| HS Code | 740108 |
| Productname | 4-Isothiocyanato-2-(trifluoromethyl)benzonitrile Pharma Grade API |
| Chemicalname | 4-Isothiocyanato-2-(trifluoromethyl)benzonitrile |
| Casnumber | 143782-23-4 |
| Molecularformula | C9H3F3N2S |
| Molecularweight | 228.19 g/mol |
| Appearance | White to off-white crystalline powder |
| Assaypurity | ≥99.0% (HPLC) |
| Grade | Pharma Grade |
| Dosageforms | Tablet, Capsule, Granule, Injection |
| Routesofadministration | Oral, Injectable |
| Storageconditions | Store in a cool, dry, well-ventilated area; protect from moisture, heat, and light |
| Solubility | Soluble in organic solvents such as DMSO, DMF, methanol, dichloromethane; practically insoluble in water |
| Chemicalclass | Isothiocyanate/benzonitrile derivative |
| Shelflife | 24 months when stored properly |
As an accredited 4-isothiocyanato-2-(trifluoromethyl)benzonitrile 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 | Supplied in 1 kg amber glass bottles, securely sealed, tamper-evident, labeled, suitable for tablet, capsule, granule, oral, and injectable API. |
| Container Loading (20′ FCL) | 20′ FCL loaded with 4-isothiocyanato-2-(trifluoromethyl)benzonitrile Pharma Grade API for tablets, capsules, granules, oral and injectable formulations, securely packed for export. |
| Shipping | 4-Isothiocyanato-2-(trifluoromethyl)benzonitrile, Pharma Grade API (tablet/capsule/granule/injection; oral and injectable), ships as a regulated hazardous material via IATA/IMDG/ADR in sealed, moisture-barrier, light-resistant UN packaging. Temperature-controlled per stability, with desiccants, toxic/irritant labels, MSDS, CoA, and chain-of-custody documentation. Handle under inert atmosphere if required; maintain cold chain where specified; comply with carrier and destination regulations. |
| Storage | Store pharma-grade material in a tightly closed, light-resistant container under inert gas (nitrogen or argon) at 2–8°C. Protect from moisture, heat, light, and ignition sources. Keep away from oxidizers, acids, bases, amines, and water. Maintain segregated, secure, GMP-compliant storage with batch traceability. For oral and injectable APIs, use clean, dedicated, well-ventilated areas; ensure container integrity. Do not freeze unless validated. |
| Shelf Life | Store unopened in tightly sealed containers, protected from light, moisture, and heat; typical shelf life is 24–36 months under recommended conditions. |
In direct compression, the primary process conflict is not the compressibility of the API but the chemical incompatibility between the terminal isothiocyanate group and any amine-functional excipient. The API is blended with lactose monohydrate, microcrystalline cellulose, colloidal silicon dioxide, and sodium stearyl fumarate to produce an amine-free dry blend. Because the trifluoromethyl substituent lowers aqueous solubility, particle size reduction to a 20 µm D90 or below is evaluated when the target dose is 1 mg to 10 mg; this is achieved with a fluid-jet mill using nitrogen at 6 bar and classifier speed 3000 RPM. Pre-blending is performed in a 300 L bin blender at 12 RPM for 15 minutes, using geometric dilution of the API with microcrystalline cellulose before final blending. Lubrication time is kept below 5 minutes to avoid over-lubrication, which can reduce tablet tensile strength. Compression on a 27-station rotary press with 8 mm standard concave round tooling typically requires target hardness of 4 kp to 8 kp; weight variation is monitored according to USP <905> and tablet breaking force according to USP <1217>. The terminal finished product is a film-coated immediate-release tablet; the hydroxypropyl methylcellulose-based coating dispersion is selected because it lacks free primary or secondary amine groups. The process must comply with 21 CFR 211.110 in-process sampling and ICH Q3D elemental impurity control. Published data for the direct-compression performance of this specific API is limited; therefore, powder rheometry and compaction simulation are required before scale-up.
