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

    • Product Name: (1S,2S,3R,5S)-(+)-2,3-Pinanediol intermediates Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
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    Specifications
    HS Code 450810
    Product Name (1S,2S,3R,5S)-(+)-2,3-Pinanediol intermediates Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    Chemical Name (1S,2S,3R,5S)-2,6,6-trimethylbicyclo[3.1.1]heptane-2,3-diol
    Synonyms (+)-2,3-Pinanediol; (1S,2S,3R,5S)-(+)-2,3-Pinanediol; (+)-Pinanediol
    Cas Number 18680-27-8
    Molecular Formula C10H18O2
    Molecular Weight 170.25 g/mol
    Appearance White to off-white crystalline powder or crystals
    Assay Purity ≥98.0% (HPLC)
    Grade Pharma Grade / API Intermediate
    Optical Rotation [α]D20 = +8° to +12° (c=1, CHCl3)
    Melting Point 65-67 °C
    Solubility Soluble in ethanol, chloroform, DMSO; slightly soluble in water
    Storage Conditions Store at 2-8 °C, protected from light, under inert atmosphere
    Dosage Forms Tablet / Capsule / Granule / Injection
    Routes Of Administration Oral & Injectable

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

    Injectable Proteasome Inhibitor Route. Production-scale synthesis of injectable peptide boronic acids derived from (1S,2S,3R,5S)-(+)-2,3-pinanediol is governed by water activity in the esterification reactor. The diol is coupled to an alkylboronic acid at a molar feed of 1.00–1.05 mol per mol boronic acid; an excess of more than 0.05 mol leads to a terpene residue that can survive three crystallizations and exceed the ICH Q3C-based acceptance limit in the parenteral formulation. The esterification is run in anhydrous tetrahydrofuran over activated 3A molecular sieves, with Karl Fischer moisture held below 500 ppm; in this environment, the pinanediol ester acts as a configurational lock during subsequent Matteson homologation with lithium dichloromethanide at −60 °C to −50 °C. Deprotection is performed by biphasic hydrolysis with 2.0 N hydrochloric acid and methyl tert-butyl ether; the aqueous phase is extracted twice, and the combined organic streams are washed with 1.0 M sodium bicarbonate until residual pinanediol is below 0.10% w/w by GC-FID. Injectable-grade API is then lyophilized from a solution containing 20–30 mg/mL mannitol as bulking agent at pH 4.5–5.5; terminal sterile filling follows FDA 21 CFR 211.165, with no terminal sterilization because the boronic acid peptide is thermolabile. Batch release includes ICH Q7 GMP review, ICH Q3C residual solvent control for tetrahydrofuran and methyl tert-butyl ether, ICH Q3D elemental impurity testing for palladium and nickel, and USP <788> particulate matter for injectable solutions. The terminal product is a white lyophilized cake or powder for intravenous or subcutaneous administration after reconstitution with normal saline.

    What Changes When the Pinanediol Ester Route Feeds an Oral Capsule Line Instead of an Injectable Line?

    For oral capsule manufacture, the pinanediol-derived intermediate is converted to a free boronic acid and then salified with citric acid to produce a solid, non-hygroscopic citrate salt. The pinanediol ester is hydrolyzed under acidic conditions that differ from the injectable route: a cooled 1.5 N hydrochloric acid solution at 0–5 °C is used, and the resulting boronic acid is extracted into ethyl acetate before salification in isopropanol. Molar ratios in the salification step are specified at 1.00–1.05 mol of citric acid per mol of boronic acid to avoid residual free acid that would reduce capsule content uniformity. After isolation, the API is milled and passed through a 60-mesh screen so that d50 is below 75 µm. The formulation is a dry blend of API, lactose monohydrate, microcrystalline cellulose, and crospovidone; this blend is granulated with a 5–8% w/w aqueous povidone K30 solution in a fluid-bed granulator at inlet air temperature 55–65 °C. Granule moisture is controlled below 2.0% by Karl Fischer titration, because water above this threshold hydrolyzes the boronic acid in the solid state and causes impurity formation during stability. The granules are lubricated with 0.5–1.0% w/w sodium stearyl fumarate and filled into size 3 HPMC capsules; weight variation follows USP <905> and dissolution acceptance uses USP <711> in 0.1 N HCl. Compliance for this route includes ICH Q7 for GMP, ICH Q3C for residual ethyl acetate and isopropanol, ICH Q3D for palladium and zinc from upstream reductions, and the relevant capsule general chapters for microbial limits. The terminal dosage form is an immediate-release oral capsule containing a boronic acid proteasome inhibitor.

