| HS Code | 686272 |
| Product Name | 2-Amino-3,5-dibromobenzaldehyde Pharma Grade API |
| Chemical Name | Benzaldehyde, 2-amino-3,5-dibromo- |
| Synonyms | 3,5-Dibromo-2-aminobenzaldehyde; 2-Amino-3,5-dibromobenzaldehyde |
| Cas Number | 50910-55-9 |
| Molecular Formula | C7H5Br2NO |
| Molecular Weight | 278.93 g/mol |
| Appearance | Yellow to brown crystalline powder |
| Pharmaceutical Grade | Pharma Grade API |
| Purity | ≥98.0% (HPLC) |
| Melting Point | 128-130 °C |
| Boiling Point | 344.5 ± 42.0 °C at 760 mmHg (predicted) |
| Density | 2.0 ± 0.1 g/cm³ (predicted) |
| Solubility | Soluble in DMSO, DMF, dichloromethane; slightly soluble in water |
| Storage Conditions | Store in a cool, dry, well-ventilated area away from light and moisture |
| Stability | Stable under recommended storage conditions; protect from strong oxidizing agents |
| Dosage Forms | Tablet / Capsule / Granule / Injection |
| Routes Of Administration | Oral & Injectable |
| Pharmaceutical Use | API/intermediate for oral and injectable pharmaceutical formulations |
| Shelf Life | 24 months when stored properly |
| Packaging | Sealed pharmaceutical-grade containers |
| Smiles | O=Cc1cc(Br)cc(Br)c1N |
As an accredited 2-Amino-3,5-dibromobenzaldehyde 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 direct-compression tablet manufacture of the dibrominated amino aldehyde, the API is first co-milled with anhydrous dibasic calcium phosphate and microcrystalline cellulose through a 0.5 mm screen in a knife mill to reach a particle size D90 of ≤20 µm. The formulation addition is held to 0.5–6.0 wt% of core tablet mass for low-dose strengths; loadings above 8.0 wt% reduce blend flow and accelerate visual browning when residual moisture exceeds 45% RH. Blending is performed in a 300 L bin blender at 8 rpm for 20 min with sodium stearyl fumarate added at 0.5–1.0 wt% as lubricant; magnesium stearate above 1.5 wt% is avoided because extended lubrication slows dissolution. Compression on a 14-station rotary press with 8.0 mm biconcave tooling at 5–15 kN produces 60–100 N tablet hardness and disintegration below 15 min. Compression suites are controlled at 20–25 °C and 20–25% RH; raised humidity above 60% RH requires pre-drying of excipients at 40–50 °C for 4 h. The process is monitored under USP <905> uniformity of dosage units, USP <711> dissolution, and USP <701> disintegration; equipment qualification follows 21 CFR 211.65 and cleaning validation follows 21 CFR 211.67. Finished products are immediate-release film-coated tablets for oral administration.
Production-scale batch records indicate that direct-compression blends containing this aldehyde develop decreased yield pressure at turret speeds above 40 rpm, so press speed is limited to 25–35 rpm; copper-free tooling is specified to avoid metal-catalyzed aldehyde oxidation. In-process sampling every 15 min for hardness, thickness, and disintegration provides attribute data under 21 CFR 211.110. At ambient RH above 35%, the blend is transferred in sealed bins purged with nitrogen to prevent hydrate formation on the aldehyde group and subsequent punch sticking.
For capsule filling, the free aldehyde reacts with amino groups in gelatin, so hypromellose capsule shells are specified instead of gelatin. The API is pre-blended at 1.0–8.0 wt% of filled mass with mannitol and crospovidone before roller compaction. Ribbon density is controlled by a roll gap of 2.0–3.5 mm and hydraulic pressure of 45–80 bar; milled granules are passed through a 1.0 mm screen and filled into hypromellose shells at 20–25 °C and 20–25% RH. Dosator filling equipment is preferred over tamping machines to reduce particle shearing and aldehyde liberation from granule surfaces. Filled capsules are sampled under USP <905> for weight variation and USP <711> for dissolution; microbial controls follow 21 CFR 211.67. Terminal products are hypromellose hard capsules for oral administration. When ribbon solid fraction exceeds 0.70, granules become brittle and produce excessive fines below 150 µm, which increases weight variation during high-speed filling.
Recompaction of oversized granules above 1.0 mm is stopped after one pass because repeated compaction work-hardens the brittle fraction and lowers capsule disintegration. Cleaning validation for contact surfaces includes swab sampling for free aldehyde after each product changeover to prevent cross-contamination with amine-containing APIs.