Low-dose encapsulation of a nitrile-bearing isothiocyanate requires the capsule shell material to be selected before the excipient system is finalised. Gelatin capsules are excluded because the lysine and arginine side chains in gelatin can react with the isothiocyanate group to form thiourea adducts, leading to crosslinking, brittleness, and dissolution failure. Hydroxypropyl methylcellulose capsules are used instead, with crospovidone or sodium starch glycolate as disintegrant and mannitol as filler. For a 1 mg or 2 mg dose, the API is first triturated with mannitol at a 1:9 ratio and then passed through a 250 µm screen. The pre-blend is introduced into a 200 L tote blender, followed by glidant addition at 0.5% w/w colloidal silicon dioxide and lubricant addition at 1.0% w/w sodium stearyl fumarate. Encapsulation on a tamping-pin capsule filler at 30,000 capsules/hour is monitored for weight variation every 15 minutes, with content uniformity acceptance per USP <905>. The terminal finished product is a size 3 hydroxypropyl methylcellulose capsule with a desiccant insert in 60 mL high-density polyethylene bottles; stability storage at 25 °C and 60% RH should be paired with dissolution testing according to USP <711>. The process boundary is that the capsule fill mass must be kept below 220 mg to maintain shell integrity under low-humidity conditions.
When the granulation process is transferred to a high-shear mixer, water cannot be used as the binder solvent because the isothiocyanate group undergoes hydrolysis to the corresponding amine, generating a degradation product that can exceed 0.10% under ICH Q3B qualification thresholds. An anhydrous binder solution is therefore prepared with ethylcellulose dispersed in ethanol or a dichloromethane-ethanol blend, subject to ICH Q3C residual solvent limits. In a 65 L high-shear granulator, the dry powders—lactose anhydrous, microcrystalline cellulose, and sodium starch glycolate—are mixed at impeller speed 150 RPM for 3 minutes, then the binder solution is added at 2.0% w/w to 4.0% w/w solids over 90 seconds. The wet mass is discharged when the granule endpoint reaches a target median diameter of 500 µm; drying is performed in a fluid-bed dryer at inlet air temperature 35 °C to 45 °C until loss on drying is below 1.5% w/w. Milling through a 1.25 mm screen eliminates oversized agglomerates. The terminal product is a granule-filled sachet or a tablet intermediate; for granule-filled sachets, the fill weight is controlled at 1.0 g to 2.0 g and the moisture-barrier laminate is selected for water vapour transmission below 0.5 g/m²/day. The critical process boundary is that residual dichloromethane must be below 6.0 mg/day according to ICH Q3C; this requires periodic gas chromatography headspace analysis of the granules.
At a bulk density below 0.35 g/cm³, the API cannot be directly compressed into a robust tablet, and if both moisture and organic solvents are excluded, dry granulation via roller compaction becomes the process route. The API is blended with lactose anhydrous, microcrystalline cellulose, and crospovidone in a 600 L bin blender for 20 minutes at 10 RPM, then lubricated with 0.75% w/w sodium stearyl fumarate for 3 minutes. The roller compactor is configured with smooth rolls of 250 mm diameter and 100 mm width; roll pressure is maintained at 4 MPa to 12 MPa and roll speed at 3 RPM to 8 RPM. Ribbons with density 1.05 g/cm³ to 1.25 g/cm³ are milled through a 0.8 mm sieve to produce granules with D50 of 250 µm to 500 µm. The granules are then compressed on a rotary tablet press with 10 mm round tooling at a target weight of 250 mg and hardness of 5 kp to 10 kp. Content uniformity is verified per USP <905>, and friability is controlled below 1.0% using USP <1216>. Published data for the specific interaction between this API and roller-compacted granules is limited; therefore, ribbon solid fraction and granule particle size distribution must be correlated with tablet dissolution before commercial batch release.
Terminal sterilisation is excluded from the injectable process because the isothiocyanate group begins to degrade under heat; therefore, the entire sterile operation shifts to aseptic filtration. For injectable dosage forms, the poorly water-soluble character of the trifluoromethylated API requires a non-aqueous or co-solvent vehicle. A typical parenteral development formulation may combine PEG 300 and propylene glycol in a 60:40 ratio, with polysorbate 20 at 0.1% w/w to reduce interfacial tension. The vehicle is pre-sterilised by membrane filtration through a 0.22 µm polyvinylidene fluoride filter; the API is introduced as a sterile powder under Grade A conditions, or the entire solution is passed through two 0.22 µm filters in series per EU GMP Annex 1. Because isothiocyanate degradation may occur at elevated temperature, terminal sterilisation is not assumed to be compatible; aseptic processing is used, and the filtration train must be validated for bacterial retention with Brevundimonas diminuta at not less than 107 CFU/cm². The solution is filled into 5 mL Type I borosilicate glass vials under Grade A laminar airflow, with 13 mm chlorobutyl stoppers. Particulate matter is controlled by USP <788> light obscuration testing; the product must also meet sterility per USP <71> and bacterial endotoxins per USP <85>. The terminal product is an injectable solution for slow intravenous administration, with an amber vial to limit photolytic degradation. The process boundary is that the vehicle must contain less than 0.5% w/w water to minimise isothiocyanate hydrolysis during shelf life.
