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(1S,2S,3R,5S)-(+)-2,3-Pinanediol Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: (1S,2S,3R,5S)-(+)-2,3-Pinanediol Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales10@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 453831
    Productname (1S,2S,3R,5S)-(+)-2,3-Pinanediol Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    Chemicalname (1S,2S,3R,5S)-2,3-Pinanediol
    Iupacname (1S,2S,3R,5S)-2,6,6-trimethylbicyclo[3.1.1]heptane-2,3-diol
    Casnumber 18680-27-8
    Molecularformula C10H18O2
    Molecularweight 170.25 g/mol
    Appearance White to off-white crystalline powder or crystals
    Odor Odorless or faint characteristic odor
    Purity ≥98.0% (HPLC)
    Assay 98.0% - 102.0% (on dried basis)
    Grade Pharma Grade / API Grade
    Dosageforms Tablet, Capsule, Granule, Injection
    Routesofadministration Oral and Injectable
    Solubility Soluble in ethanol, methanol, chloroform, dichloromethane; slightly soluble to insoluble in water
    Meltingpoint 60-67 °C
    Boilingpoint 265.6 ± 23.0 °C (predicted)
    Specificopticalrotation [α]D20 = +33° to +35° (c=1, CHCl3)
    Stereochemicalconfiguration (1S,2S,3R,5S)
    Chiralcenters 4
    Storageconditions Store in a cool, dry, well-ventilated area, protected from light, heat, and moisture; keep container tightly closed
    Shelflife 2 years when stored properly
    Lossondrying ≤0.5%
    Residueonignition ≤0.1%
    Heavymetals ≤10 ppm
    Microbiallimits Complies with pharmaceutical specifications
    Endotoxinlimit Complies with injectable grade requirements
    Particlesize Customizable upon request for tablet, capsule, or granule formulation
    Manufacturingstandard GMP-compliant
    Pharmacopoeiastandard In-house / pharmaceutical grade specification
    Usecategory Pharmaceutical API / chiral auxiliary

    As an accredited (1S,2S,3R,5S)-(+)-2,3-Pinanediol 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 Packaged in 25 kg double polyethylene-lined fiber drums, sealed for pharmaceutical API tablet, capsule, granule, oral, and injectable use.
    Container Loading (20′ FCL) Container Loading: 20′ FCL loaded with palletized, sealed pharma-grade drums of (1S,2S,3R,5S)-(+)-2,3-Pinanediol API, labeled and secured for safe transport.
    Shipping Shipped as pharma-grade (1S,2S,3R,5S)-(+)-2,3-Pinanediol in sealed, inert, light-resistant, tamper-evident containers labeled for oral and injectable API use. Transport via qualified couriers under controlled temperature per GDP and IATA/ADR/IMDG rules; protect from moisture, contamination, and extreme heat. Documentation includes CoA, SDS, packing list, and temperature records.
    Storage Store in a tightly closed, original container in a cool, dry, well-ventilated area, protected from light and moisture. Maintain controlled room temperature (15–25°C). Keep away from oxidizing agents and incompatible materials. For pharmaceutical use, follow cGMP requirements, segregate from non-API materials, and use appropriate handling to prevent contamination. Keep sealed until use.
    Shelf Life Shelf life: typically 24 months when stored sealed in a cool, dry place, protected from light and moisture; retest before use.
    Application of (1S,2S,3R,5S)-(+)-2,3-Pinanediol Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    In a 500 L glass-lined reactor equipped with a retreat-curve impeller operating at 80–120 rpm, (1S,2S,3R,5S)-(+)-2,3-pinanediol is charged with a substituted boronic acid in toluene under a Dean-Stark trap. Jacket temperature is held at 110–115 °C until water collection ceases and the recovered solvent remains clear. A Karl Fischer limit of ≤ 0.05% H₂O is applied to the reactor contents before downstream organometallic processing. Above 0.05% H₂O, the equilibrium can re-open to free diol and boronic acid, quench subsequently added butyllithium or LDA, and reduce the diastereomeric ratio below a commonly set 99:1 target for sterically crowded substrates. The resulting pinanediol boronic ester is isolated as a crystalline or distilled intermediate and stored under nitrogen with a desiccated liner. Residual toluene in the isolated ester is controlled to ≤ 890 ppm according to ICH Q3C Option 1. When the ester is intended for a route leading to an injectable API, bacterial endotoxin sampling is imposed on the ester because terminal sterile filtration of the final drug product does not remove endotoxins.The isolated ester is characterized by 11B NMR to confirm boronate ester formation and by chiral gas chromatography or supercritical fluid chromatography to verify enantiomeric purity. A pharma-grade acceptance criterion of ≥ 99.0% enantiomeric excess is typically applied for a chiral auxiliary supply. Water content is measured by USP <921> Karl Fischer titrimetry; a limit of ≤ 0.5% is common for general use, while tighter limits such as ≤ 0.05% are applied when the material feeds a water-sensitive organometallic reaction. The material is also controlled for residue on ignition and residual solvents using headspace gas chromatography, with detection conditions referenced to USP <467> and Ph. Eur. 2.2.28.

