Products

Birch Triterpenes Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: Birch Triterpenes Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales10@sinochem-nanjing.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    VTB
    Specifications
    HS Code 939045
    Product Name Birch Triterpenes Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    Api Name Birch Triterpenes
    Botanical Source Betula pendula, Betula platyphylla, Betula pubescens
    Active Constituents Betulin; Betulinic Acid; Lupeol; Oleanolic Acid; Ursolic Acid
    Cas Numbers 473-98-3; 472-15-1; 545-47-1; 508-02-1; 77-52-1
    Molecular Formulas C30H50O; C30H48O3; C30H50O; C30H48O3; C30H48O3
    Molecular Weights 442.72; 456.70; 426.72; 456.70; 456.70
    Appearance White to off-white powder
    Purity ≥95% total triterpenes
    Assay ≥95% by HPLC
    Grade Pharma Grade
    Quality Standards EP; USP; BP; ChP
    Pharmacopoeial Compliance Complies with EP, USP, BP, ChP
    Solubility Soluble in ethanol and DMSO; slightly soluble in water
    Storage Conditions Store at 2-8°C, protected from light and moisture
    Shelf Life 24 months
    Dosage Forms Tablet; Capsule; Granule; Injection
    Routes Of Administration Oral; Injectable
    Therapeutic Category Anti-inflammatory; Hepatoprotective; Antiviral; Antioxidant
    Heavy Metals ≤10 ppm
    Microbial Limits Complies with EP/USP
    Endotoxin Limit ≤5 EU/mg for injectable grade
    Sterility Sterile for injectable grade
    Residual Solvents Complies with ICH Q3C
    Particle Size Customizable, e.g., 80 mesh
    Identification IR; HPLC; MS

    As an accredited Birch Triterpenes 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 Birch Triterpenes Pharma Grade API packed in 25 kg net sealed, light-resistant fiber drums with double polyethylene liners for oral/injectable use.
    Container Loading (20′ FCL) 20′ FCL container loading: palletized drums of Birch Triterpenes Pharma Grade API, securely braced, sealed, clean/dry, for oral/injectable dosage forms.
    Shipping Birch Triterpenes Pharma Grade API is shipped in sealed, light-resistant, tamper-evident containers under validated temperature conditions (ambient or 2–8°C per grade). Qualified couriers provide monitoring and chain-of-custody. Include CoA, SDS, and GMP documentation. Avoid freeze–thaw and contamination; handle aseptically for injectable lots. Maintain required humidity and security throughout transit.
    Storage Store Birch Triterpenes Pharma Grade API in a cool, dry, well-ventilated area at controlled room temperature (15–25°C), away from heat, ignition, and direct sunlight. Keep containers tightly closed, protected from moisture, light, and contamination. Use clean, labeled, pharmaceutical-grade containers. Separate from incompatible materials. For injectable-grade material, maintain dedicated, sterile-compatible storage and follow manufacturer stability and handling instructions.
    Shelf Life Birch triterpenes API Shelf Life: Typically 24–36 months when stored sealed, protected from light and moisture at controlled room temperature.
    Application of Birch Triterpenes Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    Direct Compression of Native Birch Triterpenes Requires Particle Size Reduction Before Final Blending