| Quality Attribute | Compendial / Regulatory Reference | Application to Injectable Dosage Form |
|---|---|---|
| Sterility | USP <71>, 21 CFR 211.167 | Membrane filtration sterility test after not less than 14 days incubation |
| Bacterial endotoxins | USP <85> | LAL kinetic chromogenic assay; product-specific limit |
| Particulate matter | USP <788> | Light obscuration particle count at 10 µm and 25 µm |
| Visible particulates | USP <790> | 100% inspection under specified light intensity |
| Residual solvents | ICH Q3C | Dichloromethane Class 2 limit where applicable |
| Elemental impurities | ICH Q3D | Risk assessment for Class 1 and Class 2A metals |
During lyophilisation of this API, cryoprotectant selection is driven by the nucleophilic character of the isothiocyanate group. Mannitol and trehalose are preferred because they lack amine and thiol functionalities; glycine, arginine, and histidine are excluded because they can form thiourea adducts during lyophilisation. The pre-lyophilisation solution is prepared at 5 mg/mL API in a tert-butyl alcohol-water cosolvent system, with mannitol at 4% w/w as bulking agent. The solution is filled into 10 mL Type I borosilicate vials at 3.0 mL fill volume, then partially stoppered and loaded onto lyophiliser shelves at −45 °C. Primary drying is conducted at shelf temperature −25 °C and chamber pressure 0.2 mbar for 24 hours to 48 hours; secondary drying at +25 °C for 6 hours to 12 hours is required to reach residual moisture below 1.0% w/w by Karl Fischer titration. The freeze-dried cake is stoppered under vacuum with 13 mm fluoropolymer-coated chlorobutyl closures. Reconstitution with 0.9% w/v sodium chloride injection requires not more than 2 minutes to produce a solution free of visible particles under USP <790>. Stability of the lyophilised product is assessed at 5 °C and 25 °C / 60% RH, with assay and related substances monitored by HPLC per ICH Q3B. Published data for the lyophilisation of this specific isothiocyanate-containing API is limited; therefore, collapse temperature should be measured by freeze-drying microscopy rather than assumed from the amorphous component alone.
Competitive 4-isothiocyanato-2-(trifluoromethyl)benzonitrile 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 +8618963613625 or mail to sales10@sinochem-nanjing.com.
We will respond to you as soon as possible.
Tel: +8618963613625
Email: sales10@sinochem-nanjing.com
Flexible payment, competitive price, premium service - Inquire now!
4-isothiocyanato-2-(trifluoromethyl)benzonitrile is supplied as a pharma-grade active pharmaceutical ingredient intended for tablet, capsule, granule, and injectable product manufacture. The molecular formula is C9H4F3N2S and the molar mass is 229.20 g·mol⁻¹. The compound consists of a benzonitrile nucleus substituted at the 2-position with a trifluoromethyl group and at the 4-position with an isothiocyanato group. This substitution pattern is distinct from mono-substituted aryl isothiocyanates because two strongly electron-withdrawing groups are present on the aromatic ring. The nitrile and trifluoromethyl groups increase the electrophilic character of the isothiocyanato carbon and reduce aqueous solubility relative to the non-fluorinated 4-isothiocyanatobenzonitrile analog. The product is manufactured as the neutral crystalline solid, not as a salt or hydrate.
The dosage-form-specific grade designation, Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable, identifies a GMP-compliant material released for formulation into oral solid dosage forms and sterile injectable preparations. It is not a technical-grade reactive intermediate. Because no United States Pharmacopeia, European Pharmacopoeia, or Japanese Pharmacopoeia monograph is published for this compound, release is controlled against an in-house monograph qualified according to ICH Q6A. Supplier product codes commonly distinguish the standard oral grade, micronized oral grade, and sterile injectable grade. The micronized oral grade is controlled for particle size by laser diffraction according to ISO 13320-1:2020, while the sterile injectable grade is released with bacterial endotoxin and bioburden data suitable for aseptic processing.
