessed by USP <1216> is maintained below 1.0% to avoid edge chipping during film coating. Disintegration is measured in purified water at 37±2°C per USP <701>; the acceptance criterion is linked to the finished product monograph and is commonly not more than 30 minutes for uncoated tablets. Dissolution testing per USP <711> is conducted in 900 mL phosphate buffer pH 6.8 with 0.5% w/v polysorbate 80 to maintain sink conditions, because bile salts form micelles that can otherwise suppress free dissolution and produce high foam volume in the vessel.

    How does moisture ingress during high-speed capsule filling alter fill weight stability?

    Ox bile extract is hygroscopic; incoming bulk powder with loss on drying exceeding 5.0% w/w as measured by infrared moisture balance at 105°C is associated with adhesion to dosator pins and non-uniform slug formation on intermittent-motion capsule machines. The powder is dried in a vacuum tray dryer at 45°C under 25 mbar until loss on drying falls below 3.0% w/w. Hard HPMC capsules are selected preferentially over gelatin because the low equilibrium moisture of HPMC shell reduces brittle fracture at relative humidity below 40% and prevents shell softening at relative humidity above 60%. On a dosator-type capsule filler, fill weight repeatability is monitored at 15-minute intervals using a checkweigher; acceptance is set at not more than 3.0% relative standard deviation for a 250 mg fill. Dosator pin height is adjusted so that the compressed powder bed height remains between 5.0 mm and 7.0 mm; increasing powder bed height beyond 8.0 mm causes over-compaction and delayed disintegration. The filled capsules are placed in HDPE bottles with silica gel desiccant canisters; headspace relative humidity is held below 25% during storage. Disintegration of the filled capsules is assessed by USP <701> with a wire spiral; because bile extract can promote foam in the disintegration medium, the addition of polysorbate 80 is permitted only if specified in the finished product monograph. Published data for specific fill-weight drift at production speeds above 100,000 capsules/hour using crude ox bile extract is limited, so parameter ranges are established on the qualified machine.

    Granulation and enteric coating of sachet-strength ox bile extract granules

    Water-based wet granulation of ox bile extract is avoided because the API forms a sticky mass in the presence of aqueous binders at granulation temperatures above 35°C. Dry granulation by roller compaction is performed on a vertical roller compactor with ribbed rolls; the compacted ribbon is milled through a 0.8 mm screen. Granules with a targeted size fraction between 0.25 mm and 0.85 mm are collected; fines below 0.25 mm are recycled at a rate not exceeding 15% of total batch weight to avoid excessive dust and segregation. The granules are coated in a bottom-spray fluid bed with methacrylic acid–ethyl acrylate copolymer dispersion, triethyl citrate plasticizer at 10–15% of dry polymer solids, and talc anti-tack. Coating weight gain between 8% and 10% is required to obtain acid resistance; acid-stage dissolution in 900 mL 0.1 M hydrochloric acid for 2 hours shows not more than 10% release, followed by buffer-stage release in 900 mL phosphate buffer pH 6.8. The delayed-release profile is checked by USP <711> with a basket speed of 100 rpm and sinker. Sachet filling is conducted on a vertical form-fill-seal machine at 25°C and relative humidity below 35%; each sachet contains 1.0 g or 2.0 g of enteric-coated granules. In-process fill weight tolerance is ±5.0% per sachet. Because bile extract granules are susceptible to electrostatic charging, an ionising bar is positioned at the sachet forming tube to reduce weight variation caused by granule cling.