    Direct compression of native crystalline birch triterpenes without prior particle engineering is not a robust production route because the unmilled material exhibits plate-like crystal habit, low bulk density, and poor flow under gravity feed. Spiral jet milling is applied to reduce primary particle size to a laser-diffraction D90 below 10 µm using ISO 13320:2020 as the sizing method. A rotary tablet press equipped with a force feeder and Euro B tooling is operated at 10–20 kN main compression force and 2–4 kN precompression force. Turret speed is typically held at 20–40 rpm. The formulation consists of silicified microcrystalline cellulose as the primary filler, croscarmellose sodium at 2.0–4.0% w/w, colloidal silicon dioxide at 0.5–1.0% w/w, and magnesium stearate at 0.25–0.50% w/w. API loading is commonly set between 10% w/w and 30% w/w depending on the intended dose. Blending is performed in a bin blender at 10–12 rpm for 15–20 min with a vessel fill of 60–70%. In-process controls include content uniformity testing according to USP <905>, with an acceptance value not exceeding 15 for 10 units. Tablet hardness is controlled between 60 N and 100 N. Friability is tested according to USP <1216>, with mass loss after 100 rotations not more than 1.0%. Disintegration is tested in water at 37±2 °C according to USP <701>, with a limit of not more than 15 min. Dissolution testing uses 900 mL of phosphate buffer at pH 6.8 containing 0.25–0.5% sodium lauryl sulfate, paddle speed 75 rpm, and temperature 37±0.5 °C per USP <711>. The surfactant is required because aqueous solubility of native betulin is consistently reported below 1 µg/mL. Quantification of betulin and potential oxidative degradation products is performed by reversed-phase HPLC with UV detection near 210 nm. Compression force must be reduced if capping appears at tablet hardness above 80 N. If the final blend bulk density falls below 0.35 g/mL, a force feeder with twin-paddle agitation should be used to maintain die fill consistency.

    On a tamping-pin capsule filling machine, the main control variable is the tapped bulk density of the formulated powder blend rather than the API particle size alone. A blend containing 20% w/w micronized birch triterpenes, pregelatinized starch, lactose monohydrate, and sodium stearyl fumarate can show fill weight variation above 5% when the Hausner ratio exceeds 1.35. Powder flow is evaluated by USP <1174>, and Carr index values above 25 indicate that colloidal silicon dioxide at 0.5–1.5% w/w or a short-lubrication step with magnesium stearate is necessary. Capsule disintegration is evaluated in water at 37±2 °C according to USP <701>, with a limit of not more than 15 min for immediate-release hard gelatin or HPMC capsules. The shell choice between gelatin and HPMC can shift disintegration and dissolution behaviour, so the selected shell must be confirmed by dissolution testing in 0.1 N hydrochloric acid and phosphate buffer at pH 6.8 per USP <711>. A typical fill weight for a 100 mg API dose is 300–500 mg depending on excipient bulk density. Mean fill weight is controlled within ±3% of target, and individual capsule weight variation is evaluated under USP <905> uniformity of dosage units. Because the powder is not compacted before filling, segregation during transfer from the hopper to the dosing disc is a known bottleneck on high-speed lines. Sampling at the beginning, middle, and end of the batch is required for blend assay. If the API is pre-blended with a high-surface-area carrier such as fumed silicon dioxide at 0.5–1.0% w/w, the mixture is passed through a 0.425 mm sieve before charging the capsule hopper. Capsule filling is performed at controlled room temperature and relative humidity not more than 60% RH to avoid moisture-induced cohesion and static charging.

    Process stepCritical controlTypical rangeCompendial methodLimit
    Jet millingParticle size D90 by laser diffraction≤10 µmISO 13320:2020In-process verification
    BlendingBlend assay relative standard deviation≤5.0%In-house HPLCUSP <905> support
    Direct compressionTablet hardness60–100 NUSP <1217>Visual and instrument
    Tablet friabilityMass loss after 100 rotations≤1.0%USP <1216>NMT 1.0%
    Tablet disintegrationDisintegration time in water at 37±2 °C≤15 minUSP <701>NMT 15 min
    Capsule fillMean fill weight±3% of targetUSP <905>AV ≤15

    What Process Boundary Separates Dry Roller Compaction From Aqueous High-Shear Granulation for Brittle Triterpene Powders?

