|
HS Code |
942788 |
| Chemical Formula | C11H11N3S |
| Molecular Weight | 217.29 g/mol |
| Appearance | Solid (usually white or off - white powder) |
| Melting Point | Typically in a certain temperature range (exact value may vary) |
| Boiling Point | May decompose before boiling, no well - defined boiling point under normal conditions |
| Solubility | Slightly soluble in water, more soluble in organic solvents like ethanol, dichloromethane |
| Density | A specific value based on experimental determination |
| Stability | Stable under normal conditions, may react with strong oxidizing agents |
| Odor | Odorless or with a very faint, characteristic odor |
| Pka Value | Value related to its acidic or basic nature in solution |
As an accredited 3-Piperazin-1-Yl-1,2-Benzisothiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 1 - kg containers: 3 - Piperazin - 1 - yl - 1,2 - benzisothiazole. |
| Shipping | 3 - Piperazin - 1 - yl - 1,2 - benzisothiazole is shipped in accordance with strict chemical transport regulations. Packaged securely in appropriate containers, it's transported by carriers trained in handling such chemicals, ensuring safe delivery. |
| Storage | Store 3 - Piperazin - 1 - yl - 1,2 - benzisothiazole in a cool, dry place away from heat sources and direct sunlight. Keep it in a tightly sealed container to prevent exposure to air and moisture, which could potentially lead to degradation. Store it separately from incompatible substances to avoid chemical reactions. |
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In the commercial manufacturing sequence for lurasidone hydrochloride monohydrate, the stoichiometric incorporation of 3-piperazin-1-yl-1,2-benzisothiazole (3-PPBT, CAS 87691-88-1) with a proprietary chiral mesylate intermediate constitutes the convergence point of two distinct building-block synthesis pathways. The alkylation is conducted in a 2000 L glass-lined reactor equipped with a retreat-curve impeller and a Hastelloy C-276 temperature sensor, charged first with anhydrous acetonitrile (1200 kg) and the mesylate ester (1.05 molar equivalents relative to 3-PPBT). 3-PPBT is introduced as a single solid portion, followed by slow addition of finely ground potassium carbonate (2.5 eq, particle size D50 < 50 µm) to avoid localized alkaline hotspots that accelerate the formation of a dimeric N,N′-bis-benzisothiazolylpiperazine impurity. The heterogeneous mixture is heated to 78–82 °C under nitrogen and maintained under aggressive agitation (Reynolds number > 3000 in the liquid phase) for 14–18 h. In-process monitoring via HPLC-UV at 230 nm targets a residual 3-PPBT concentration below 0.15 area% before heat-up to gentle reflux for a polishing hold. The process window is narrow: exceeding 85 °C triggers a base-catalysed retro-Michael side reaction that regenerates free piperazine, which subsequently participates in a competing N-alkylation event and elevates the N-desalkyl genotoxic impurity above the ICH M7 threshold of toxicological concern (1.5 µg/day). Consequently, the free piperazine content in the incoming 3-PPBT lot must be certified at ≤0.10 % w/w; when supplier CoA data indicate levels above 0.08 %, the material is subjected to repurification by low-temperature recrystallization from a toluene/isopropanol mixture (5:1 v/v) at −5 °C, reducing residual piperazine to < 50 ppm. Upon reaction completion, the crude product is cooled to 20 °C, filtered through a pressure leaf filter to remove inorganic salts, and the filtrate is acidified with hydrogen chloride gas dissolved in isopropanol (15 % w/w HCl) to precipitate lurasidone hydrochloride monohydrate. The slurry is dewatered in a horizontal peeler centrifuge with a 0.1 m³ basket capacity, washed with chilled acetone (0–5 °C), and dried in a double-cone vacuum dryer at 45 °C under a vacuum of < 5 mbar until the loss on drying falls below 0.5 %. The final active pharmaceutical ingredient obtained after this penultimate step is further processed into finished dosage forms under conditions that require the 3-PPBT-derived fragment to maintain enantiomeric purity ≥ 99.5 % ee, confirmed by chiral HPLC with a detection limit of 0.05 % for the undesired enantiomer, per USP <541> and Ph. Eur. 2.2.29.
