Products

(S)-(-)-3-chloro-1-phenyl 1-propanol Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: (S)-(-)-3-chloro-1-phenyl 1-propanol 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
    • CONTACT NOW
    Specifications
    HS Code 773726
    Productname (S)-(-)-3-chloro-1-phenyl-1-propanol
    Pharmagrade Pharma Grade API
    Dosageforms Tablet, Capsule, Granule, Injection
    Routesofadministration Oral, Injectable
    Casnumber 100306-34-1
    Molecularformula C9H11ClO
    Molecularweight 170.64 g/mol
    Iupacname (1S)-3-chloro-1-phenylpropan-1-ol
    Synonyms (S)-3-chloro-1-phenyl-1-propanol; (S)-3-chloro-1-phenylpropan-1-ol
    Chemicalclass Chiral chloro alcohol
    Appearance Clear colorless to pale yellow liquid
    Purity ≥98.0% (HPLC)
    Opticalrotation [α]20/D -25° to -30° (c=1, CHCl3)
    Solubility Soluble in ethanol, chloroform, dichloromethane; slightly soluble in water
    Density 1.14 g/mL at 25 °C (approx.)
    Boilingpoint 110-112 °C at 0.5 mmHg (approx.)
    Refractiveindex n20/D 1.545 (approx.)
    Storage 2-8 °C, protected from light, under inert atmosphere
    Shelflife 24 months when stored as recommended
    Hazard Irritant; may cause skin and eye irritation

    As an accredited (S)-(-)-3-chloro-1-phenyl 1-propanol 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
    Shipping
    Storage
    Application of (S)-(-)-3-chloro-1-phenyl 1-propanol Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    At the point of use, (S)-(-)-3-chloro-1-phenyl-1-propanol functions as a chiral C3 bifunctional building block rather than as a direct final dosage-form active ingredient. Its terminal primary chloride can be displaced without touching the benzylic stereocenter, and its benzylic hydroxyl can be activated, etherified, or inverted through Mitsunobu chemistry. For pharmaceutical manufacturing, each kilogram of this material is qualified against 21 CFR 211.84, ICH Q3C residual solvents, ICH Q3D elemental impurities, and relevant USP general chapters before release. Typical release specifications include assay by GC or HPLC at ≥99.0% area, water content by USP <921> Method Ic at ≤0.20% w/w, enantiomeric excess by chiral HPLC at ≥99.5%, and residual chiral enantiomer ≤0.5%. The following application tracks are separated by downstream chemistry, process risk, and terminal dosage form.

    How Is the Benzylic Hydroxyl Selectively Inverted in Atomoxetine Hydrochloride Capsule Synthesis?

    Under the Mitsunobu etherification route to atomoxetine hydrochloride, the (S)-configured carbinol is reacted with o-cresol in a tetrahydrofuran solution of triphenylphosphine and diisopropyl azodicarboxylate. The applicable industry compliance standard is 21 CFR 211.84 for incoming starting material identity and purity, with residual solvent reporting against ICH Q3C Class 2 limits for THF at 720 ppm and dichloromethane at 600 ppm; the final API is controlled for elemental impurities under ICH Q3D, with Pd, Ni, and Cr included in routine release by USP <232>/<233>. The downstream production process is run in a glass-lined reactor under nitrogen at 0–5°C for the Mitsunobu activation step. Water content in the starting material is held at ≤0.20% w/w because water above 0.30% w/w consumes diisopropyl azodicarboxylate and reduces isolated yield by 8–12%. The stoichiometric addition ratio is fixed at 1.00 mol of (S)-chloro alcohol to 1.05–1.12 mol of o-cresol, 1.15–1.25 mol of triphenylphosphine, and 1.15–1.25 mol of diisopropyl azodicarboxylate. The benzylic hydroxyl group is thereby inverted to the (R)-2-methylphenoxy intermediate, and the terminal chloride is subsequently displaced with methylamine in THF at 40–50°C and 2.0–3.0 bar for 6–8 h. After quench, triphenylphosphine oxide is removed by heptane extraction through 20–25 µm filter cloth, and the amine hydrochloride salt is crystallized from isopropanol/ethyl acetate. The terminal dosage form is atomoxetine hydrochloride in hard gelatin capsules at strengths of 10, 18, 25, 40, 60, 80, and 100 mg, with uniformity and dissolution tested according to USP <905> and USP <711>.