    Oral liquid forms of ox bile extract present simultaneous challenges of bitter taste, foam generation, and photolytic discolouration. Reconstitution from granules at the point of dispensing is preferred over multi-dose aqueous liquids because the API degrades in aqueous solution faster than in dry granule form. When reconstitution is specified, purified water at 40°C is added to a target volume of 50 mL; water hardness above 120 mg/L calcium carbonate equivalents is avoided because divalent cations can interact with bile salt micelles and produce turbidity. Polysorbate 80 at 0.1% w/v may be added under mixing at 300 rpm for 5 minutes; the solution is then dosed immediately. Foam generation during mixing is controlled with simethicone emulsion at 0.2% v/v, and the vessel is filled to a pre-calibrated mark to avoid headspace-dependent foam rise. The reconstituted liquid is stored in amber glass bottles protected from light; bile pigments in ox bile extract are light-sensitive and darkening occurs when exposed to ultraviolet light at 365 nm for more than 24 hours. Chemical stability is assessed by total bile salt assay; a drop of more than 5.0% from initial assay is considered out-of-trend. The dose is administered through an oral syringe and should be consumed within 30 minutes, because microbial proliferation in a non-preserved reconstituted liquid exceeds 10 CFU/mL at ambient temperature after 2 hours. If preservative is required for multi-dose packaging, potassium sorbate 0.1% w/v and sodium benzoate 0.1% w/v are added before pH adjustment to 5.5.

    When injectable-grade ox bile extract is specified, particulate-control and haemolysis testing must define the process boundary

    Crude ox bile extract intended for parenteral administration differs fundamentally from oral-grade material. Animal-derived API must be accompanied by viral safety documentation and TSE/BSE country-of-origin certification; purification steps are typically validated for removal of proteinaceous impurities and bile pigments using activated carbon treatment followed by membrane filtration. Injectable solutions are prepared in a Grade A laminar airflow with Grade B background per EU GMP Annex 1; the product is passed through a 0.22 μm PVDF membrane filter. Because bile salts are surface-active and can form visible particulates upon pH adjustment, pH is controlled at 7.0–7.4 with phosphate buffer. Bacterial endotoxin is measured by USP <85>; the limit is derived from the maximum bolus dose using the formula K/M, where K is set at 5 EU/kg for intravenous non-intrathecal products. The resulting product-specific endotoxin limit for the API is therefore dose-dependent, not a fixed value. Particulate matter is evaluated by USP <788> light obscuration particle count; limits for small-volume injections are not more than 6000 particles per container for ≥10 μm and not more than 600 particles per container for ≥25 μm. In vitro haemolysis testing is mandatory because bile salts can lyse erythrocytes at concentrations above their critical micellar concentration. Samples incubated with rabbit or human erythrocytes at 37°C for 60 minutes must show not more than 2.0% haemolysis at the proposed clinical concentration. If terminal steam sterilisation at 121°C for 15 minutes is evaluated, degradation products and colour change must be monitored against the unsterilised control. Published data for specific injectable formulations using crude ox bile extract are limited; product development therefore requires additional preclinical safety qualification.

    Fixed-dose digestive enzyme combinations require separated granule fractions before final blending

    Ox bile extract is co-formulated with pancreatin or pepsin in solid oral dosage forms for digestive enzyme replacement and choleretic indications. Because bile salts are amphiphilic and can reduce enzyme activity in wet mass, the enzyme component and bile extract component are granulated separately. Pancreatin is dry-blended with lactose monohydrate and cellulose, compacted, and milled to a particle size fraction of 0.25 mm to 0.71 mm; the bile extract component is dry-granulated as described above. The two granule fractions are combined in a low-shear tumble blender at 15 rpm for 20 minutes. Segregation risk is minimised by matching bulk density within 0.10 g/mL and by filling capsules or tablets immediately after blending. Enzyme activity is assayed by USP pancreatin monograph methods; lipase activity is determined by tributyrin titration, amylase by starch substrate, and protease by casein digestion. Stability studies under ICH Q1A conditions at 40°C and 75% RH are used to establish whether the bile extract causes activity loss; when lipase activity drops more than 10% from initial, the enzyme fraction is protected with an enteric coating before blending. Tablets are compressed with a low compression force to avoid enzyme denaturation; capsule filling is performed at room temperature below 25°C because pancreatic enzymes degrade rapidly above 30°C. The final product must meet USP <905> uniformity of dosage units; the acceptance value is not more than 15.0.