It must be noted that the above requirements represent internal manufacturer specifications aligned with regulatory Drug Master Files; the actual numerical limits are established through batch-to-batch statistical process control on at least 100 commercial-scale campaigns, and any deviation in the 3-PPBT quality immediately alters the downstream crystallization induction time, extending the grinding cycle in the final micronization step by up to 30 % due to polymorphic form contamination. Ziprasidone Mesylate: Amidation Thermochemistry and Base-Accelerated Racemization ControlWhen the same 3-piperazin-1-yl-1,2-benzisothiazole serves as the benzisothiazole carrier in the synthesis of ziprasidone mesylate trihydrate, the chemistry shifts from alkylation to a dehydrative amidation with a 6-chlorooxindole-3-acetic acid derivative, and the thermal management strategy diverges entirely. The amidation is executed in a 3000 L glass-lined reactor configured with an external recirculation loop passing through a plate heat exchanger capable of removing 800 W·kg⁻¹ of reaction mixture. 3-PPBT (1.00 eq, dried at 50 °C for 12 h under −0.095 MPa) is dissolved in tetrahydrofuran (8.0 L per kg of 3-PPBT) and cooled to −5 °C. A coupling reagent system consisting of 1.2 eq of 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide hydrochloride and 0.10 eq of 1-hydroxybenzotriazole hydrate is added, followed by the carboxylic acid substrate pre-dissolved in THF. The rationale for selecting THF over the acetonitrile solvent used in lurasidone preparation is twofold: the oxindole partner undergoes base-catalysed racemization in acetonitrile-K₂CO₃ slurries above 10 °C, and the amidation by-product urea derivative shows exceptionally low solubility in THF, facilitating precipitation-driven purification without a subsequent column chromatography step. The reaction mass is maintained at 0–5 °C during the addition of triethylamine (1.5 eq) over 90 min, after which the cooling is removed and the batch stirs at 22–25 °C for 6 h. In-process control by HPLC stops the reaction when the area% of unreacted 3-PPBT drops below 0.5 %. A critical operational bottleneck arises when relative humidity in the manufacturing suite exceeds 60 %: the THF solution absorbs atmospheric water, hydrolysing the carbodiimide to a formamidine by-product that co-elutes with the desired amide during preparative chromatography on silica gel and demands off-line mass-directed purification that reduces process throughput by 40 %. Therefore, the amidation is strictly performed under a dry nitrogen blanket. The free base of ziprasidone is liberated, dissolved in warm acetone, and treated with methanesulfonic acid (1.05 eq) at 50 °C to yield ziprasidone mesylate trihydrate, which after recrystallization from acetone-water (6:4 v/v) achieves an endotoxin level below 0.10 EU·mg⁻¹ as determined by the limulus amebocyte lysate test per Ph. Eur. 2.6.14. The final trihydrate crystal habit, monitored by XRPD, is sensitive to the cooling rate between 50 °C and 20 °C; a linear ramp of 0.25 °C·min⁻¹ is mandatory to prevent the metastable dihydrate polymorph that exhibits a dissolution rate 30 % lower in pH 6.8 phosphate buffer and consequently fails the USP dissolution test <711>. Microbial spoilage control in synthetic metalworking fluids and industrial recirculating cooling water systems frequently relies on benzisothiazolinone (BIT) chemistry; however, the free solubility of BIT drops below 0.15 wt% in coolants formulated above pH 9.5, leading to precipitation on heat exchanger surfaces. 3-Piperazin-1-yl-1,2-benzisothiazole has been evaluated as a structural variant where the tertiary piperazine nitrogen imparts enhanced alkalinity tolerance and surfactant-like interfacial activity without the formaldehyde-release liability of triazine biocides. Published experimental work extracted from a series of patent filings (e.g., WO2020/xxxxxx) indicates that pre-blending 3-PPBT with monopropylene glycol (1:3 w/w) at 40 °C before dosage into a semi-synthetic cutting fluid concentrate yields a metastable transparent microemulsion. At a use dilution of 0.15 wt% in the fluid reservoir, the compound reduced sulfate-reducing bacteria counts from 10⁶ CFU·mL⁻¹ to below 10² CFU·mL⁻¹ within 72 h when tested according to ASTM E2275-19. The performance edge over BIT is observed exclusively in fluids containing >15 % petroleum sulfonate emulsifiers; in fully synthetic polyalkylene glycol-based coolants, the benzisothiazole-piperazine derivative tends to preferentially partition into the tramp oil phase, causing the residual aqueous concentration to drop below the minimum inhibitory concentration within 200 h. No regulatory approval under the EU Biocidal Products Regulation (BPR) or US FIFRA has been publicly granted for this precise application as of the current writing, and therefore its use remains confined to jurisdictions where it is incorporated as a non-marketed in-can preservative additive under trade secrecy. Under storage conditions exceeding 35 °C, the monopropylene glycol pre-mix shows a steady increase in the oxidized N-oxide metabolite, identified by LC-HRMS, which exhibits 10-fold lower antimicrobial activity; the pre-mix must be kept in sealed HDPE drums under nitrogen headspace and discarded after 90 days. Occupying the Co-Catalyst Phase: Palladium-Ligand Constructs in Amination ChemistryBeyond the landscape of active pharmaceutical ingredient synthesis, the benzisothiazole-piperazine entity has been exploited as an N,N-bidentate ligand precursor for the stabilization of palladium(0) in two-phase water-toluene Buchwald-Hartwig amination protocols. 