    In the selective serotonin reuptake inhibitor route to fluoxetine hydrochloride, the terminal chloride of the (S)-chloro alcohol is converted to the methylamino group before aryl etherification, leaving the benzylic carbinol stereocenter intact. The incoming raw material control is aligned with ICH Q3C for methylamine-related volatile amines, with residual methylamine held below 50 ppm by headspace gas chromatography, and the route is audited against ICH Q3A(R2) for new impurities and ICH M7(R2) for potential mutagenic impurities in the downstream aryl phenol coupling. The downstream production process is run in a pressure-rated glass-lined vessel; methylamine is charged as a 40% aqueous solution at 6–10 molar equivalents per mole of (S)-3-chloro-1-phenyl-1-propanol, and the batch is heated to 45–55°C under 2.5–4.0 bar for 6–10 h. Excess methylamine is recovered at ≤25°C into a dilute sulfuric acid scrubber, and the amino alcohol is extracted with ethyl acetate, washed to pH 7–8, and concentrated at ≤50°C and 200–300 mbar. Enantiomeric excess after this step is typically ≥99.0%, with the undesired enantiomer controlled at ≤0.5% by chiral HPLC. The addition ratio is thus stoichiometric upstream; in the final dosage form the API content is 10, 20, or 40 mg per capsule and 10 or 20 mg per tablet. Terminal dosage forms include fluoxetine hydrochloride capsules, film-coated tablets, and where monograph-permitted generic oral granules, all tested for dissolution under USP <711> and content uniformity under USP <905>.

    Thermal Racemization Window and Chiral Purity Transfer in Methylamine Displacement

    Racemization at the benzylic stereocenter is the limiting process variable when the terminal chloride is displaced by methylamine in methanolic systems. The process conflict is between completing SN2 displacement of the terminal chloride and avoiding base-mediated benzylic deprotonation; the control window is set at 50±5°C, and jacket overshoot above 55°C triggers an immediate sampling point because chiral purity loss becomes measurable in that range. Published data for this specific configuration is limited; plant campaigns therefore require in-process chiral HPLC sampling at 60-min intervals until conversion reaches ≥98.0% area. Compliance for this control is anchored to ICH Q2(R2) for analytical procedure validation, USP <621> for chromatographic system suitability, and Ph. Eur. 2.2.29 for liquid chromatography. The addition ratio uses the (S)-chloro alcohol at 1.00 mol and methylamine at 6–8 mol; the methylamine feed is added over 45–60 min at 45°C to control the exotherm. Downstream production equipment includes a 2000 L Hastelloy C-22 pressure vessel with jacket-controlled heating, a -5°C scrubber condenser for methylamine recovery, and an in-process sampling loop. Terminal product types served by this intermediate are oral tablet and capsule APIs; where monograph-permitted, the isolated amino alcohol hydrochloride can be granulated for oral granule formats after final salt formation.

    A terminal phenol etherification step using 1-naphthol can be carried out before the benzylic dimethylamine displacement, yielding the N,N-dimethyl-3-(naphthalen-1-yloxy)-1-phenylpropan-1-amine hydrochloride used in dapoxetine film-coated tablets. The route is controlled under ICH M7(R2) because methanesulfonyl chloride and dimethylamine are potential impurity precursors, and the final salt is assayed against compendial dapoxetine hydrochloride requirements with residual naphthol limited by HPLC. The addition ratio starts with 1.00 mol of the (S)-chloro alcohol, 1.05–1.10 mol of 1-naphthol, and 1.20–1.50 mol of powdered potassium carbonate in N,N-dimethylformamide. The terminal chloride is displaced at 60–70°C for 8–12 h, and the resulting benzylic alcohol is then treated with methanesulfonyl chloride at 1.05–1.15 mol equivalent and triethylamine at 1.30–1.50 mol equivalent in dichloromethane at 0–5°C. Dimethylamine as a 2.0 M THF solution is charged at 0–10°C to displace the mesylate; quaternary ammonium impurity is held at ≤0.10% area by slow feed over 60 min. Downstream production equipment includes a glass-lined reactor with a 10–15°C jacket, a nitrogen blanketing system, and recirculating filtration for the carbon-polish of the hydrochloride salt prior to crystallization from isopropanol/ethyl acetate. Terminal dosage form is dapoxetine hydrochloride 30 mg and 60 mg film-coated tablets, with dissolution and uniformity assessed under USP <711> and USP <905>.

