| HS Code | 590325 |
| Product Name | Ortho-Nitrobenzyl Alcohol |
| Chemical Name | 2-Nitrobenzyl Alcohol |
| Synonyms | o-Nitrobenzyl Alcohol; 2-Nitrobenzenemethanol; 2-Nitrophenylmethanol |
| Cas Number | 612-25-9 |
| Einecs Number | 210-302-1 |
| Molecular Formula | C7H7NO3 |
| Molecular Weight | 153.14 g/mol |
| Appearance | Yellow to light brown crystalline powder |
| Assay Purity | ≥98.0% (HPLC) |
| Grade | Pharma Grade / API Intermediate |
| Melting Point | 69-73 °C |
| Boiling Point | 267.8 °C at 760 mmHg |
| Flash Point | 115.8 °C |
| Density | 1.3 g/cm³ |
| Solubility | Soluble in ethanol, ether, chloroform; slightly soluble in water |
| Storage Conditions | Store in a cool, dry, well-ventilated area protected from light and heat |
| Dosage Form Suitability | Tablet, Capsule, Granule, Oral, Injection, Injectable as API intermediate |
| Application | Pharmaceutical intermediate; photolabile protecting group in organic synthesis |
| Packaging | 25 kg fiber drum or custom packaging |
| Shelf Life | 2 years under proper storage |
| Hs Code | 2906.29.00 |
As an accredited Ortho-Nitrobenzyl Alcohol 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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In oral solid dosage manufacture, ortho-nitrobenzyl alcohol (CAS 612-25-9) enters the API supply chain as a controlled intermediate rather than as a directly compressible active. The primary commercial route for 1,4-dihydropyridine calcium channel blockers oxidizes ortho-nitrobenzyl alcohol to 2-nitrobenzaldehyde (CAS 552-89-6), which is then condensed with methyl acetoacetate and ammonia in a Hantzsch reaction. Nifedipine (CAS 21829-25-4), nimodipine (CAS 66085-59-4), nitrendipine (CAS 39562-70-4) and nisoldipine (CAS 63675-72-9) share this downstream dependency. Pharma-grade ortho-nitrobenzyl alcohol is therefore specified for melting range (69–72 °C), residual 2-nitrobenzaldehyde, total heavy metals, loss on drying and purity by HPLC. In tablet and capsule production, the downstream dihydropyridine APIs are poorly water-soluble and photolabile, so processing requires particle size reduction to a D90 below 25 µm, protective amber lighting, and surfactant-containing dissolution testing under USP <711>. Content uniformity is assessed by USP <905>. The oxidation status of the intermediate batch influences residual aldehyde levels in the crystallized API, and this impurity class is critical because aldehydes crosslink gelatin capsule shells. Liquid-filled nifedipine soft gelatin capsules typically use polyethylene glycol and other water-miscible fill vehicles; low-molecular-weight aldehydes react with gelatin lysine residues to form a crosslinked pellicle at the capsule–fill interface. The pellicle retards capsule rupture, produces biphasic dissolution curves, and is accelerated by storage above 40 °C or above 40% relative humidity. Capsule manufacturers therefore apply aldehyde limits to the API and to the fill excipients, specify gelatin bloom strength, and monitor dissolution in both fresh and accelerated stability samples. Residual solvent control under ICH Q3C is equally batch-defining because the oxidation and recrystallization train may retain methanol, dichloromethane or ethyl acetate, and the choice of final recrystallization solvent determines the residual solvent profile for the downstream dosage form.