    Representative compendial and in-process test methods for ox bile extract dosage forms
    Dosage formAttributeMethod or standardTypical acceptance or operational limit
    Oral tabletDisintegrationUSP <701>Purified water, 37±2°C, not more than 30 min
    Oral tabletDissolutionUSP <711>900 mL phosphate buffer pH 6.8, 0.5% w/v polysorbate 80
    Oral tabletFriabilityUSP <1216>Not more than 1.0%
    CapsuleFill weight variabilityIn-process checkweigherRSD not more than 3.0% at 250 mg fill
    GranuleAcid resistanceUSP <711>0.1 M HCl, 2 h, release not more than 10%
    InjectionBacterial endotoxinsUSP <85>Dose-derived K/M, K = 5 EU/kg
    InjectionParticulate matterUSP <788>6000/container at ≥10 μm; 600/container at ≥25 μm
    InjectionHaemolysisIn vitro erythrocyte assayNot more than 2.0% at clinical concentration
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    Certification & Compliance
    More Introduction

    Ox Bile Extract Pharma Grade API, designated OBE-PG-450 for oral solid dosage forms and OBE-IP-450 for injectable processing, is a dried bovine bile derivative standardized to a minimum cholic acid content of 45.0% on the dried basis. The material is supplied as an off-white to light tan hygroscopic powder with a characteristic bitter taste and contains the native conjugated bile acid profile of Bos taurus bile, principally glycocholic and taurocholic acids with minor deoxycholic and chenodeoxycholic acid conjugates. Solubility in purified water at 25°C is pH- and concentration-dependent; clear micellar dispersions form above the critical micellar concentration, while unconjugated cholic acid may precipitate below pH 4.0. The oral grade is controlled for identity by thin-layer chromatography, cholic acid assay by high-performance liquid chromatography with detection at 210 nm, loss on drying by USP <731>, residue on ignition by USP <281>, and microbial enumeration by USP <61> and USP <62>. The injectable grade is further processed to reduce bacterial endotoxin to ≤0.5 EU/mg, aseptically filtered, and tested for sterility by USP <71>. The oral and injectable grades are not interchangeable because the injectable grade carries tighter bioburden, bacterial endotoxin, and particulate matter controls.

    Final dosage forms include tablets, capsules, granules for oral suspension, and injectable solutions. In oral solid dosage forms, the API is used for bile acid replacement and digestive support; in injectable forms, the mixed conjugate system provides micellar solubilization of lipophilic actives. Unit strength is calculated as cholic acid equivalent after assay correction, rather than as a fixed powder weight. This is a critical difference from synthetic bile salts, which are dispensed as a single chemical entity.

    Specification Profile and Pharmacopoeial Anchoring

    ParameterOBE-PG-450 oral gradeOBE-IP-450 injectable gradeTest method
    AppearanceOff-white to light tan hygroscopic powderWhite to off-white lyophilized powderVisual examination
    Cholic acid content≥45.0% on dried basis≥45.0% on dried basisHPLC with UV detection at 210 nm
    Loss on drying≤5.0%≤3.0%USP <731>
    Residue on ignition≤8.0%≤5.0%USP <281>
    pH of 1% aqueous dispersion5.0-7.06.5-7.8Potentiometric, 25°C
    Microbial limitsTotal aerobic count ≤10³ CFU/g; bile-tolerant Gram-negative bacteria absentSterile; tested by USP <71>USP <61>, USP <62>
    Bacterial endotoxinNot specified for oral≤0.5 EU/mgUSP <85>
    Particle sizeD90 ≤150 µmD90 ≤100 µmLaser diffraction
    Elemental impuritiesConforms to ICH Q3D Option 1; lead ≤0.5 ppm, cadmium ≤0.2 ppm, mercury ≤0.1 ppm, arsenic ≤1.5 ppmUSP <233>
    Residual solventsEthanol ≤0.5%; Class 3 solvents onlyUSP <467>