Compared with the non-fluorinated 4-isothiocyanatobenzonitrile analog, the 2-trifluoromethyl substituent produces higher reversed-phase chromatographic retention and lower aqueous solubility. Compared with aliphatic isothiocyanates such as sulforaphane, the aromatic benzonitrile structure is more rigid and less volatile. These differences affect dissolution, permeability, and handling but do not establish safety or efficacy without product-specific data.
The release specification for a non-compendial aryl isothiocyanate of this type is typically built from a combination of chromatographic purity, residual solvent, elemental impurity, water, and particle size controls. The exact acceptance limits are supplier-specific and must be verified against the current certificate of analysis. A representative testing matrix is shown below.
| Test | Method or standard | Typical pharma-grade acceptance |
|---|---|---|
| Appearance | Visual inspection | White to off-white crystalline powder |
| Identification | FTIR, HPLC retention time | Conforms to reference standard |
| Assay by HPLC | USP <621> | 98.0–102.0% on dried basis |
| Related substances | In-house HPLC, ICH Q3A | Total impurities ≤1.0%; unspecified individual ≤0.10% |
| Water | USP <921> | ≤0.5% |
| Loss on drying | USP <731> | ≤0.5% |
| Residue on ignition | USP <281> | ≤0.1% |
| Residual solvents | USP <467> | ICH Q3C Option 1 limits |
| Elemental impurities | USP <232>/<233> | ICH Q3D class limits |
| Endotoxin, injectable grade | USP <85> | ≤0.10 EU·mg⁻¹ or justified by dose |
| Particulate matter, injectable finished product | USP <788> | Meets small-volume injectable limits |
| Sterility, injectable finished product | USP <71> | No growth |
| Particle size distribution | ISO 13320-1:2020 | D90 limit as per order or monograph |
The assay and impurity methods are validated for specificity, linearity, accuracy, and precision according to ICH Q2(R1). The impurity method should resolve positional isomers, including the 3-isothiocyanato and 4-trifluoromethyl variants, because these isomers can have different toxicological profiles. For injectable-grade material, the endotoxin limit is derived from the maximum total daily dose and is not a fixed universal value.
Tablet, capsule, and granule manufacture begins with dry handling under controlled humidity. The isothiocyanate group is hydrolytically sensitive and can form the corresponding amine and carbonyl sulfide in the presence of water. Aqueous wet granulation is therefore avoided unless a non-aqueous binder system is justified. Direct compression and dry granulation are the preferred processing routes. Excipient compatibility is evaluated in binary mixtures stored for 4 weeks at 40°C/75% RH and 25°C/60% RH according to ICH Q1A(R2). A loss of assay greater than 5% or formation of a new unspecified impurity above 0.10% is treated as a compatibility failure. Excipients containing primary or secondary amines, thiols, or strongly alkaline surfaces should be avoided because they can accelerate isothiocyanate degradation or form thiourea adducts. Anhydrous lactose, microcrystalline cellulose, and dibasic calcium phosphate dihydrate are typical starting diluents. Colloidal silicon dioxide and sodium stearyl fumarate may be used as flow and lubrication aids.
Powder flow is characterized by angle of repose, bulk density, tapped density, and compressibility index according to USP <616>. A compressibility index above 25% generally indicates the need for dry granulation or a glidant. The API is screened through a 500 µm or finer sieve before blending to break agglomerates. Blending may be performed in a V-blender or bin blender at 10–25 rpm for 15–30 min as a starting range, with blend uniformity confirmed by USP <905>. Dry granulation is conducted on a roller compactor with monitored roll force, roll speed, and gap. Overcompaction can reduce tabletability, while undercompaction produces weak granules. Granulated material is milled and compressed on a rotary tablet press with pre-compression. Tablet breaking force is measured by USP <1217>. Dissolution testing is performed according to USP <711>; media containing 0.1–1.0% sodium lauryl sulfate may be required to achieve sink conditions, but the surfactant concentration is justified by solubility data.