    What Limits Diastereoselectivity in the Matteson Homologation Sequence?

    The lithiation-homologation sequence proceeds through LDA in THF at −78 °C. Pinanediol boronic ester is combined with dichloromethane and LDA to generate an α-chloro boronate intermediate; subsequent treatment with ZnCl₂ activates chloride displacement by an amine, alkoxide, or other nucleophile. Diastereoselectivity is governed by internal temperature, LDA addition rate, and the steric demand of the incoming nucleophile. Process-scale batches use a jacketed stirred tank with a Pt100 thermocouple positioned in the lower impeller zone. The LDA feed is controlled to hold the internal temperature below −65 °C during addition. If the temperature rises above −60 °C, α-deprotonation selectivity is reduced and additional chiral HPLC peaks appear in the crude α-chloro boronate. Published data for the (1S,2S,3R,5S) isomer under these conditions report diastereomeric ratios above 98:2 for certain methyl-substituted substrates; values below 95:5 are considered out-of-specification in a downstream chiral API route because the subsequent hydrolysis to the free boronic acid would carry the distereomeric impurity forward.During the substitution step, ZnCl₂ is added as a THF solution at 0–25 °C. The resulting pinanediol boronic ester is then hydrolyzed to the free boronic acid under controlled pH. This hydrolysis is not a neutralization-only step; boronic acid products can form boroxine condensates at low pH and high concentration. Residual dichloromethane from the homologation sequence is controlled to ≤ 600 ppm, and THF to ≤ 720 ppm, under ICH Q3C. When the boronic acid API is intended for injectable use, additional testing for residual pinanediol is performed by LC-UV or evaporative light scattering detection. A qualified limit of ≤ 0.10% area is commonly applied in the release specification, although published data for residual pinanediol in specific injectable APIs is limited and must be justified batch-wise.Bortezomib-type active substances produced through pinanediol-mediated homologation are formulated as lyophilized powders for reconstitution. In the lyophilization cycle, the active substance is dissolved with mannitol as a bulking agent, pH is adjusted to 5.0–5.5, and the solution is filled into Type I borosilicate vials. Shelf temperatures are ramped around the collapse temperature of the formulation; primary drying is maintained below −30 °C with chamber pressure 50–150 µbar. Residual moisture of the lyophilized cake is controlled by Karl Fischer to ≤ 1.0% H₂O. Higher moisture accelerates boronic acid degradation and can shift the reconstituted pH outside the approved interval. The final injectable product is released under USP <1> Injections, USP <788> particulate matter, and USP <790> visible particulates, with API-specific limits for bacterial endotoxins calculated under USP <85> and Ph. Eur. 2.6.14.