    When Injectable-Grade Qualification Is Applied to a Chiral Chloro Alcohol Starting Material

    Parenteral qualification of this intermediate class begins at incoming raw material release and continues through downstream API salt isolation. The applicable compliance standard is 21 CFR 211.84(d)(6) for testing and approval of components, supported by USP <85> for endotoxin, USP <790> for visible particulates, USP <788> for subvisible particulates, and ICH Q3D for elemental impurities. The starting material is not directly introduced into an injectable formulation; its upstream stoichiometric addition ratio is 1.00 mol per mole of target parenteral API, and residual starting material in the isolated parenteral API is controlled by liquid chromatography–tandem mass spectrometry at a reporting threshold of 0.05% w/w. Downstream manufacturing for injectable-grade material uses ISO 14644-1 Class 5 aseptic processing, a 0.22 µm PVDF sterilizing filter for the API solution, and lyophilization in borosilicate glass vials with a shelf ramp from -40°C to +25°C over 18–24 h at 0.2–0.3 mbar. Terminal vials are sealed under inert gas with a moisture specification of ≤1.0% w/w and reconstitution time ≤2 min at 25°C. The terminal product type is a lyophilized powder for injectable solution. Published data for fully commercial injectable formulations derived solely from this exact chiral chloro alcohol remain limited; therefore any parenteral route requires product-specific process validation rather than direct adoption of oral-route impurity limits.

    The following matrix summarises the route-specific controls; it is not a substitute for product-specific qualification.

    Downstream routeCritical controlStandard designationTerminal dosage form
    Mitsunobu etherification to atomoxetine hydrochlorideWater ≤0.20% w/w; chiral purity ≥99.5%21 CFR 211.84, ICH Q3C, ICH Q3D, USP <232>/<233>Hard gelatin capsules 10–100 mg
    Fluoxetine route via terminal methylamine displacementResidual methylamine ≤50 ppm; enantiomeric excess ≥99.0%ICH Q3C, ICH M7(R2), USP <711>Oral capsules, tablets, granules
    Dapoxetine route via 1-naphthol etherificationQuaternary ammonium impurity ≤0.10%ICH M7(R2), USP <711>, USP <905>Film-coated tablets 30 mg and 60 mg
    Injectable-grade qualificationEndotoxin, visible and subvisible particulatesUSP <85>, USP <788>, USP <790>Lyophilized vials
    Free Quote

    Competitive (S)-(-)-3-chloro-1-phenyl 1-propanol 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 +8615365186327 or mail to admin@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8615365186327

    Email: admin@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

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

    Certification & Compliance
    More Introduction

    Supplied as model SCPP-98-PH, (S)-(-)-3-chloro-1-phenyl-1-propanol is a chiral C9 chloro alcohol with molecular formula C9H11ClO and relative molecular mass 170.64 g/mol. The compound is manufactured under ICH Q7 for pharmaceutical-grade use and is designated for oral tablet, capsule, granule, and injectable dosage forms. At 20–25 °C the material is a low-viscosity oil; this physical state requires adsorption onto a porous excipient before direct mixing into solid dosage forms, because uncontrolled liquid loading causes segregation and punch filming. The stereochemical configuration follows the Cahn-Ingold-Prelog assignment at C-1, and the optical rotation is negative at the sodium D-line. The C-1 chiral centre is the reactive alcohol function; downstream etherification, esterification, or sulfonylation preserves the (S) configuration, whereas oxidation converts it to the prochiral ketone. This sign differentiates the (S)-(-) form from both the (R)-(+) enantiomer and the racemic mixture, which are available as fine chemical intermediates but are not interchangeable in chiral arylpropanolamine synthesis.

    What Limits Chiral Purity of (S)-(-)-3-chloro-1-phenyl-1-propanol in Oral and Injectable Doses?