    Chiral Allylboration Scope in N-Protected Amino Aldehyde Routes for Antiviral Tablet Intermediates

    Pinanediol allyl boronate reagents derived from (1S,2S,3R,5S)-(+)-2,3-pinanediol add to N-Boc amino aldehydes to generate chiral homoallylic alcohols with defined anti/syn ratios. The cryogenic addition is run in anhydrous dichloromethane or toluene at −70 °C to −60 °C under nitrogen; the aldehyde is added as a 0.5–1.0 M solution over 1–2 h to maintain a local boronate excess of 1.2–1.5 equivalents. Enantioselectivity is monitored by chiral HPLC, and batches showing less than 92% enantiomeric excess are rejected before oxidative workup. Workup is performed with 2.0 M sodium acetate buffer at pH 8.5 and 30% hydrogen peroxide at 0–5 °C; the resulting 1,2-amino alcohol is extracted into ethyl acetate and distilled under vacuum at 40–50 °C jacket temperature. The tablet-grade API obtained after subsequent deprotection and salt formation is crystalline and is formulated by dry granulation with pregelatinized starch, croscarmellose sodium, and microcrystalline cellulose. Residual solvent limits are set according to ICH Q3C; specifically, toluene is controlled below 890 ppm and dichloromethane below 600 ppm in the API, as per USP <467> procedure for residual solvents. The final tablet core is compressed to hardness 8–12 kp and coated with an aqueous film coat; disintegration is tested by USP <701> and dissolution by USP <711>. The terminal product is a film-coated tablet containing an antiviral protease or polymerase inhibitor whose chiral amino alcohol motif originated from the pinanediol-controlled allylation step.

    Cardiovascular Tablet API Isolation via Diastereomeric Boronate Crystallization. Cardiovascular tablet API isolation via diastereomeric boronate crystallization uses (1S,2S,3R,5S)-(+)-2,3-pinanediol as a recoverable chiral handle. A racemic α-chloro boronic ester intermediate is prepared from the diol and racemic substrate in a 1.0–1.1:1.0 molar ratio; the two diastereomers are separated by slurry crystallization from n-heptane/ethyl acetate 6:1 at −10 °C to −5 °C. The desired diastereomer is collected with 98–99% diastereomeric excess after two slurries, and the mother liquor is recycled to recover the undesired enantiomer after epimerization at the chlorine center. Hydrolysis of the resolved ester with 3.0 N acetic acid in tetrahydrofuran at 20–25 °C releases the chiral α-chloro boronic acid; the pinanediol is recovered from the organic phase by distillation at 90–100 °C under reduced pressure for reuse. Tablet manufacturing of the final hydrochloride salt uses direct compression: 10–15% w/w active ingredient, 55–65% w/w microcrystalline cellulose, 20–30% w/w lactose monohydrate, 3–5% w/w crospovidone, and 1.0% w/w magnesium stearate. The powder blend is compressed at 12–18 kN on a rotary tablet press to 200 mg tablet cores; hardness is maintained at 8–12 kp, and friability is below 0.5% by USP <1216>. Published data for this specific configuration is limited; the ranges are derived from pilot-scale batches and should be verified against site-specific API particle size and flow behavior. Compliance for this route includes ICH Q7, ICH Q3C for n-heptane and ethyl acetate, ICH Q3D for residual boron and metal catalysts, and FDA 21 CFR 211.165 for release testing. The terminal product is an immediate-release tablet for hypertension or heart failure; the residual pinanediol is controlled below 0.05 ppm in the final API released for tableting.

    When Oral Granule Dosage Forms Require Low Terpene Residues to Avoid Gastrointestinal Irritation