    When Oral Capsules of Boronic Acid APIs Are Manufactured after Pinanediol-Directed Synthesis

    Encapsulation is conducted in a low-humidity suite controlled at ≤ 40% RH; dry blending with mannitol, microcrystalline cellulose, or pregelatinized starch is used. Direct filling into hard gelatin or HPMC capsules is preferred over wet granulation because boronic acid APIs can equilibrate with water to form boroxines. A dosator or tamping-pin capsule filler is selected based on bulk density; fill weights are monitored every 15–30 min with relative standard deviation limits aligned to USP <905>. Final capsules may include desiccant canisters to maintain low headspace humidity. Dissolution is assessed using USP Apparatus 1 or 2 at 37 ± 0.5 °C; media pH is selected from the biopharmaceutical classification of the active substance. For low-dose potent products, content uniformity testing follows Ph. Eur. 2.9.40, with acceptance value ≤ 15.0 unless otherwise specified in the marketing authorization.Tablet compression of downstream APIs synthesized from pinanediol is feasible when the active substance is stable enough for dry granulation. Roller compaction is used with roll pressure 8–12 kN/cm and screen size 1.0–1.25 mm. Lubrication with magnesium stearate at 0.25–1.0% w/w is controlled to avoid over-lubrication. Tablet hardness is tested to meet disintegration times specified in Ph. Eur. 2.9.1 and USP <701>. For moisture-sensitive boronic acid APIs, direct compression or dry granulation is preferred over fluid-bed wet granulation because the latter introduces hydrolytic stress during spraying and drying.

    Asymmetric allylation feedstock for homoallylic alcohol tablet intermediates

    Pinanediol allylboronates generated from the diol are used to add allyl groups to aldehyde intermediates. The reaction is carried out in dry dichloromethane or toluene at −20 to 0 °C; the optical purity of the resulting homoallylic alcohol is typically ≥ 95:5 er for unhindered aldehydes. More substituted aldehydes require lower temperatures and longer addition times; published data for this specific pinanediol isomer in preparative allylation of complex pharmaceutical aldehydes is limited. The resulting alcohol is converted to ester, ether, or mesylate intermediates before final API crystallization and tablet or capsule processing. Process-scale stereochemical performance should be confirmed by chiral HPLC because the enantioselectivity observed in laboratory glassware can shift when the reaction is transferred to a 100–500 L gas-purged reactor.

    How Are Particulate, Endotoxin, and Residual Solvent Risks Addressed for Injectable Routes?