    Dry roller compaction is selected when the API is sensitive to residual water, when organic solvent limits under ICH Q3C make a solvent-based binder unattractive, or when short lead time is required for clinical trial material. The roller compactor is operated with roll pressure between 4 MPa and 8 MPa, roll gap of 1–3 mm, and screen size of 0.8–1.5 mm. Ribbon solid fraction above 0.65 is targeted, and the milled granules show a D50 between 200 µm and 600 µm. Aqueous high-shear granulation is preferred when content uniformity cannot be maintained by dry granulation because of fine API segregation. In a 300 L high-shear granulator, the dry mix is granulated with a 5–10% w/w aqueous binder solution of povidone K30 or hydroxypropyl cellulose. Impeller tip speed is set at 4–8 m/s, chopper speed at 1,500–3,000 rpm, and binder spray rate at 0.5–1.0 kg/min. The wet mass is transferred to a fluid-bed dryer and dried to loss on drying of 1.5–2.5%. Dried granules are sieved through a 1.0 mm screen before lubrication. Both routes require a final blend lubricated with magnesium stearate at 0.5% w/w for 3–5 min. Residual water is tested by Karl Fischer titration according to USP <921>. If the granulation endpoint is exceeded, granule hardness rises and disintegration may exceed 15 min. If the granules are too dry, compression force must increase to reach target hardness, and tablet capping may appear above 120 N. For heat-sensitive development batches, wet granulation inlet air temperature is held at 60–70 °C, with product temperature not exceeding 45 °C. The roller compaction and high-shear granulation routes are validated separately because the granule porosity, particle size distribution, and residual water profiles are not interchangeable.

    For unit-dose stick packs, the granule fraction between 180 µm and 710 µm determines flow, fill accuracy, and reconstitution behaviour. A directly compressible or wet-granulated intermediate can be filled on a vertical form-fill-seal machine with auger or volumetric cup dosing. Fill weight variation at a 1 g target is generally controlled within ±5%, and individual sachet mass within ±10%. The vehicle is based on mannitol, xylitol, or isomalt, with crospovidone at 1–3% w/w as disintegrant and colloidal silicon dioxide as glidant. Because birch triterpenes are lipophilic, wetting in water is poor; the addition of sodium lauryl sulfate at 0.1–0.5% w/w or poloxamer 188 at 0.5–1.0% w/w can reduce the contact angle and aid dispersion. Finished granules are dried to water activity below 0.60 to control microbial growth and minimise hydrolytic degradation. The sachets are sealed with a barrier film, typically PET/aluminium/PE laminate, to limit oxygen and moisture ingress. Stability evaluation follows ICH Q1A(R2) long-term storage at 25 °C/60% RH and accelerated storage at 40 °C/75% RH for 6 months. Particle size distribution is confirmed by sieve analysis according to USP <786>; coarse material retained on an 850 µm sieve should be limited to avoid grittiness in oral delivery.

    Sterile Injectable Presentation: Lyophilized Nanosuspension and Aseptic Process Boundaries

    For injectable development, native birch triterpenes cannot be formulated as a simple aqueous solution without co-solvents or a carrier system. One technically defined route is wet-ball milling of the API with 0.5–1.0 mm yttria-stabilized zirconia beads in a stabilizer solution containing poloxamer 188 at 0.5–1.0% w/v and sodium deoxycholate at 0.1–0.2% w/v. The milling chamber is cooled to 5–15 °C to limit thermal stress. Milling continues until laser diffraction according to ISO 13320:2020 shows D90 below 1 µm and D50 below 0.3 µm. Mannitol or sucrose at 5–10% w/v is added as a cryoprotectant before lyophilization. The lyophilization cycle is design-space dependent. For mannitol-based formulations, primary drying at −20 °C to −10 °C and chamber pressure of 0.1–0.2 mbar is typical. For sucrose-containing formulations, the product temperature must remain below the collapse temperature, often near −31 °C, or the cake will lose structure on reconstitution. Primary drying is commonly held for 24–48 h, followed by secondary drying at 20–30 °C. The resulting cake is reconstituted with water for injection to a concentration of 5–20 mg/mL, depending on the stopper extractable and leachable profile. Sterility is confirmed by membrane filtration according to USP <71>. Bacterial endotoxin is controlled by kinetic chromogenic LAL according to USP <85>, with a conservative development limit of 0.25 EU/mg or a dose-adjusted limit derived from 5 EU/kg body weight per hour. Subvisible particulate matter must meet USP <787> for therapeutic products or USP <788> for large-volume parenterals, with light-obscuration criteria of not more than 6000 particles at ≥10 µm and 600 particles at ≥25 µm per container for small-volume parenterals. If the particle size is not reduced below 0.22 µm, terminal sterile filtration is impossible; therefore aseptic processing is mandatory. Published sterilization compatibility data for this specific configuration is limited, so terminal autoclaving at 121 °C for 15 min is not assumed to be feasible without thermostability proof. All injectable work must be performed under ICH Q3D elemental impurity limits and 21 CFR 211 aseptic processing controls.