The question is not rhetorical: 2-nitrobenzaldehyde is a necessary building block in dihydropyridine synthesis, but its carryover as an unreacted impurity has formulation-specific consequences that differ between tablet, capsule and injectable presentations. In oral tablets, residual 2-nitrobenzaldehyde at low parts-per-million levels does not produce the same failure mode because the tablet core contains no gelatin and the aldehyde can be diluted or volatilized during wet granulation drying. In liquid-filled soft gelatin capsules, however, the aldehyde remains in intimate contact with the capsule shell for the entire shelf life. Aldehyde-mediated gelatin crosslinking occurs when free aldehyde groups form Schiff bases with the epsilon-amino groups of lysine residues, followed by aldol condensation or further crosslinking under thermal stress. The resulting membrane is less soluble in aqueous acid, causing capsule rupture times to lengthen and dissolution profiles under USP <711> to fall outside acceptance criteria. The failure is not linear with aldehyde concentration; published pharmaceutical capsule studies indicate that pellicle formation can be negligible below a threshold but increases rapidly above an aldehyde-to-gelatin molar ratio that depends on bloom strength, plasticizer content and residual moisture. For this reason, pharma-grade ortho-nitrobenzyl alcohol used for nifedipine intermediates is often specified for 2-nitrobenzaldehyde content by HPLC with a quantification limit below 0.05%, and the downstream API is tested for total aldehydes using a pharmacopeial method where available. Because no general pharmacopeial monograph exists for ortho-nitrobenzyl alcohol itself, the user normally writes a supplier specification under ICH Q7 and applies ICH Q3A(R2) impurity thresholds to the derived API. The ICH Q3A(R2) reporting threshold for new drug substances is 0.05%, the identification threshold is 0.10%, and the qualification threshold is 0.15% for a maximum daily dose not exceeding 2 g/day.
| API | CAS | Representative dosage form | Key pharmacopeial/standards references |
|---|---|---|---|
| Nifedipine | 21829-25-4 | Immediate-release capsules, extended-release oral tablets | USP <711>, USP <905>, ICH Q1B |
| Nimodipine | 66085-59-4 | Oral capsules, injectable solution | USP <1>, USP <711>, USP <85> |
| Nitrendipine | 39562-70-4 | Oral tablets | USP <711>, USP <905> |
| Nisoldipine | 63675-72-9 | Extended-release oral tablets | USP <711>, USP <905>, USP <1216> |
Injectable nimodipine concentrate manufacture places additional demands on ONBA-derived API quality because the route terminates in a sterile solution or concentrate that cannot be purified by crystallization after filtration. Nimodipine injection formulations typically use ethanol and polyethylene glycol 400 as solubilizers, with water for injection and a citrate buffer, and are supplied in amber glass ampoules or vials. The API must meet low bioburden and endotoxin limits before sterile filtration because the terminal filtration step removes particulate matter but does not remove endotoxins. For a parenteral product, USP <1> Injections, USP <85> Bacterial Endotoxins and USP <788> Particulate Matter in Injections apply. Ortho-nitrobenzyl alcohol-derived intermediates that contain residual heavy metals from chromium-based oxidation streams are particularly problematic for injectable dihydropyridines because heavy metal limits for parenteral products are more restrictive than those for oral solid dosage. If a chromium reagent is used to convert ortho-nitrobenzyl alcohol to 2-nitrobenzaldehyde, the API purification must demonstrate quantitative removal of chromium species to below the limit stated in the product registration file, and the oxidation route is often replaced with catalytic air oxidation or TEMPO–sodium hypochlorite systems to avoid heavy metal carryover. Injectable dihydropyridine APIs also require tight control of the ethanol and aldehyde content because ethanol is a common residual solvent from recrystallization and may interact with the final formulation solvent system. Photostability is a manufacturing constraint: nimodipine solutions are light-sensitive, and the filling line must use amber glass and low-actinic lighting because exposure to fluorescent light generates oxidized nitropyridine analogues and changes potency. Filling of nimodipine concentrates into glass ampoules is performed under nitrogen overlay to limit oxygen-mediated degradation. The API particle size specification is less critical for injectable solutions than for tablets, but solution filtration compatibility must be confirmed through filter validation studies using membrane filters with pore sizes of 0.2 µm or smaller.