    When a chiral diol building block is used in the synthesis of an API intended for an injectable dosage form, quality systems treat the synthetic intermediate as a critical raw material. Residual solvent control follows ICH Q3C; elemental impurity risk follows ICH Q3D and USP <232>/<233>. If palladium or nickel catalysts are not used, the major elemental risk is from process equipment. Glass-lined or titanium-alloy reactors are specified in late-stage steps to minimize metal shedding. Bacterial endotoxin limits in the final API are calculated from the maximum dose; for a lyophilized parenteral oncology product, the limit may be set below 0.5 EU/mg based on the maximum daily dose and USP <85> requirements. Sub-visible particulate matter in the final injectable is regulated by USP <788> and Ph. Eur. 2.9.19; the incoming pinanediol building block is not routinely tested for particulate matter unless it is used in a terminal filtration-avoiding stream, but the final API is filtered before fill.For oral solid dosage forms, microbial enumeration is controlled under USP <61>/<62> and Ph. Eur. 2.6.12/2.6.13. A non-sterile API acceptance limit of total aerobic microbial count ≤ 100 CFU/g and total combined yeasts and molds ≤ 10 CFU/g is commonly applied. When the same API is intended for both oral and injectable use, the injectable route drives the stricter endotoxin and particulate controls. Routine release of (1S,2S,3R,5S)-(+)-2,3-pinanediol includes appearance, water content, chiral purity, and residual solvent profile. A chiral stationary-phase HPLC method with a polysaccharide column is used for enantiomeric purity; UV detection at 210 nm is typical for a diol lacking a strong chromophore. Gas chromatography with headspace injection is used for residual solvents. For pharma-grade supply, certificates of analysis should align with ICH Q7 for raw materials and include retest date, storage conditions, and statement of GMP status.
    Core release and supply chain controls for pharma-grade (1S,2S,3R,5S)-(+)-2,3-pinanediol
    Quality areaStandard or methodTypical pharmaceutical-grade acceptance criterion
    Residual solventsICH Q3C (R8), USP <467>, Ph. Eur. 2.2.28Toluene ≤ 890 ppm, THF ≤ 720 ppm, dichloromethane ≤ 600 ppm
    Water contentUSP <921> Karl Fischer≤ 0.5% as general release; ≤ 0.05% for organometallic feed
    Enantiomeric purityChiral HPLC or SFC≥ 99.0% ee or enantiomeric ratio ≥ 99:1
    Elemental impuritiesICH Q3D, USP <232>/<233>Class 1 and 2A limits based on route; Pd ≤ 100 µg/day oral, ≤ 10 µg/day parenteral
    Bacterial endotoxin, injectable routeUSP <85>, Ph. Eur. 2.6.14Limit calculated from dose; example ≤ 0.5 EU/mg for oncologic parenteral
    Microbial enumeration, non-sterile useUSP <61>/<62>, Ph. Eur. 2.6.12/2.6.13TAMC ≤ 100 CFU/g, TYMC ≤ 10 CFU/g, specified pathogens absent
    Residual pinanediol in final APILC-UV or ELSDQualified limit, commonly ≤ 0.10% area
    Oral and injectable processing thresholds for moisture-sensitive boronic acid APIs derived from pinanediol chemistry
    Unit operationParameter and rangeTechnical basis
    Direct encapsulationRelative humidity ≤ 40% RHReduces boronic acid hydrolysis and boroxine formation
    Roller compactionRoll pressure 8–12 kN/cm, mesh 1.0–1.25 mmAvoids wet granulation hydrolytic stress
    Lyophilization primary dryingShelf temperature ≤ −30 °C, chamber pressure 50–150 µbarPrevents cake collapse and moisture-driven degradation
    Reconstitution pH5.0–5.5Stabilizes acidic boronic acid function in aqueous injectable
    Final injectable particulate matterUSP <788>, USP <790>, Ph. Eur. 2.9.19Controls sub-visible and visible particulates after reconstitution
    Content uniformityUSP <905>, Ph. Eur. 2.9.40Confirms low-dose potent API distribution in capsule or tablet
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    Certification & Compliance
    More Introduction

    Product designation (1S,2S,3R,5S)-(+)-2,3-Pinanediol Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable corresponds to CAS 18680-27-8, molecular formula C10H18O2, and relative molecular mass 170.25 g/mol. The substance is a chiral 2,3-diol derived from the pinane skeleton and is handled under pharmaceutical quality systems aligned with ICH Q7 for starting materials and advanced intermediates used in active pharmaceutical ingredient synthesis and formulation development. The (+) descriptor reflects the sign of specific optical rotation for the 1S,2S,3R,5S absolute configuration. In pharmaceutical development, the product is applied where stereochemical control of an intermediate or final active pharmaceutical ingredient is required, including solid oral dosage forms prepared by direct compression or granulation and injectable presentations employing aseptic filling or terminal sterilization. The material is not a monographed drug substance in the major pharmacopoeias; therefore, the release specification is product-specific and must be linked to the downstream critical quality attributes of the dosage form.

    What Limits Chiral Purity Retention in Boronate Ester Synthesis?

    The formation of cyclic boronate esters from (1S,2S,3R,5S)-(+)-2,3-pinanediol is a critical application in asymmetric synthesis. In a typical process configuration, the diol and an alkyl- or arylboronic acid are refluxed in toluene or cyclohexane in a jacketed reactor equipped with a Dean-Stark trap and pitched-blade turbine agitation. Water removal by azeotropic distillation drives the equilibrium toward the cyclic ester. Because residual water can hydrolyze the boronate and cause diastereomeric equilibration, the reaction headspace and solvent charge must be dried before charging. Process development studies generally recommend maintaining a nitrogen or argon overlay to limit oxidative degradation of the pinane skeleton. Extended exposure to strong oxidizers or to heat above the melting range can compromise chiral purity. Published data for this specific configuration is limited; therefore, water tolerance and hold-time studies should be performed on a lot-specific basis before setting a fixed drying limit. The stereochemical role of the diol is to generate a rigid boronate intermediate in which the approach of nucleophiles is biased by the pinane ring. Variation in the chiral purity of the starting diol directly affects the enantiomeric excess of downstream homologated intermediates. For this reason, chiral GC-FID using a cyclodextrin capillary column is more informative than achiral assay alone.