    Injectable control pointSpecific methodTypical development limitStandard
    Particle size after millingLaser diffractionD50 ≤0.3 µm; D90 ≤1.0 µmISO 13320:2020
    Subvisible particulate matterLight obscuration≥10 µm: ≤6000/container; ≥25 µm: ≤600/containerUSP <787>/<788>
    SterilityMembrane filtrationNo growth after 14 daysUSP <71>
    Bacterial endotoxinKinetic chromogenic LAL≤0.25 EU/mg or dose-adjustedUSP <85>
    Residual moisture in lyophilized cakeKarl Fischer titration≤3.0% w/wUSP <921>
    Free Quote

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

    For samples, pricing, or more information, please contact us at +8618963613625 or mail to sales10@sinochem-nanjing.com.

    We will respond to you as soon as possible.

    Tel: +8618963613625

    Email: sales10@sinochem-nanjing.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

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

    Certification & Compliance
    More Introduction

    Birch Triterpenes Pharma Grade API is a botanical pentacyclic triterpene fraction obtained from the outer bark of Betula pendula Roth and Betula pubescens Ehrh. The product is supplied in two route-specific model designations: an oral solid-dose grade for tablet, capsule, and granule manufacture, and a low-burden injectable grade for parenteral solution or suspension compounding. Because a dedicated pharmacopoeial monograph for birch triterpenes is not currently published in Ph. Eur. or USP, the specification is constructed from ICH Q6A, ICH Q3C, ICH Q3D, and applicable general chapters. The principal analytical targets are total pentacyclic triterpene assay, marker ratio for betulin, lupeol, and betulinic acid, residual solvent content, elemental impurities, microbial quality, and—for the injectable grade—bacterial endotoxins. The two grades contain the same chemical entity and marker profile; the difference is not one of chemical identity but of bioburden, endotoxin, particle size distribution, and packaging environment. This material is distinct from cosmetic-grade birch bark extract, which is not released against pharmaceutical permitted daily exposure limits, and from single-marker synthetic betulinic acid, which does not reproduce the multicomponent fingerprint of the botanical fraction. The API is not administered as a neat powder; it is formulated into finished oral or parenteral dosage forms, with the route-specific grade selected according to the downstream manufacturing process.

    What Distinguishes an Injectable-Grade Triterpene API from Its Oral-Solid-Dose Counterpart?

    For oral solid dosage forms, microbial quality is controlled under Ph. Eur. 5.1.4 or USP 1111 as a non-sterile material. For injectable applications, the same botanical fraction is released with a stricter bacterial endotoxin limit and a low bioburden specification, because the finished parenteral dosage form must meet sterility requirements. The difference is also physical: the oral grade may be supplied as a milled or granulated powder with a particle size distribution selected for flow and blend uniformity, whereas the injectable grade is micronized or otherwise size-reduced to support suspension stability. The oral grade is not tested for sterility; the injectable grade may be supplied as a low-burden API intended for downstream sterilisation or aseptic processing. Packaging is another point of separation: injectable-grade material is filled into double low-density polyethylene bags inside HDPE drums in an ISO 14644-1 class 8 or better environment, while the oral grade may be handled in a controlled non-sterile area.