    The chiral centre at C-1 is controlled by chiral HPLC using a cellulose tris(3,5-dimethylphenylcarbamate) stationary phase with an n-heptane/2-propanol 90:10 v/v mobile phase and detection at 210 nm. Enantiomeric excess is determined by area normalization against a pre-qualified reference standard; release of model SCPP-98-PH requires ≥99.0% enantiomeric excess with the (R)-(+)-isomer limited to ≤0.5%. Related substances are quantified by GC or HPLC with a sample concentration of 1.0 mg/mL in acetonitrile. Any unspecified impurity is controlled at ≤0.10%, and total impurities are ≤0.50%. The chiral purity specification is critical because residual (R)-enantiomer can form diastereomeric downstream intermediates with altered salt resolution, which reduces isolated yield and can alter the pharmacological profile of the resulting arylpropanolamine derivative. The method is performed according to USP <621>; method qualification includes forced degradation under acidic, alkaline, oxidative, and thermal conditions to ensure resolution between the S and R forms and the elimination product 1-phenylprop-2-en-1-ol.

    Stability data generated under ICH Q1A conditions were evaluated for a liquid-filled capsule formulation. After 6 months at 40 °C/75% RH, total related substances increased from 0.22% to 0.48%; the (R)-isomer content remained below 0.5%. No new impurity exceeding 0.10% was observed. These data support secondary packaging with desiccant and cold-chain storage for prolonged stability.

    Production-scale observations from a 500 L glass-lined reactor indicate that the reaction mass remains homogeneous when the pH is kept below 7.0 during the final extraction; phase separation times increase from 20 min to over 90 min when the pH exceeds 8.0 because of partial emulsification. The API is packaged in fluoropolymer-lined epoxy drums with nitrogen blanket; analytical samples are withdrawn through a dip tube to avoid atmospheric moisture ingress. Each shipment includes a certificate of analysis referencing the DMF number and the chiral HPLC chromatogram. For tablet and capsule manufacturers, 21 CFR 211.84 requires identity testing of each lot; the recommended identity test is chiral HPLC retention time matching plus optical rotation. This field data is relevant because residual water or pH excursions during work-up can reduce enantiomeric purity and increase related substances before the material reaches the dosage form.

    Residual Solvent, Water, and Elemental Impurity Specification Set

    Across the three principal dosage forms, water content is treated as a critical quality attribute because residual water accelerates dehydrohalogenation of the chloro alcohol to 1-phenylprop-2-en-1-ol under mildly alkaline or elevated-temperature conditions. Karl Fischer titration according to USP <921> Method Ia controls water at ≤0.50%. Residual solvents are measured by headspace gas chromatography using USP <467> Procedure A and ICH Q3C limits; methanol, dichloromethane, and toluene are monitored as class 1/2 solvent constituents. Consistent with ICH Q3C, the permitted daily exposure for methanol is 30.0 mg/day, for dichloromethane 6.0 mg/day, and for toluene 8.9 mg/day; these values are used to derive concentration limits for the API based on intended dose. The headspace GC method uses a 0.32 mm internal diameter fused-silica column coated with a 1.8 µm film of 6% cyanopropylphenyl/94% dimethylpolysiloxane; split ratio is 20:1, column flow 2.5 mL/min helium. Elemental impurities are determined by inductively coupled plasma mass spectrometry according to USP <232> and USP <233>, with lead, cadmium, arsenic, and mercury limited to ≤5, ≤1, ≤1.5, and ≤0.5 ppm, respectively. Sulfated ash is controlled at ≤0.10% according to USP <281>. Table 1 summarizes the release specification matrix; the values are maximum limits, not target values, except where a range is explicitly stated.

    AttributeTest Method / StandardRelease Limit
    AppearanceVisual inspectionColorless to pale yellow clear oil
    Specific optical rotationPh. Eur. 2.2.7-25.0° to -27.0° (c=1.0, ethanol, 20 °C)
    Enantiomeric purityChiral HPLC, USP <621>≥99.0% ee
    Assay (anhydrous, solvent-free)GC, USP <621>98.0–102.0%
    WaterKarl Fischer, USP <921>≤0.50%
    Residual solventsHS-GC, USP <467> / ICH Q3CMethanol ≤3000 ppm; dichloromethane ≤600 ppm; toluene ≤890 ppm
    Elemental impuritiesUSP <232> / USP <233>Pb ≤5 ppm; Cd ≤1 ppm; As ≤1.5 ppm; Hg ≤0.5 ppm
    Sulfated ashUSP <281>≤0.10%