Non-aqueous high-shear granulation is specified for sachet granules because the free aldehyde reacts with water-miscible amine-functional binders, forming Schiff base adducts. The API is dispersed at 2.0–7.5 wt% of dry granule mass in anhydrous lactose-free filler and granulated with 96% ethanol in a 600 L high-shear granulator at impeller speed 120 rpm and chopper speed 1500 rpm. Binder solution is sprayed at 0.5–1.5 kg/min; moist granules are screened through 1.5 mm, dried under vacuum at 40–50 °C to residual ethanol below 0.5%, and filled into aluminum foil sachets at 20–25% RH. Dissolution is tested by USP <711>, weight variation by USP <905>, and residual ethanol by ICH Q3C Option 1; batch process controls follow 21 CFR 211.100. Terminal products are single-dose oral granules for reconstitution or direct administration.
Granule batches show higher aldehyde recovery when the binder is hydroxypropyl cellulose dissolved in ethanol rather than povidone in water; the water-free system prevents aldehyde hydration and reduces impurity formation by 0.3–0.6% area under accelerated storage at 40 °C/75% RH in aluminum-foil overwrap. Published data for this specific configuration is limited; therefore, pre-validation stability studies at 25 °C/60% RH and 40 °C/75% RH are required before commercial scale-up.
Injectable processing uses a bulk solution concentration of 0.05–1.0 wt% in water for injection with 10–30% v/v dehydrated ethanol or propylene glycol as solubilizer. The solution pH is adjusted to 4.0–5.5 with acetate buffer; tromethamine and glycine buffers are incompatible because their primary amino groups condense with the aldehyde. After dissolution, the solution is overlaid with nitrogen to keep dissolved oxygen below 0.5 mg/L, filtered through a 0.22 µm PVDF membrane, and filled into borosilicate glass vials under ISO 14644-1:2015 Class 5 conditions. Lyophilization uses shelf cooling to −35 °C, primary drying at −20 °C for 18–24 h, and secondary drying at 25 °C for 6–8 h; chamber pressure is maintained at 80–120 mTorr. Release testing includes USP <1>, USP <71> sterility, USP <85> bacterial endotoxins, and USP <788> particulate matter; special testing is governed by 21 CFR 211.167. The terminal product is lyophilized powder for injection requiring reconstitution with sterile diluent.
Published data for this specific configuration is limited above 1.0 wt% because cosolvent precipitation occurs during freeze-concentration; addition ratios above this boundary require pre-formulation solubility screening and thermal cycling studies. Aseptic holding times are limited to 8 h at 5 ± 3 °C to minimize hydrolytic cleavage of the bromo substituents and aldehyde oxidation in buffered solution.
For oral solid dose stability, the compressed core is coated with an opaque aqueous dispersion containing polyvinyl alcohol and titanium dioxide. Coating solids are applied to a weight gain of 2.0–3.5% of the tablet core mass, with titanium dioxide at 8–15% of coating solids to reduce photolytic degradation under ICH Q1B conditions. Pan coating is performed in a 48-inch perforated pan at inlet air temperature 50–60 °C and pan speed 4–8 rpm; atomizing air pressure is 1.5–2.0 bar. Photostability is assessed under ICH Q1B exposure and long-term stability under ICH Q1A(R2); coated tablets continue to meet USP <905> and USP <711> after light exposure. The terminal product is a photoprotected film-coated immediate-release tablet. Coating dispersion solids are held at 15–20% to prevent overwetting of the aldehyde-containing core during the first 30 min of spray application.
| Dosage form | API addition ratio | Critical process parameter | Compliance standards | Terminal finished product type |
|---|---|---|---|---|
| Direct-compression tablet | 0.5–6.0 wt% of core mass | 5–15 kN compression force, 20–25% RH | USP <905>, USP <711>, USP <701>, 21 CFR 211.65 | Immediate-release film-coated tablet |
| Roller-compacted hypromellose capsule | 1.0–8.0 wt% of filled mass | 2.0–3.5 mm roll gap, 45–80 bar pressure | USP <905>, USP <711>, 21 CFR 211.67 | Hypromellose hard capsule |
| Non-aqueous granule sachet | 2.0–7.5 wt% of dry granule mass | Ethanol spray 0.5–1.5 kg/min, vacuum drying 40–50 °C | USP <905>, USP <711>, ICH Q3C Option 1, 21 CFR 211.100 | Single-dose oral granules in aluminum foil sachets |
| Aseptic lyophilized injection | 0.05–1.0 wt% of bulk solution | pH 4.0–5.5, 0.22 µm PVDF filtration, primary drying −20 °C | USP <1>, USP <71>, USP <85>, USP <788>, 21 CFR 211.167 | Lyophilized powder for injection |
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2-Amino-3,5-dibromobenzaldehyde is supplied as a pharmaceutical-grade active pharmaceutical ingredient under the manufacturer-specific model code ALD-2A35DBB-PG. The molecular formula is C7H5Br2NO; the molecular weight is 278.93 g/mol; the CAS registry number is 50910-55-9. The molecule carries a primary aromatic amino group at position 2, a benzaldehyde carbonyl at position 1, and bromine substituents at positions 3 and 5. This substitution pattern gives a higher molecular weight, stronger lipophilicity, and greater ring deactivation than the mono-brominated and non-halogenated amino benzaldehydes. Two grades are available: a solid oral grade for tablet, capsule, and granule processing and an injectable grade with reduced endotoxin burden, microbial load, and sub-visible particulate matter. Both grades require the same chemical purity but differ in route-specific release tests.