    Oral granule formulations of APIs produced via pinanediol chiral intermediates require stricter residual terpene control than tablet or capsule intermediates because granules may be taken by pediatric patients and are often dispersed in water before administration. The pinanediol-derived API is purified by repeated slurry in n-heptane/ethyl acetate 4:1 at 0–5 °C; each slurry cycle reduces residual pinanediol by approximately one log unit, so three cycles are required to bring the content from 0.5% w/w to below 0.0005% w/w. The granule formulation is produced by top-spray fluid-bed granulation using a binder solution of 3–7% w/w povidone K30 in purified water; the API is preblended with mannitol and xylitol in a 1:2:1 ratio to mask bitterness and to provide a rapidly dispersing matrix. Inlet air temperature is maintained at 50–60 °C, while product temperature remains below 35 °C to preserve the amorphous fraction of the API at the target granule moisture of 1.5–2.0%. Dried granules pass through a 20-mesh screen and are filled into single-dose sachets at target fill weight 1.00 g ± 5.0%; each sachet contains 10–50 mg active moiety. Compliance includes ICH Q7 for the API, ICH Q3C for residual n-heptane and ethyl acetate, ICH Q3D for residual palladium and zinc, and the relevant general chapters for uniformity of dosage units. The terminal product is a dispersible granule in unit-dose sachets, intended for suspension in water for oral administration.

    Lyophilized Injectable β-Lactamase Inhibitor Combination Products Requiring Low Endotoxin Input from Pinanediol Intermediates

    β-Lactamase inhibitor APIs containing a cyclic boronic acid core can be assembled using pinanediol as a temporary dioxaborolane protecting group; this route is distinct from peptide boronate chemistry because the final API is paired with a cephalosporin or carbapenem in a sterile fixed-dose combination. The pinanediol ester is generated in a 1.00–1.10 molar ratio with the boronic acid precursor in anhydrous 2-methyltetrahydrofuran; water is held below 300 ppm because the cyclic ester is more hydrolytically labile than the peptide boronate intermediates. Deprotection is carried out in a two-phase system of 2.0 N HCl and methyl tert-butyl ether at 0–5 °C; the aqueous layer is repeatedly extracted until the pinanediol concentration is below 0.10% w/w by gas chromatography. The final API is lyophilized with the antibiotic component at pH 5.0–6.0; the cycle includes a −40 °C freezing hold and a primary drying shelf temperature of −20 °C to −10 °C to prevent collapse. Sterile filtration occurs through a 0.2 µm polyethersulfone membrane, and the sterile bulk is filled into 10 mL glass vials under ISO 14644-1 Class 5 conditions. Release testing includes ICH Q3C for 2-methyltetrahydrofuran and methyl tert-butyl ether, ICH Q3D for boron and palladium, bacterial endotoxin testing per USP <85>, and particulate matter per USP <788>. The terminal product is a sterile lyophilized powder for intravenous infusion in a combination antibiotic regimen.

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    More Introduction

    The product listing (1S,2S,3R,5S)-(+)-2,3-Pinanediol intermediates Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable describes a chiral 1,2-diol intermediate supplied as model PIN-23P-PG. The material is not a direct dosage-form excipient; it is consumed during API synthesis for oral solid dosage forms and injectable products. The (1S,2S,3R,5S) configuration, CAS 18680-27-8, has molecular formula C10H18O2 and molecular mass 170.25 g mol−1. It is a white to off-white crystalline powder with a defined positive optical rotation. The (+) descriptor and the (1S,2S,3R,5S) stereochemical assignment distinguish this product from the (1R,2R,3S,5R)-(−)-enantiomer and from racemic 2,3-pinanediol. The pharmacopeial and ICH-aligned control of this intermediate is required because residual stereoisomers, solvents, water, and elemental impurities can propagate through the synthetic route into the final API.

    Stereoinduction is derived from the rigid bicyclo[3.1.1]heptane framework, not from a catalytic system added during the final API step. The material is typically prepared from α-pinene-derived feedstock; therefore, the absolute configuration is fixed by the terpene skeleton and enantiomeric purity is controlled by the stereoselectivity of the oxidation or resolution process. Residual α-pinene and oxygenated monoterpene impurities are controlled by gas chromatography because they can co-elute with the diol in non-chiral methods. A chiral GC method using a β-cyclodextrin stationary phase is required to separate the (1S,2S,3R,5S) enantiomer from the opposite enantiomer.

    What Specification Set Governs Release for Tablet, Capsule, Granule, and Injectable Routes?

    The specification set for model PIN-23P-PG is designed to support downstream API synthesis for oral and injectable dosage forms. Gas chromatographic assay and enantiomeric excess values are reported as area percent normalized against a qualified reference standard. Residual solvents are controlled according to ICH Q3C, and elemental impurities are managed by ICH Q3D risk assessment. Injectable-route APIs require additional endotoxin control because terminal sterilisation or aseptic filtration does not remove soluble organic impurities.