    These values represent release targets for pharmaceutical use and are not intended for food-grade or technical-grade bile powders. The manufacturing dossier for both grades is maintained under FDA 21 CFR 211 for finished pharmaceuticals and ICH Q7 for active pharmaceutical ingredients. Because the extract is of animal origin, viral safety and transmissible spongiform encephalopathy documentation are provided according to EMEA/410/01 Rev. 3. The HPLC assay uses a C18 column with a phosphate buffer/acetonitrile gradient and UV detection at 210 nm. System suitability requires resolution between glycocholic acid and taurocholic acid not less than 2.0, with injection precision not more than 2.0% RSD. The method is stability-indicating and separates free cholic acid from its glycine and taurine conjugates.

    What Distinguishes Ox Bile Extract from Synthetic Bile Acid Salts in Solid Oral Dosage Forms?

    Synthetic sodium deoxycholate and sodium cholate are single-molecular entities with pharmacopoeial assays based on purity of one analyte. Ox bile extract is a polydisperse mixture of conjugated and free bile acids, so release relies on chromatographic fingerprint and total cholic acid content. This compositional difference changes processing behaviour in several ways. The mixed conjugated system lowers the effective critical micellar concentration relative to sodium cholate; published CMC values for sodium cholate in 0.15 M sodium chloride at 25°C are typically 9-15 mM, while the extract forms micellar aggregates over a broader concentration range. Precise CMC shift for the natural mixture is batch-specific; published data for this specific configuration is limited. The extract contains both glycine and taurine conjugates, which maintain ionization across a wider pH range than free cholic acid, but the free acid fraction can still produce clouding below pH 4.0. The extract is also more hygroscopic than spray-dried synthetic sodium deoxycholate, so tablet and capsule formulations require moisture-protective packaging above RH 60%.

    AttributeOx bile extract OBE-PG-450Synthetic sodium deoxycholatePorcine bile extract
    CompositionMixture of glycine/taurine conjugates and free bile acidsSingle bile saltMixture with hyodeoxycholic acid-dominant profile
    Critical micelle behaviourBroad aggregation range; mixed micellesSharp CMC, typically 2-6 mM in 0.15 M NaClMixed micelles; different bile salt ratio
    Pharmacopoeial release markerCholic acid content ≥45.0%Assay ≥98.0% on dried basisHyodeoxycholic acid content
    Processing riskHygroscopic, bitter, requires humidity controlLess hygroscopic; high-pH solutions can attack certain film coatsHygroscopic; porcine-specific odor

    Porcine bile extract is sometimes used as an alternative biological mixture, but its bile acid profile contains higher relative proportions of hyodeoxycholic acid; this changes the solubilization capacity for lipophilic actives. For a reproducible single-component surfactant, synthetic sodium deoxycholate is preferred. For physiological bile salt replacement, the multicomponent ox extract is selected because it more closely mirrors endogenous bile acid composition. The release of ox bile extract must nevertheless include a viral safety and TSE statement; synthetic bile salts do not carry this biological risk profile.

    During wet granulation of OBE-PG-450 in a top-spray fluid-bed granulator, product moisture and exhaust humidity are controlled separately because the bile salts absorb moisture above RH 60% and form a cohesive mass that can block distributor plates. Aqueous binder solutions are prepared with purified water at 20-25°C; binder temperatures above 30°C increase bile salt solubility and produce denser granules with higher compression friability. In high-shear granulation, the endpoint is controlled by impeller torque rather than fixed time: a torque rise of 25-35% over dry mix baseline typically corresponds to a granule D50 between 120 µm and 180 µm when the bowl is charged to 70% of swept volume. These ranges are equipment-dependent; published data for this specific configuration is limited, and development batches require torque mapping. The wet mass is screened through 1.0 mm and dried at inlet air temperature not exceeding 45°C to prevent surface case-hardening.