The conversion of ortho-nitrobenzyl alcohol to 2-nitrobenzaldehyde is an alcohol-to-aldehyde oxidation with a narrow process window because over-oxidation produces 2-nitrobenzoic acid (CAS 552-16-9) and under-oxidation leaves residual alcohol. In a glass-lined reactor equipped with a retreat-curve agitator, the reaction mass is charged with the alcohol, a solvent such as dichloromethane or ethyl acetate, and an oxidant system. The jacket is held below 30 °C because the benzylic alcohol group is readily oxidized and the reaction releases heat; higher temperatures accelerate over-oxidation to the carboxylic acid and increase the formation of aldol condensation by-products. Agitation rate controls the mass transfer of the oxidant into the organic phase and the removal of heat from the reactor wall. Low agitation can produce a stagnant boundary layer at the wall where local temperature exceeds the bulk set point and acid impurity formation rises. High agitation can entrain air into the headspace and increase oxidative degradation of the product aldehyde. The pH of the aqueous phase, when a two-phase hypochlorite system is used, must be maintained between 8.0 and 9.5 because the active chlorine species shifts from hypochlorous acid to hypochlorite as pH increases. Outside this range, the reaction rate changes and the formation of chlorinated by-products may occur. Process analytical technology is typically limited to offline HPLC sampling of an aliquot quenched with sodium bisulfite to stop the oxidation. Residual ortho-nitrobenzyl alcohol in the isolated 2-nitrobenzaldehyde is specified below 0.5% by HPLC for downstream Hantzsch condensation because residual primary alcohol can participate in side reactions with methyl acetoacetate and ammonia and reduce reaction selectivity. Published kinetic parameters for exact industrial glass-lined reactor conditions are limited because oxidation process details are proprietary; however, the general sensitivity of benzylic alcohol oxidation to temperature, pH and agitation is well documented in process chemistry literature.
Ortho-nitrobenzyl alcohol and its substituted derivatives are employed in experimental drug delivery research as photolabile protecting groups because the o-nitrobenzyl moiety undergoes intramolecular hydrogen abstraction and subsequent cleavage when irradiated with ultraviolet light in the 350–365 nm range. In polymer–drug conjugates, an o-nitrobenzyl linkage can connect a therapeutic peptide or small molecule to a poly(ethylene glycol) or hydrogel backbone, and irradiation triggers release at the site of illumination. This chemistry is not used as a direct injectable formulation of unmodified ortho-nitrobenzyl alcohol, and no approved injectable product is known to contain ortho-nitrobenzyl alcohol as the active pharmaceutical ingredient. Published data for approved injectable products using unmodified ONBA is limited. The importance of the o-nitrobenzyl group lies in the synthesis of cleavable protecting groups and linkers for research-grade injectable depots, light-activated antibody–drug conjugates, and photocleavable peptide scaffolds. Such systems are evaluated in vitro using UV reactors with wavelength-selected lamps, and degradation is measured by HPLC with photodiode-array detection. For any parenteral development candidate based on an o-nitrobenzyl linker, biocompatibility data must be generated under ISO 10993 because the photocleavage products include nitrosobenzaldehyde intermediates that may be reactive toward proteins. The cleavage efficiency depends on substitution on the benzyl ring, solvent polarity, and light intensity; ortho-nitrobenzyl alcohol derivatives with electron-donating or electron-withdrawing groups at the 4- or 5-position shift the UV maximum and change the quantum yield. As a result, the pharmaceutical intermediate market supplies ortho-nitrobenzyl alcohol primarily as a starting material for substituted o-nitrobenzyl alcohols and o-nitrobenzyl chloroformates rather than as a drug substance itself.