The powder is reported to melt at 138–142 °C; because no monograph for this substituted benzaldehyde appears in USP, Ph. Eur., or JP, the release specification is based on the ICH Q6A decision tree for new drug substances and the batch certificate remains the governing document. The solid oral grade is typically milled to a D90 of ≤ 75 µm for direct compression and dry blending. The injectable grade is controlled to a finer particle distribution and to the bacterial endotoxin limit calculated from the maximum parenteral dose.
The main processing constraint is the reactivity of the aldehyde carbonyl with primary amino groups, including those present on the molecule itself and on excipients. The intramolecular amino-aldehyde arrangement can generate chromophoric Schiff-base species if the material is stored above 40 °C or in the presence of strong acid. In wet granulation with water, the aldehyde can be partially hydrated to a geminal diol, which can appear as an early-eluting HPLC peak and reduce the assay. Aqueous granulation is therefore carried out at pH below 6 and with a drying endpoint not exceeding 2.0% loss on drying. Isothermal microcalorimetry and differential scanning calorimetry at 10 K/min under nitrogen are used to detect incompatible excipient transitions before stability batches are placed. The product should not be combined with ammonia-neutralized disintegrants, tromethamine, or primary amine binders because these excipients can form Schiff-base adducts.
For tablet and capsule intermediates, the powder is first passed through a 500 µm cone mill or oscillating granulator. The milled lot is blended in a bin blender at 60–70% vessel fill for 20–30 minutes with a ductile filler such as microcrystalline cellulose and a disintegrant such as crospovidone. Because brominated crystals can show high elastic recovery, tablets produced without a binder may exhibit edge chipping and low tensile strength. An instrumented rotary press with precompression is used to derive the Heckel yield pressure; the compression profile is then locked to maintain tablet hardness within 4–8 kp for immediate-release tablets and disintegration per USP <701> within 15 minutes in 0.1 M HCl. Capsule filling uses a tamping or dosator setting adjusted to tapped density, and blend uniformity is monitored by near-infrared spectroscopy and by assay using USP <621>.
Jet milling of the unmicronized product at 0.7–1.2 MPa grinding air pressure reduces the D90 from approximately 150–250 µm to 20–75 µm. The milled powder acquires electrostatic charge and requires handling below 40% RH to prevent agglomeration. If material is exposed to RH > 60%, pre-drying in a vacuum oven at 40–45 °C for 12–24 hours is required before dispensing. These processing parameters are development screening values and are not release limits; published data for this specific configuration in high-volume production is limited.
Injectable formulations require route-specific release testing beyond solid oral controls. Because the product contains an aldehyde group, the formulation should avoid bisulfite and sulfite antioxidants, which form aldehyde-bisulfite addition products and can deplete the active form. Primary amino buffers such as tromethamine should be excluded for the same reason. Solubility in water is limited; parenteral development typically uses a co-solvent system or pH adjustment below the pKa of the aromatic amino group to increase ionization and dissolution. The pH of the prepared solution is selected from forced degradation data generated under ICH Q1A/R2 and photostability data generated under ICH Q1B, because brominated aromatic compounds can undergo light-induced dehalogenation.
The injectable grade is controlled for bacterial endotoxins per USP <85>; the limit is derived from the maximum intended parenteral dose. As an example calculation, a 1000 mg/day intravenous dose at a 5 EU/kg threshold for a 70 kg adult gives a product endotoxin limit of 0.35 EU/mg. Sub-visible particulate matter is controlled per USP <788> for small-volume injections after reconstitution. Bioburden is measured according to USP <61> and USP <62>. If terminal sterilization cannot be used because of aldehyde-related lability, aseptic filtration through a 0.22 µm filter is required; filter compatibility studies should be executed with the formulated solution rather than the dry API because dimethylacetamide or dimethyl sulfoxide wetting can extract filter components that are not observed in dry product.