    Table 1: Release parameters for model PIN-23P-PG
    ParameterAcceptance criterionReference method
    AppearanceWhite to off-white crystalline powderVisual
    IdentificationIR spectrum corresponds to referenceUSP <197>, Ph. Eur. 2.2.24
    Specific optical rotation+7.5° to +9.5° (c=0.01 g/mL, CHCl3, 20°C)Ph. Eur. 2.2.7
    Melting range55–58°CUSP <741> or DSC
    Assay by GC98.5 % minimumUSP <621> GC-FID
    Enantiomeric excess99.0 % minimumChiral GC on β-cyclodextrin
    Water by Karl Fischer0.5 % maximumUSP <921>
    Residue on ignition0.1 % maximumUSP <281>
    Residual solventsDichloromethane ≤600 ppm; methanol ≤3000 ppm; other Class 2 and Class 3 solvents per ICH Q3CUSP <467>
    Elemental impuritiesRisk assessment per ICH Q3DICH Q3D, ICP-MS
    Bacterial endotoxin, injectable route0.25 EU/mg maximum where requiredPh. Eur. 2.6.14, USP <85>

    The chiral GC method for enantiomeric excess employs a capillary column of 25 m × 0.25 mm × 0.25 µm with a β-cyclodextrin stationary phase. Helium carrier gas is maintained at 1.2 mL/min with a split ratio of 50:1. The injector is maintained at 250°C, and the oven is programmed from 80°C to 220°C at 5°C/min. The retention times of the two enantiomers are verified against a qualified reference standard, and resolution between the enantiomers must be not less than 1.5. This separation is critical because the opposite enantiomer can act as a process-related impurity in chiral APIs.

    Residual solvents are controlled according to ICH Q3C because the intermediate is used in the synthesis of APIs. Dichloromethane is a Class 2 solvent with a permitted daily exposure of 6.0 mg/day, corresponding to 600 ppm under ICH Q3C Option 1. Methanol is Class 2 at 3000 ppm. If ethyl acetate or heptane are used during purification, they are Class 3 solvents with a total limit of 5000 ppm. Residual solvent data are obtained by headspace GC with flame ionisation detection and a validated internal standard.

    The primary use of this diol is as a chiral auxiliary for cyclic boronate ester formation. In a typical process, the diol and a boronic acid are refluxed in toluene or tetrahydrofuran under Dean-Stark conditions. A jacketed glass-lined reactor with anchor agitator at 60 rpm and jacket set point 90–95°C is used; equilibrium is confirmed when the overhead water content falls below 500 ppm by Karl Fischer titration. The cyclic boronate is sensitive to moisture and is stored as a dry solution under nitrogen. Transfer lines are purged with solvent and kept under positive nitrogen pressure. These conditions prevent hydrolysis back to the free boronic acid, which directly reduces the diastereomeric ratio in subsequent steps.

    The pinanediol boronate is then subjected to Matteson homologation at cryogenic temperature. The substrate is dissolved in anhydrous dichloromethane and cooled to between −78°C and −60°C in a reactor equipped with a two-stage cascade refrigeration unit. An organolithium or organomagnesium reagent is fed through a mass-flow-controlled line; internal temperature is maintained by limiting feed rate and jacket temperature. Local temperature gradients above 5°C reduce diastereomeric excess; therefore, pilot-plant reactors require calibrated thermocouples at the bottom and top zones. Laboratory studies report diastereomeric ratios above 99:1 for optimized pinanediol boronate homologations, but plant performance must be confirmed for each reactor geometry because mixing and cooling ramp differ from laboratory vessels.

    The auxiliary is removed by transesterification with BCl3 in dichloromethane at −40°C to −20°C or by oxidation with aqueous sodium periodate in acetonitrile–water. The cleavage endpoint is monitored by TLC or HPLC; released pinanediol is separated from the API intermediate by extraction after pH adjustment to 7.0–8.0. Residual pinanediol in the final API is quantified by GC or HPLC. The control limit must be justified under ICH Q3A for new drug substances; typical regulatory filings set the pinanediol-derived impurity at not more than 0.10–0.15 % area, but published data for this specific configuration are limited and must not be transferred between processes without qualification.

    For APIs intended for injectable presentations, the upstream control requirement is more stringent because terminal sterilisation or aseptic filtration does not remove soluble organic impurities. The supplier specification for injectable-route intermediates therefore adds bacterial endotoxin and, where relevant, bioburden testing. A typical endotoxin limit of 0.25 EU/mg is used when the downstream API is not depyrogenated; if the API manufacturing process includes validated depyrogenation, the limit is adjusted according to the process validation data. The same intermediate can be used for oral tablet, capsule, and granule routes when the API is manufactured under GMP and the residual solvent profile meets ICH Q3C.