Ortho-nitrobenzyl alcohol is converted to 2-nitrobenzyl chloroformate by reaction with phosgene or triphosgene under anhydrous conditions. The chloroformate then reacts with amino acids and peptide intermediates to introduce the 2-nitrobenzyloxycarbonyl protecting group, which is cleaved by hydrogenolysis or by photolysis in research settings. In solid-phase peptide synthesis of injectable peptide APIs, the choice of N-terminal protecting group is usually 9-fluorenylmethoxycarbonyl or tert-butoxycarbonyl because those chemistries are validated for large-scale solid-phase manufacturing; 2-nitrobenzyl chloroformate is used when a photolabile or hydrogenolytically cleavable protecting group is required for orthogonal protection of a side-chain amine or for peptide conjugate synthesis. The pharma-grade ortho-nitrobenzyl alcohol used for this conversion must be free of water and residual acid because chloroformate yield is sensitive to moisture. A water content below 0.1% is typically specified for ortho-nitrobenzyl alcohol destined for chloroformate synthesis. The resulting 2-nitrobenzyl chloroformate is assayed by derivatization with a primary amine and HPLC analysis of the resulting carbamate. In peptide API manufacturing, the crude peptide is purified by preparative HPLC and lyophilized to a sterile powder for injection. Peptide APIs such as leuprolide, goserelin and octreotide are manufactured under ICH Q7 and release-tested against USP <1> when formulated as injectable products. Ortho-nitrobenzyl alcohol is not present in the final peptide API; it is a process intermediate used to prepare the protecting reagent, and residual 2-nitrobenzyl alcohol or 2-nitrobenzyl chloroformate in the peptide synthesis stream is controlled through the manufacturing process. Published data on the exact consumption ratio of ortho-nitrobenzyl alcohol in commercial peptide API campaigns is limited because peptide synthesis routes are proprietary.
| Requirement | Specification or limit | Standard/reference |
|---|---|---|
| Reporting threshold for impurities in new drug substances | 0.05% | ICH Q3A(R2) |
| Identification threshold for impurities | 0.10% | ICH Q3A(R2) |
| Qualification threshold for impurities | 0.15% | ICH Q3A(R2) |
| Methanol residual solvent limit | 3000 ppm | ICH Q3C Class 2 |
| Dichloromethane residual solvent limit | 600 ppm | ICH Q3C Class 2 |
| Ethyl acetate residual solvent limit | 5000 ppm | ICH Q3C Class 3 |
| Bacterial endotoxins for injectable products | Monograph-defined limit | USP <85> |
| Particulate matter in injections | Monograph-defined limit | USP <788> |
| Tablet friability | Monograph-defined limit | USP <1216> |
| Disintegration | Monograph-defined limit | USP <701> |
Granulation of ONBA-derived dihydropyridine APIs for extended-release tablets is constrained by the low aqueous solubility and photolability of the active. High-shear wet granulation with lactose monohydrate, microcrystalline cellulose, crospovidone and magnesium stearate is used, but the granulation endpoint must be controlled because over-granulation increases granule density and retards drug release from the matrix. The API particle size distribution is typically measured by laser diffraction, and the D90 is specified below 25 µm for content uniformity in low-dose tablets. Residual moisture after drying is specified below 3.0% because higher moisture increases sticking during compression and accelerates dihydropyridine oxidation. Magnesium stearate is added at 0.5–1.5% by weight and blended for a defined number of revolutions; excessive blending reduces tablet tensile strength and increases disintegration time. Compression force is adjusted to a tablet hardness of 5–10 kp for immediate-release nifedipine tablets, while extended-release formulations may use osmotic pump or matrix technology. Tablet friability is assessed by USP <1216> and disintegration by USP <701>. Dissolution testing under USP <711> often uses a surfactant-containing medium because the APIs require solubilization; the accepted dissolution medium is defined in the individual monograph and must be validated for peak separation from photodegradation products. Batch-to-batch variability in ortho-nitrobenzyl alcohol oxidation can alter the impurity profile of the dihydropyridine API and thereby shift dissolution and content uniformity results, which is why API suppliers include oxidation state markers on the certificate of analysis.