    Quality attribute Method or standard Oral solid-dose grade Injectable grade
    Total triterpene assay, dried basis USP 621 / Ph. Eur. 2.2.29 95.0%–105.0%, product-specific Same as oral; tighter water content
    Residual solvents ICH Q3C, USP 467 Methanol ≤3000 ppm if used; dichloromethane ≤600 ppm if used Same
    Elemental impurities ICH Q3D, USP 232/233 Oral PDE-based; Pb 5 µg/day, Cd 2 µg/day, As 15 µg/day, Hg 30 µg/day Parenteral PDE-based; Pb 5 µg/day, Cd 2 µg/day, As 15 µg/day, Hg 3 µg/day
    Microbial enumeration Ph. Eur. 2.6.12 / USP 61 TAMC ≤10³ CFU/g; TYMC ≤10² CFU/g Low bioburden ≤10² CFU/g; specified pathogens absent
    Bacterial endotoxins Ph. Eur. 2.6.14 / USP 85 Not normally tested ≤0.25 EU/mg when maximum parenteral dose permits; otherwise calculated per Ph. Eur. 5.1.10
    Particle size distribution USP 429 Product-specific; range set by downstream processing For suspension: D90 ≤10 µm; for solution: solubility-controlled
    Sterility Ph. Eur. 2.6.1 / USP 71 Not required Required for finished parenteral; API may be low-burden and sterilised downstream

    The limits in the table are representative pharmacopoeial ceilings or ICH-derived values, not a batch certificate. Product-specific acceptance limits are established during process validation and fixed in the marketing authorisation or quality agreement. The endotoxin limit for injectable grade is dose-normalised: a result of 0.50 EU/mg may be acceptable for a low-dose parenteral formulation with a small maximum dose, but it is not automatically acceptable for a high-dose infusion. The calculation per Ph. Eur. 5.1.10 or USP 85 is based on the maximum intended bolus dose per kilogram body weight; therefore injectable-grade specification values are route-risk controls rather than absolute product constants.

    The same birch triterpene fraction is not interchangeable with Centella asiatica triterpenes, Boswellia serrata boswellic acids, or oleanolic acid from olive leaf. Those products have different marker profiles, different solubility in hydroalcoholic vehicles, and different compendial status. The birch-derived material is also distinct from purified betulin, which is a single chemical entity with a sharp melting endotherm; the pharma-grade birch triterpene product retains co-extracted pentacyclic triterpenes that modify dissolution and particle surface energy. For oral solid-dosage development, this multicomponent nature means that content uniformity and dissolution testing may require a multi-marker approach rather than a single analyte.

    In tablet and capsule manufacturing, the limiting unit operation is usually powder flow and die filling rather than chemical potency. High total triterpene fractions are hydrophobic and may form cohesive agglomerates; a Hausner ratio above 1.35 or Carr index above 25 is typically used as the trigger for roller compaction or slugging before tablet compression. Direct compression is feasible only when the API is pre-blended with free-flowing diluents such as microcrystalline cellulose and dibasic calcium phosphate dihydrate. On a rotary tablet press with a force feeder, blends containing high loadings of the non-granulated API can exhibit variable die filling; dry granulation increases bulk density and reduces segregation. Dry granulation is preferred because aqueous granulating fluids do not readily wet the lipophilic triterpene surfaces. If wet granulation is required, a hydroalcoholic binder solution or a surfactant-containing aqueous system is used to lower interfacial tension. For capsule filling, dosator and tamping-pin machines require a granulated intermediate with controlled particle size; fine API powder can flood the dosing station or cause weight variation. The hydrophobic particles can delay tablet disintegration, so croscarmellose sodium or sodium starch glycolate is included at a level sufficient to meet disintegration per USP 701 or Ph. Eur. 2.9.1. Low-dose oral formulations containing less than 10 mg per unit require content uniformity testing per Ph. Eur. 2.9.40 or USP 905; broad particle size distributions can cause segregation during long compression runs. Granules for oral suspension are produced by blending the API with mannitol or sugar spheres, adding a binder such as povidone, and using a wetting agent to disperse the hydrophobic powder. Fluid-bed granulation can be used if the API is dispersed in the binder solution, but spray rate and inlet air temperature must be controlled to avoid fines and nozzle fouling. Published data for this specific configuration is limited; the flow and wetting limitations are nevertheless consistent with the known behaviour of high-melting, low-aqueous-solubility pentacyclic triterpenes.