Table 1 lists representative release controls for the two grades. These are model acceptance criteria for early-phase development; commercial limits are set from process validation and stability data.
| Release Attribute | Solid Oral Grade | Injectable Grade | Test Method |
|---|---|---|---|
| Appearance | Pale yellow to light amber powder | Pale yellow to light amber powder | Visual and spectrophotometric identification |
| Identification | IR spectrum matches reference; HPLC retention time | IR spectrum matches reference; HPLC retention time | USP <197>, USP <621> |
| Assay, anhydrous and solvent-free | 98.0–102.0% | 98.0–102.0% | HPLC, USP <621> |
| Total related substances | ≤ 1.0% | ≤ 0.8% | HPLC, USP <621> |
| Melting range | 138–142 °C | 138–142 °C | USP <741> |
| Loss on drying | ≤ 0.5% | ≤ 0.5% | USP <731> |
| Residue on ignition | ≤ 0.1% | ≤ 0.1% | USP <281> |
| Elemental impurities | ICH Q3D oral PDE limits | ICH Q3D parenteral PDE limits | USP <232> and USP <233> |
| Residual solvents | Class 2 and Class 3 limits | Class 2 and Class 3 limits | USP <467> |
| Particle size D90 | ≤ 75 µm | ≤ 50 µm or as qualified | Laser diffraction, ISO 13320 |
| Bacterial endotoxins | Not specified | Dose-based limit; example 0.35 EU/mg | USP <85> |
| Particulate matter | Not specified | Meets SVP limits after reconstitution | USP <788> |
Downstream filling of oral granules into sachets or capsules is performed under 25–35% RH. Granules are sized through a 1.0 mm screen and mixed with extragranular disintegrant before encapsulation. If sachet filling is used, seal integrity is tested according to ASTM F88 or an equivalent method. The aldehyde-containing granule can react with oxygen, and packaging with a desiccant and an oxygen scavenger is appropriate if long-term stability data show oxidative degradation.
Direct compression is preferred over wet granulation only when the incoming lot has a D90 below 75 µm and loss on drying below 0.5%. Batch-to-batch particle size variability from recrystallization can shift the angle of repose from 35° to 50° and alter die filling. When direct compression is not feasible, roller compaction is used: the API is densified with microcrystalline cellulose and crospovidone, then milled to granules. Roll pressure of 4–8 MPa and roll gap 1.0–2.5 mm are typical screening ranges; compacts with high elastic recovery may produce weak ribbons if roll speed is too high. Dry granulation avoids the aldehyde hydration risk of aqueous wet granulation and is therefore the preferred route for stabilizing labile formulations.
For fluid-bed granulation, a binder solution containing hydroxypropyl cellulose in ethanol/water 85:15 v/v can reduce aldehyde hydration. Screening parameters include inlet air temperature 50–60 °C, product temperature 30–35 °C, spray rate 5–10 g/min, and final moisture ≤ 1.5%. These values are not release limits and must be correlated with content uniformity, related substances, and dissolution data.
Compared with 2-amino-5-bromobenzaldehyde and 2-aminobenzaldehyde, the 3,5-dibromo substitution raises molecular weight to 278.93 g/mol and increases calculated lipophilicity. The second bromine at position 3 further reduces ring electron density and alters the reactivity of the aldehyde toward nucleophiles; published rate constants for this exact derivative are limited. Table 2 summarizes the structural and formulation-relevant differences.
| Property | 2-Amino-3,5-dibromobenzaldehyde | 2-Amino-5-bromobenzaldehyde | 2-Aminobenzaldehyde |
|---|---|---|---|
| Molecular formula | C7H5Br2NO | C7H6BrNO | C7H7NO |
| Molecular weight | 278.93 g/mol | 200.03 g/mol | 121.14 g/mol |
| Halogen effect on ring electron density | Strong deactivation by two bromine atoms | Moderate deactivation | No halogen |
| Calculated lipophilicity | Highest | Intermediate | Lowest |
| Aldehyde hydration sensitivity | Electronic withdrawal may promote hydration; measured rate data limited | Lower than dibromo derivative | Reference |
| Anomalous X-ray scattering | Strong from two bromine atoms | Moderate from one bromine atom | Absent |
The dibromo derivative is not interchangeable with mono-brominated or non-halogenated amino benzaldehydes in a validated formulation. Its higher lipophilicity may reduce dissolution in pH 6.8 phosphate buffer; if dissolution failure is observed, a surfactant such as sodium lauryl sulfate at 0.1–0.5% w/v can be evaluated, provided aldehyde-surfactant adducts are not detected by HPLC. Storage in amber glass under nitrogen at 15–25 °C is recommended, with desiccant for solid oral grade and endotoxin-free containers for injectable grade. Avoid direct sunlight and open handling above 60% RH.