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Ortho-nitrobenzyl alcohol (2-nitrobenzyl alcohol; CAS 612-25-9; molecular formula C7H7NO3; relative molecular mass 153.14 g·mol−1) is supplied as a controlled pharmaceutical intermediate under two release models: ONBA-PH-OSD for tablet, capsule, and granule manufacturing and ONBA-PH-INJ for parenteral processing. The oral model is released as a white to pale yellow crystalline powder with HPLC assay ≥99.0% area, water content ≤0.5% by USP 〈921〉 Method Ia, and residue on ignition ≤0.10% by USP 〈281〉. The injectable model is milled under ISO 14644-1 ISO Class 7 conditions to a laser-diffraction particle size d90 ≤40 µm and is released with bacterial endotoxin ≤0.25 EU/mg by USP 〈85〉 and total aerobic microbial count ≤10 CFU/g by USP 〈61〉. The material is not a finished drug product; it is controlled as an API starting material under ICH Q7 and is intended for subsequent chemical conversion into active pharmaceutical ingredients used in oral and injectable dosage forms.
The ortho-nitro group enables a six-membered intramolecular hydrogen transfer during ultraviolet excitation, yielding 2-nitrosobenzaldehyde and the cleaved alcohol through a route that is not available to the para isomer. This is the principal technical reason for selecting 2-nitrobenzyl alcohol in synthetic schemes requiring light-removable protection for prodrugs or linkers. Positional isomerism also changes bulk thermal properties: 2-nitrobenzyl alcohol exhibits a melting range of 69–72°C by USP 〈741〉, 3-nitrobenzyl alcohol melts at 30–32°C, and 4-nitrobenzyl alcohol melts at 92–95°C. The ortho isomer therefore remains crystalline during standard drying and milling, but its melting point is low enough to require vacuum drying below 45°C to avoid sintering. The meta isomer presents poor milling behavior because its melting point is close to ambient temperature and may cause screen blinding in pin mills. Compared with 2-nitrobenzyl chloride, the alcohol model avoids a reactive benzyl halide center and the corresponding ICH M7 mutagenic impurity control burden. 2-Nitrobenzyl chloride may require purge-factor calculations or analytical limits below the threshold of toxicological concern; the alcohol form does not carry the same DNA-reactive impurity classification.
| Derivative | CAS | Melting range | Pharmaceutical-processing difference |
|---|---|---|---|
| 2-Nitrobenzyl alcohol | 612-25-9 | 69–72°C | Photolabile ortho protection; crystalline at milling temperature; no halogenated genotoxic burden |
| 3-Nitrobenzyl alcohol | 619-25-0 | 30–32°C | Low melting range complicates jet milling and dry dispersion |
| 4-Nitrobenzyl alcohol | 619-73-8 | 92–95°C | Higher melting range; lacks the ortho photolability required for selective deprotection |
| 2-Nitrobenzyl chloride | 610-22-0 | See supplier certificate | Reactive halide requires mutagenic impurity control under ICH M7 |
The two models share identity specifications but diverge in particulate, microbial, and water limits. HPLC assay uses a C18 column (250 × 4.6 mm, 5 µm) with UV detection at 254 nm. Particle size is determined by laser diffraction per ISO 13320 using dry dispersion at 1.5 bar. The limits below are representative acceptance criteria applied at release.
| Attribute | ONBA-PH-OSD | ONBA-PH-INJ | Method/Standard |
|---|---|---|---|
| Appearance | White to pale yellow crystalline powder | White to off-white crystalline powder | Visual inspection |
| Assay (HPLC area %) | ≥ 99.0 | ≥ 99.5 | USP 〈621〉 |
| Melting range | 69–72°C | 69–72°C | USP 〈741〉 |
| Water content | ≤ 0.5% | ≤ 0.2% | USP 〈921〉 Method Ia |
| Residue on ignition | ≤ 0.10% | ≤ 0.05% | USP 〈281〉 |
| Total impurities | ≤ 0.5% | ≤ 0.3% | HPLC area normalization |
| Particle size d90 | ≤ 100 µm | ≤ 40 µm | ISO 13320 |
| Bacterial endotoxin | Not specified | ≤ 0.25 EU/mg | USP 〈85〉 |
| Total aerobic microbial count | ≤ 1000 CFU/g | ≤ 10 CFU/g | USP 〈61〉 |
| Residual solvents | Methanol ≤ 3000 ppm; dichloromethane ≤ 600 ppm; dimethylformamide ≤ 880 ppm; ethyl acetate ≤ 5000 ppm | USP 〈467〉 Procedure A | |
Residual solvent control follows ICH Q3C Option 1 limits. If the manufacturing route includes metal-catalyzed hydrogenation, elemental impurity control follows ICH Q3D and USP 〈232〉/〈233〉, with routine analysis for Class 1 elements cadmium, lead, arsenic, and mercury, and Class 2A elements cobalt, nickel, and vanadium where the route includes metal-catalyzed hydrogenation. Published data for the complete elemental profile of this specific intermediate are limited; the control strategy therefore relies on supplier risk assessment and periodic verification rather than mandatory batch testing for every element.