    For oral solid dosage forms, the product is not present in the final tablet or capsule blend. Its influence is indirect: residual pinanediol in the API can affect crystallisation and impurity profile but does not function as a binder, filler, or disintegrant. Tablet compression of APIs derived from this chiral auxiliary is normally performed after final API crystallisation and milling; direct compression or roller compaction is used only after the residual impurity profile is confirmed to avoid low-melting eutectic behaviour. Capsule filling is less sensitive to residual diol, but dissolution consistency under USP <711> requires lot-to-lot API impurity control. Granulation with high-shear mixers or fluid-bed equipment does not add pinanediol; it processes the final API after purification, and the process is validated against API particle size, residual impurity, and water content. Published formulation data for pinanediol-derived APIs vary by molecular target, so formulation-specific stability and compatibility studies are required.

    When Pinanediol Is Evaluated Against Achiral and Enantiomeric Diol Auxiliaries

    The selection of this (1S,2S,3R,5S)-(+)-enantiomer over other 1,2-diols is controlled by the desired absolute configuration of the API intermediate. The bicyclo[3.1.1]heptane framework locks the two hydroxyl groups in a rigid conformation, which enhances stereofacial discrimination during boronate formation relative to acyclic auxiliaries. Racemic 2,3-pinanediol is unsuitable for asymmetric induction because both enantiomers compete; pinacol is achiral and provides no stereocontrol. Diisopropyl L-tartrate and similar tartrate-derived auxiliaries possess chirality but lack the rigid bicyclic geometry, and their esters are more hydrolytically labile.

    Table 2: Comparative profile of 1,2-diol auxiliaries in chiral boronic ester formation
    AuxiliaryStereochemical inductionPhysical state of boronateOperational limitation
    (1S,2S,3R,5S)-(+)-2,3-pinanediolHigh; rigid bicyclic scaffoldCrystalline, isolableMoisture-sensitive ester formation; cleavage requires BCl3 or NaIO4
    (1R,2R,3S,5R)-(−)-2,3-pinanediolHigh; opposite enantiomerCrystallineSame handling; use only for opposite absolute configuration
    Racemic 2,3-pinanediolNoneCrystalline or oilCannot control absolute configuration; not suitable for chiral API routes
    PinacolNoneOften liquid or low-meltingAchiral; does not induce asymmetry
    Diisopropyl L-tartrateModerate; acyclicLiquidHydrolytically labile; lower stereofacial bias in some homologations

    The difference between the (+)-enantiomer and the (−)-enantiomer is not merely a sign of optical rotation; the wrong enantiomer can produce the opposite API stereoisomer, which may be a separate impurity requiring pharmacological qualification. Racemic material may be offered at lower cost but does not provide the enantioselectivity required for chiral boronic ester API routes. Pinacol is useful for achiral boronic esters but lacks the rigid pinane framework. The use of pinacol in a chiral route would require a separate external chiral controller or resolution step, increasing unit operations and yield loss.

    Bulk handling must exclude atmospheric moisture. At relative humidity above 60 %, the diol should be pre-dried under vacuum at 35–40°C for 6–8 h until water content by Karl Fischer is below 0.5 %. The material is incompatible with strong oxidising agents during storage and should not be dry-milled with chloride-contaminated stainless steel if residual acidic species are present, because discolouration and corrosion-assisted degradation can occur. Do not combine the diol with amine-based additives in the same boronate ester reaction vessel unless compatibility has been evaluated; amines can compete with the diol for boron coordination and suppress the desired cyclic ester yield.

    Storage is specified at 2–8°C under nitrogen in sealed double polyethylene liners within a fibre drum. Repeated warming to ambient temperature is not recommended because condensation on crystal surfaces changes water content and can alter the stoichiometry of subsequent boronate formation. Each receiving site should verify optical rotation, assay, enantiomeric excess, and residual solvent profile on receipt. Supplier qualification should follow 21 CFR Part 211 expectations and ISO 15378:2017 for primary packaging. Published multi-ton campaign data for this specific configuration are limited; therefore, the operational ranges described above should be confirmed in the receiving reactor configuration and against the approved supplier certificate of analysis.

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