    For immediate-release tablet and capsule development, the crystalline diol is typically screened in low-dose active blends because the material is more commonly used as a synthetic intermediate than as a high-dose final active ingredient. Blending with microcrystalline cellulose, mannitol, and croscarmellose sodium in a low-shear V-blender requires humidity control below 60% RH to limit agglomeration and surface adhesion. Particle size distribution is characterized by laser diffraction per USP 429; if segregation or content uniformity issues are observed in a low-dose blend, the material is pre-sieved through a 250 µm mesh or co-milled to reduce coarse particles. Tablet compression trials should evaluate punch sticking because low-melting chiral diols can soften under compacting pressure. For capsule filling, the powder may be dry-granulated by roller compaction when improved flow and bulk density are required.

    Specification Framework and Analytical Release Criteria

    Release testing for the pharma-grade material is organized around compendial methods adapted to a low-UV-absorbing crystalline diol. Because the compound lacks a strong chromophore, gas chromatography is preferred over HPLC-UV for assay and chiral purity. The following table lists representative acceptance criteria for a pharma-grade release specification; the valid certificate of analysis may impose tighter limits for a given lot.

    AttributeMethodRepresentative acceptance criterion
    AppearanceVisual examinationWhite to off-white crystalline powder
    IdentificationGC retention time and specific optical rotation, Ph Eur 2.2.7Positive optical rotation; retention time within ± 0.05 min of reference
    AssayGC-FID, USP 621≥ 98.0% area
    Chiral purityChiral GC-FID, cyclodextrin capillary column≥ 99.0% enantiomeric excess
    WaterKarl Fischer, USP 921 Method Ia≤ 0.5% w/w
    Residue on ignitionUSP 281 / Ph Eur 2.4.16≤ 0.1%
    Residual solventsUSP 467 / Ph Eur 2.4.24Limits per ICH Q3C; specific solvents reported on certificate of analysis
    Elemental impuritiesUSP 232/233 / ICH Q3DPDE-based limits per intended route of administration; class 1 elements controlled
    Endotoxin, injectable gradeUSP 85 / Ph Eur 2.6.14≤ 0.050 EU/mg when injectable testing is selected
    Microbial enumeration, nonsterileUSP 61/62TAMC ≤ 100 CFU/g; TYMC ≤ 10 CFU/g; absence of Escherichia coli

    Because the compound is a chiral intermediate rather than a final monographed drug substance, the specification must be linked to the synthetic route and the intended final dosage form. For injectable applications, endotoxin and particulate matter are additional release considerations. The nonsterile grade is not interchangeable with injectable-grade material unless endotoxin control and bioburden reduction are demonstrated through the full manufacturing and filtration train.

    Granulation of the diol requires compatibility screening with aqueous binder systems because the material may be sensitive to prolonged moist heat. When a wet granulation step is used, hydroalcoholic granulation fluids are often selected over pure aqueous systems, and drying is performed in a vacuum tray dryer or fluid-bed dryer at reduced temperatures. The drying endpoint is confirmed by loss on drying rather than by fixed time alone. For roller compaction, the material is blended with microcrystalline cellulose and crospovidone before compaction; the ribbons are milled through a 1.0 mm screen to obtain granules suitable for tablet compression or capsule filling. Residual moisture after granulation should be brought below 0.5% w/w before lubrication with magnesium stearate, because free water can interact with the diol and alter blend flow.