The injectable model ONBA-PH-INJ is not a sterile product, but it is intended to be converted into a parenteral final API without a subsequent purification step that removes endotoxin. Release testing therefore adds bacterial endotoxin, bioburden, sub-visible particle, and water limits that are absent from the oral-grade specification. The endotoxin acceptance of ≤0.25 EU/mg by USP 〈85〉 is derived from the final product endotoxin limit using the formula K/M; if the final injectable dose exceeds 10 mL or if the intermediate is used at higher mass loads, the endotoxin limit must be reduced accordingly. Sub-visible particle testing follows USP 〈788〉 at the final drug product stage, but the solid intermediate is controlled for foreign particulate matter by optical microscopy and particle-size distribution rather than light obscuration, because it is subsequently dissolved and filtered. The water content limit of ≤0.2% by USP 〈921〉 Method Ia reduces hydrolysis risk and limits microbial proliferation. Production drying is carried out in a vacuum shelf dryer at 40°C and ≤0.08 MPa for not less than 4 h after the product bed temperature reaches set point.
The benzylic alcohol group is sensitive to oxidation to 2-nitrobenzaldehyde. In forced-degradation screening under 0.3% hydrogen peroxide at 25°C for 24 h, aldehyde-related impurity increases; the corresponding processing controls therefore exclude strong oxidizers and require inert-gas blanketing where practical. Photodegradation follows a separate pathway: the ortho-nitrobenzyl chromophore absorbs UV-A/B radiation and undergoes intramolecular cleavage, forming 2-nitrosobenzaldehyde. The product is packaged in amber glass or black high-density polyethylene containers with desiccant, and direct light exposure exceeding 200 W·h/m² UV-A and 1.2 million lux·h visible per ICH Q1B should be avoided. If storage relative humidity exceeds 60%, pre-drying is required before weighing and blending because surface moisture can cause agglomeration and reduce flowability. Incompatibilities include strong bases, which can promote benzylic oxidation and condensation, primary amines under acidic conditions, which can react with aldehyde degradation products, and reducing metals with acidic residues that may undesirably reduce the nitro group to the corresponding aniline. Batch-to-batch variance in residual aldehyde content is observed when vacuum drying uses a rotary vacuum dryer with wall temperature exceeding 45°C; localized discoloration can occur at contact points where the powder sinters and sublimation efficiency decreases.
On pilot-scale tablet manufacturing with a rotary press equipped with B-tooling, the oral model is pre-blended with microcrystalline cellulose and croscarmellose sodium in a bin blender at 25 rpm for 15 min. For direct compression, the oral model is milled through a pin mill with 0.5 mm screen to d90 ≤100 µm, and the particle-size distribution is confirmed by ISO 13320 laser diffraction. Capsule filling on a dosator machine requires adequate flow; if the blend Carr index exceeds 25%, the batch is deagglomerated or the mill speed is adjusted. Wet granulation is not applied to the intermediate itself without a compatibility study because exposure to aqueous binder solutions can increase fines and accelerate oxidation. For injectable processing, the intermediate is introduced before final salt formation or lyophilization; the injectable model is therefore controlled for endotoxin and bioburden at the intermediate stage rather than relying on terminal sterilization. Published data for terminal sterilization of ortho-nitrobenzyl alcohol in aqueous solution is limited, and the material should not be autoclaved without route-specific stability verification.