Capsule filling on dosator or tamping-pin equipment is controlled by powder bed height, pin settings, and fill weight. Granules for capsule filling are controlled for particle size distribution by sieving, and oversized granules are recycled through a mill. Aqueous film coating of tablets is possible only with short exposure time and low inlet temperature; organic solvent-based coatings are preferred for moisture-sensitive isothiocyanates. Primary packaging for oral solid dosage forms should provide a low water vapor transmission rate, such as aluminum foil blister or HDPE bottles with desiccant.
Injectable manufacturing requires a separate control strategy because the compound has limited aqueous solubility and is hydrolytically sensitive. Ready-to-use aqueous solutions are not typical unless the formulation intent is a reactive intermediate or the isothiocyanate is stabilized in a co-solvent system. Lyophilized powder in glass vials under nitrogen or vacuum is the preferred format. The fill solution is prepared in a co-solvent system such as tert-butyl alcohol, ethanol, or dimethyl sulfoxide diluted with Water for Injection. The exact composition is determined by solubility and lyophilization behavior, not by a fixed formula.
Aseptic filtration is performed through a 0.22 µm PVDF or PTFE membrane filter. The filter is integrity-tested before and after use by bubble point or diffusive flow. Compatibility is evaluated by measuring assay and impurity profile after static contact at the target concentration for up to 24 hours at manufacturing temperature. A loss of assay greater than 5% or a new impurity above 0.10% disqualifies the filter. The filling operation is conducted in an ISO 5 environment according to ISO 14644-1:2015, with viable and non-viable monitoring. Manufacturing is governed by 21 CFR 210 and 21 CFR 211.
Lyophilization cycle development uses freeze-drying microscopy or differential scanning calorimetry to determine the collapse temperature of the formulation. The primary drying shelf temperature is set below the collapse temperature, and chamber pressure is controlled to balance heat transfer and sublimation. The dried cake is stoppered under reduced pressure or nitrogen and tested for moisture by Karl Fischer, sterility by USP <71>, bacterial endotoxins by USP <85>, particulate matter by USP <788>, and container closure integrity by USP <1207>. Residual solvent content is tested by USP <467> and must meet ICH Q3C limits.
The injectable-grade API is handled under nitrogen in an isolator or laminar flow. The dispensing suite is controlled to low humidity, with residual oxygen below 5% and dew point below -40°C for critical handling steps. The material should not be held in aqueous media at neutral to alkaline pH for prolonged periods because the isothiocyanate group hydrolyzes under these conditions. If an injectable emulsion or liposome is considered, the formulation scientist should evaluate possible covalent reaction with phospholipid headgroups containing free amino groups.
Relative to 4-isothiocyanatobenzonitrile, the 2-trifluoromethyl derivative has higher lipophilicity and lower aqueous solubility. The electron-withdrawing trifluoromethyl group increases the reactivity of the isothiocyanate carbon toward nucleophiles, which has direct implications for aqueous stability and covalent adduct formation. The nitrile and isothiocyanate groups give characteristic infrared bands near 2230 cm⁻¹ and 2050–2150 cm⁻¹, respectively, and these features are used to distinguish the product from structural isomers. Chromatographic purity methods must separate the 2,4-substituted compound from its positional isomers because substitution at the 3- or 5-position can alter reactivity and impurity toxicity.
Pharma-grade material differs from technical-grade aryl isothiocyanate by the absence of unidentified process-related impurities above ICH Q3A thresholds. The synthesis may introduce hydrolyzed amine, symmetric thiourea dimers, residual starting material, and residual thiophosgene-related species. A risk assessment under ICH M7 is required for potential mutagenic impurities, and the batch release documentation should include the specific control strategy. Bulk storage at 2–8°C under nitrogen in double polyethylene bags inside aluminum foil laminate minimizes water uptake. The retest period is assigned from ICH Q1A stability data. If the material is exposed to ambient humidity above 40% RH for more than 2 hours during dispensing, requalification for water and related substances is recommended because the NCS group hydrolyzes.
Published data for this specific derivative’s aqueous degradation kinetics and oral bioavailability are limited. Preformulation studies are therefore required before defining a control strategy for a given dosage form. The absence of a public monograph means that the in-house release specification should be reviewed against the proposed dose, route, and manufacturing process rather than adopted from a supplier template.