    Roller compaction is selected for moisture-sensitive formulations. A blend of OBE-PG-450, microcrystalline cellulose, croscarmellose sodium, and colloidal silicon dioxide is compacted at roll pressure 4-6 kN/cm on a 25 cm roll diameter compactor and milled through 1.0 mm. Ribbon porosity is kept between 20% and 30% to reduce fines that segregate in the tablet press feed frame. Final lubrication with 0.5% w/w sodium stearyl fumarate replaces magnesium stearate; magnesium stearate above 1.0% w/w retards release of the bile salt matrix in USP <711> dissolution testing.

    Tablets compressed to hardness 60-90 N on a rotary press show disintegration times below 15 minutes in 900 mL phosphate buffer at pH 6.8 and 37°C by USP <701>. The cores are seal-coated with hydroxypropyl methylcellulose at 5-8% weight gain to reduce bitter aftertaste and to restrict moisture uptake; coating pan exhaust temperature is held at 30-35°C because higher product temperatures soften the bile salt-containing core and increase edge wear. Two-piece hard gelatin capsules are filled with granules rather than direct powder blends because the hygroscopic API clogs powder hoppers above 40% RH; on dosator-style capsule fillers, the dosing disk is cleaned after each shift because bile salt fines adhere to stainless steel.

    Granules for oral suspension are dispersed in water immediately before administration. Standing aqueous suspensions at 25°C for longer than 2 hours can develop a viscous micellar phase, and dosing accuracy decreases if the dispersion is not stirred after standing. Final blend flowability for stick-pack filling is characterized by Carr index below 25, with particle size matching between the API granulate and lactose to prevent segregation.

    Stability studies for both grades are conducted at 25°C/60% RH and 40°C/75% RH. Oral grade bulk powder requires desiccant when packaged product is stored above 30°C. The injectable grade is evaluated under ICH Q1A conditions; pH and micelle size are monitored because a shift in micelle size can alter filterability and product consistency.

    When the API Is Processed for Injectable Dosage Forms

    For injectable use, OBE-IP-450 is reconstituted in Water for Injection at a total bile salt concentration of 20-50 mg/mL. The resulting system is a micellar dispersion rather than a simple molecular solution; dynamic light scattering shows average micelle hydrodynamic diameters of 5-10 nm, but aggregates larger than 200 nm can form when pH and ionic strength are uncontrolled. Sterile filtration through 0.22 µm polyethersulfone membranes can retain these aggregates, so filtration is preceded by pH adjustment and ionic strength control. The solution is aseptically filtered and filled into Type I borosilicate vials under Grade A conditions. Terminal steam sterilization at 121°C for 15 minutes is not recommended because taurine conjugates may hydrolyze and increase free cholic acid; if terminal sterilization is unavoidable, the impurity profile must remain within specification.

    Depyrogenation before sterile filtration is performed by anion-exchange chromatography or ultrafiltration to reduce bacterial endotoxin to ≤0.5 EU/mg as measured by USP <85>. The pH is maintained between 7.0 and 7.8 with phosphate buffer to prevent free cholic acid precipitation. Osmolality is adjusted with sodium chloride to 280-320 mOsm/kg by freezing-point depression, and particulate matter is controlled to USP <788> limits. Injectable formulations containing calcium ions require compatibility evaluation; calcium bile salts have low aqueous solubility above pH 6.0, and admixture with calcium gluconate is avoided unless specific compatibility data support co-administration.

    Process validation must demonstrate that the sterile filtration step does not reduce cholic acid assay below 95.0% of the pre-filtration value; a decrease greater than 5.0% indicates filter incompatibility. OBE-IP-450 vials are stored at 2-8°C before reconstitution. Repeated freeze-thaw cycles of the reconstituted solution are not recommended because micelle size distribution may shift. The oral grade OBE-PG-450 is not suitable for injection because it lacks the bacterial endotoxin and particulate matter controls required by USP <788>.

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