    When the Stereoisomer Is Used in Sterile Injectable Formulations

    Sterile injectable presentations introduce a different control hierarchy. The diol is not inherently sterile, and dry-heat sterilization is generally avoided because the material may melt or soften before achieving a reliable sterilization temperature. If terminal sterilization of the finished dosage form is required, moisture heat exposure such as autoclaving at 121°C for 15 min must be supported by stereochemical stability data. Published data for this specific configuration is limited; therefore, forced degradation studies under ICH Q1A conditions should be used to establish that chiral purity remains within acceptance limits after moist-heat exposure. Aseptic filtration through a 0.22 µm PVDF or polyethersulfone membrane is common for solution dosage forms, but filter compatibility must be verified because low-molecular-weight diols can swell or plasticize certain membrane polymers. Particulate matter limits follow USP 788 for injectable products; subvisible particle counts and a bioburden-reduction step are required unless the process is fully aseptic. Endotoxin control is addressed through depyrogenation of containers, closures, and equipment, rather than through high-temperature treatment of the compound itself. The material should be stored at 2–8°C under inert gas and protected from moisture and oxidizing agents when injectable-grade status is to be maintained.

    Compared with the enantiomeric (1R,2R,3S,5R)-(−)-2,3-pinanediol, the (1S,2S,3R,5S)-(+)-2,3-pinanediol produces opposite diastereofacial selection in chiral boronate reactions. This difference is not a minor quality attribute; it determines the absolute configuration of the downstream active pharmaceutical ingredient. The racemic 2,3-pinanediol mixture is unsuitable for stereoselective synthesis of a chiral API because it provides no enantiomeric induction and can generate a mixture of diastereomers. Compared with other chiral auxiliaries such as diisopropyl tartrate or camphor-derived diols, pinanediol-derived boronates often form crystalline intermediates with characteristic solubility and hydrolytic cleavage behavior. The pinane skeleton is comparatively rigid and can simplify isolation of the chiral intermediate by crystallization. However, complete removal of the chiral diol from the final API must be demonstrated where the diol is an auxiliary and not part of the drug substance structure. Residual chiral diol in the final API is controlled through purge factor calculations and routine release testing, typically by GC-FID or GC-MS. Technical-grade 2,3-pinanediol differs from the pharma-grade material in that it may contain higher levels of residual catalysts, uncontrolled stereoisomer content, and variable heavy metal profiles. Because those impurities can be carried into the final dosage form or synthetic intermediate, the pharma-grade product uses defined residual solvent and elemental impurity controls under ICH Q3C and ICH Q3D. The pharma-grade designation therefore reflects a quality management system and a release and stability testing program rather than a difference in chemical structure alone.

    Aspect(1S,2S,3R,5S)-(+)-2,3-pinanediol(1R,2R,3S,5R)-(−)-2,3-pinanediolTechnical-grade or racemic 2,3-pinanediol
    CAS registry18680-27-818680-28-9Racemic mixture; no single stereochemical pharma designation
    Optical rotationPositiveNegativeNo net optical rotation
    Chiral inductionOpposite diastereoface selectionOpposite diastereoface selectionNo enantioselective induction
    Typical pharma handlingICH Q7, high chiral purity, residual solvent and elemental impurity controlICH Q7, high chiral purity, residual solvent and elemental impurity controlGenerally technical grade; requires purification and qualification before use in chiral synthesis
    Residual chiral impurity riskControlled by chiral GC-FIDControlled by chiral GC-FIDHigh for chiral API synthesis
    Regulatory applicationStarting material or intermediate for stereoselective synthesisStarting material or intermediate for opposite stereoselective synthesisNot suitable for chiral API synthesis without purification

    Operational boundaries are defined by moisture sensitivity, stereochemical stability, and the intended route of administration. The compound should not be blended with strong oxidizing agents, stored in open containers at elevated humidity, or processed under conditions that expose it to prolonged heat without supporting stability data. For oral dosage forms, the primary manufacturing risks are particle size control, moisture-induced agglomeration, and punch sticking during compression. For injectable dosage forms, the primary risks are endotoxin transfer, filter compatibility, and absence of terminal-sterilization stereochemical data. Where exact degradation pathways or process limits are not established, the filing must rely on lot-specific forced degradation data and process qualification rather than assumed stability. The material is therefore suitable for development and production only when the specification and processing controls are derived from the downstream product’s critical quality attributes and supported by compendial test methods.

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