    When Jet Milling Is Necessary for Parenteral Suspension Uniformity

    Parenteral suspension formulations impose a particle size requirement that is not shared by oral granules. A sterile suspension for intramuscular or subcutaneous injection must remain physically stable and pass through a needle without clogging; the API particle size is therefore reduced by jet milling or wet milling until the volume median diameter is ≤10 µm and the D90 is controlled by laser diffraction per USP 429. Micronization can generate amorphous surface domains; X-ray powder diffraction per USP 941 and differential scanning calorimetry are used to monitor solid-state changes. The injectable grade is not necessarily supplied as a sterile powder; it is produced as a low-burden powder with controlled endotoxin, and the formulated solution or suspension is sterilised downstream. Sterile filtration through a 0.22 µm membrane is possible only for fully dissolved API in a miscible solvent system. A suspension cannot pass a sterilising-grade membrane, so the vehicle and excipients are filter-sterilised separately and aseptically combined with the terminal-sterilised or aseptically processed API. Terminal moist-heat sterilisation at 121°C for 15 minutes is evaluated on a formulation-specific basis because triterpene alcohols can undergo oxidation or dehydration under stress. For high-viscosity oily vehicles, filtration and filling require pressure-rated equipment and temperature control to avoid vehicle oxidation. The triterpene fraction is poorly soluble in water, so injection vehicle development typically involves non-aqueous cosolvents, phospholipid-based systems, or cyclodextrin derivatives; each vehicle changes solubility and the risk of precipitation at the injection site. The choice between solution and suspension depends on the dose, the target release profile, and the local tolerability of the vehicle. These formulation-specific constraints are not captured in a single API specification and must be resolved during pharmaceutical development.

    Residual Solvent and Elemental Impurity Control in Botanical Triterpene APIs

    Botanical extraction solvents are the first source of chemical impurity variation. Methanol, ethanol, isopropanol, acetone, and dichloromethane are common extraction and crystallisation solvents; each is assigned an ICH Q3C class and a corresponding limit. Ethanol and acetone are Class 3 solvents with a generic limit of 5000 ppm; methanol is Class 2 with an Option 1 limit of 3000 ppm; dichloromethane is Class 2 with a limit of 600 ppm. The pharma-grade API is released only after residual solvent testing by headspace gas chromatography per USP 467 or Ph. Eur. 2.4.24. Elemental impurities in a bark-derived product are controlled against ICH Q3D permitted daily exposure values. A parenteral grade requires mercury ≤3 µg/day, whereas an oral grade can tolerate mercury up to 30 µg/day; lead 5 µg/day and cadmium 2 µg/day are common to both routes. Additional botanical controls include pesticide residues per Ph. Eur. 2.8.13 and USP 561, as well as arsenic speciation if the extraction area has geogenic arsenic contamination. The difference from unrefined birch bark extract is procedural: cosmetic-grade or laboratory-grade extracts are not released against ICH Q3D PDEs or pharmacopoeial microbial limits and may contain higher polyphenol, lignin, or residual solvent burdens. Compared with synthetic single-marker triterpene APIs, the botanical fraction requires a chromatographic fingerprint covering multiple triterpene peaks rather than a single assay value. This fingerprint is generated by HPLC or GC with detection at the appropriate wavelength or by evaporative light scattering; the marker ratio between betulin, lupeol, and betulinic acid is controlled to maintain batch-to-batch consistency. Oxidative stability is evaluated under ICH Q1A(R2) storage conditions and photostability per ICH Q1B, because the unsaturated pentacyclic skeleton can form oxo-derivatives under light or oxygen stress.

    Packaging and storage conditions are route-dependent. The oral grade may be double-bagged in polyethylene and placed in an HDPE drum with silica gel if needed; the injectable grade is bagged in a controlled environment, with the outer bag disinfected before entry into classified areas. Moisture uptake is generally low due to the lipophilic nature of the triterpenes, but bulk powder should be kept away from oxidising agents. The material should not be combined with strong oxidising agents or stored in direct sunlight; compatibility studies with common capsule shells, tablet lubricants, and parenteral packaging elastomers are required under ICH Q1A(R2).

    Top