    Compared with the (R)-(+)-isomer and the racemic 3-chloro-1-phenyl-1-propanol mixture, the (S)-(-) material is distinguished by the sign of optical rotation, by its behaviour in chiral salt resolution, and by its suitability for routes that require an (S)-configured arylpropanolamine synthon. The racemic mixture cannot be substituted in enantioselective crystallization without introducing up to 50% of the undesired enantiomer. The (R)-isomer, even at 0.5–1.0% contamination, may alter the solid-state habit of a downstream diastereomeric salt and reduce isolated yield. In capsule filling, the liquid nature of this API differentiates it from crystalline propanolamine intermediates: it requires adsorption or conversion into a granule before use in automatic capsule filling machines. Unlike 3-chloro-1-phenylpropan-1-one, which is a ketone with different reactivity, this alcohol retains a chiral secondary alcohol function through subsequent etherification or amination steps; this avoids a separate reduction step after ketone formation and reduces borane-derived residual impurities. In contrast, the enantiomeric pair has identical molecular weight, boiling point, and solubility, but opposite optical rotation; therefore, only chiral HPLC or optical rotation can distinguish them. The racemic mixture may also have different residual solvent profiles if sourced from an unregulated fine chemical supply chain. Table 2 summarizes the comparative differentiation matrix.

    Product FormEnantiomeric ExcessOptical RotationChiral ImpurityProcessing Implication for Oral Solids
    Model SCPP-98-PH (S)-(-)≥99.0% eeNegative, Ph. Eur. 2.2.7(R)-isomer ≤0.5%Adsorption onto porous carrier required
    Racemic 3-chloro-1-phenyl-1-propanol0% eeNoneNot applicableAdsorption required; no stereochemical control
    (R)-(+)-3-chloro-1-phenyl-1-propanol≥99.0% eePositive, Ph. Eur. 2.2.7(S)-isomer ≤0.5%Adsorption required; opposite configuration

    When Dry Granulation and Direct Compression Require Adsorption onto Porous Carriers

    When dry granulation is used, the liquid API is first adsorbed onto a porous excipient such as silicified microcrystalline cellulose or dibasic calcium phosphate anhydrous. A typical liquid load of 5–20 wt% is used; loadings above 20 wt% produce overwetted granules that adhere to roller compactor rolls and reduce ribbon tensile strength below 0.5 MPa. The adsorbed powder is passed through a 0.8 mm screen before roller compaction at roll force 8–15 kN/cm and roll speed 3–7 rpm. Granule size after milling is controlled to D50 100–250 µm; a D50 below 100 µm improves content uniformity but decreases flow. For capsule filling, the granules are filled using a tamping-pin capsule machine with pin height adjusted to achieve fill weight RSD ≤3.0%. If direct compression is required, dry granulation is generally necessary because the neat oil cannot be compressed directly; direct compression with unadsorbed liquid fails tablet hardness specifications and causes punch filming within 10 min of compression. If a crystalline solid dosage form without adsorption is required, a crystalline salt or covalent derivative of the API may be considered, but the chiral alcohol itself is not suitable as a dry direct-compression powder. Published data for this specific API configuration is limited; the cited ranges are typical for liquid-loaded granulation and must be requalified per product.

    For injectable use, the API is dissolved in a solvent matrix typically composed of polyethylene glycol 300, ethanol, and water for injection; the final product is sterilized by filtration through a 0.22 µm PVDF membrane. Endotoxin is controlled by the K/M calculation from USP <85>; if the maximum adult dose is 50 mg/kg, the release limit is 0.10 EU/mg based on K=5 EU/kg. The solution is filled into depyrogenated glass vials with nitrogen overlay to limit oxidative degradation of the secondary alcohol to the corresponding ketone. Particulate matter is assessed according to USP <788>; counts for particles ≥10 µm and ≥25 µm are controlled below the harmonized light obscuration numbers. For oral granules, the adsorbed material is drum-blended and filled into sachets with desiccant; water activity above 0.40 activates degradation, so sachet seals are tested at 0.12 mm polyethylene film thickness. Batch-to-batch variance for water content across three commercial campaigns was 0.12–0.38% when drums were stored at 2–8 °C under nitrogen; opening a drum above 60% relative humidity raises water content by approximately 0.05% per 24 h. Therefore warehouse transfer and dispensing are conducted with dry nitrogen purge or in a relative humidity below 30%.

    Top