3-PPBT is metallated with tetrakis(triphenylphosphine)palladium(0) in anhydrous THF at 25 °C for 2 h under argon to form a complex that is extracted into the toluene phase and used directly without isolation. Elemental ICP-OES analysis of the organic layer confirms a Pd loading of 0.12 wt%, and the complex achieves turnover numbers exceeding 4500 in the coupling of 4-bromoanisole with morpholine under 10 bar nitrogen pressure at 90 °C. Unlike the free 3-PPBT, the palladium-ligated form is acutely sensitive to dissolved oxygen, requiring degassing of the aqueous phase to < 0.5 ppm O₂ before injection. The addition of tetrabutylammonium bromide (0.02 eq) further accelerates the rate by a factor of 2.3, ascribed to enhanced phase-transfer kinetics of the anionic Pd(0)-benzisothiazole intermediate. Spectroscopic monitoring of the catalytic cycle by ^31P NMR at the manufacturing site indicates that the active species decomposes via ligand oxidation if the reaction time exceeds 20 h, forming insoluble palladium black that accumulates on the bottom valve of the reactor and demands a manual clean-out with aqua regia every 12 batches, a maintenance frequency that places practical limits on this catalyst system in commercial production settings. Positron emission tomography centers rely on rapid, automated radiochemical syntheses to incorporate ^11C-labeled acyl groups into D₂/5-HT₂A receptor probes for neuropsychiatric studies. The 3-piperazin-1-yl-benzisothiazole core serves as the pre-functionalized scaffold for on-cassette acylation with [^11C]cyclohexanecarbonyl chloride generated in-situ from the corresponding Grignard reagent and [^11C]CO₂ in a GE TRACERlab FX FN module. The acylation is performed in anhydrous THF at −10 °C within a 3.0 mL reaction vessel lined with a PEEK rotary valve, using 5.0 mg of 3-PPBT and a 2.5-fold molar excess of the cyclotron-produced labeling synthon. After 4 min of reaction time, the crude mixture is quenched with 1.0 M ammonium chloride and purified by semi-preparative HPLC on a reverse-phase C18 column (10 × 250 mm, 5 µm) with a mobile phase of acetonitrile/ 50 mM ammonium formate (45:55 v/v) at 5.0 mL·min⁻¹. The product fraction is collected, concentrated, and formulated in 10 % ethanol in saline for intravenous injection, with a final radiochemical purity exceeding 99.0 % and a molar activity above 70 GBq·µmol⁻¹. Quality control failure modes unique to this compound class include radiolysis-induced N-dealkylation at the piperazine ring when the total dose exceeds 180 GBq at end of synthesis, an event that requires the addition of ascorbic acid (0.1 mg·mL⁻¹) as a radical scavenger to the final formulation vial. Each batch is released only after a 3-scan LC-MS check for the non-radioactive impurity peak at m/z 246.1 (corresponding to the cleaved benzisothiazole fragment) is confirmed below 40 µg·mL⁻¹, in accordance with the hospital pharmacy’s internal GMP monograph for research tracers. |
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Designated by CAS 87691-87-0, 3-Piperazin-1-yl-1,2-benzisothiazole is a bicyclic heteroaryl-piperazine building block manufactured as a free-flowing pale-yellow to off-white crystalline powder. The empirical formula is C11H13N3S with a relative molecular mass of 219.31 g·mol−1. Its primary commercial role is as a late-stage intermediate in the convergent synthesis of atypical antipsychotic active pharmaceutical ingredients (APIs), where the intact benzisothiazole–piperazine fragment is introduced via N-alkylation at the distal piperazine nitrogen. Bulk material is produced under full cGMP for registered starting-material supply, with a typical batch size between 50 and 250 kg. The product is not a drug substance; it is a non-sterile, isolated intermediate that must undergo further chemical transformation and purification before any pharmaceutical dosage form is generated. Residual piperazine monomer, a process-related impurity deriving from the stoichiometric excess used during nucleophilic aromatic substitution, is tightly controlled because even sub-0.5% carryover can generate bis-alkylated dimer during subsequent API coupling, a critical impurity flagged by Ph.Eur. monographs for related benzisothiazole drugs.
The 1,2-benzisothiazole ring system fused to a flexible piperazine spacer creates a pharmacophore capable of engaging serotonin 5-HT1A and 5-HT2A receptors as well as dopamine D2 and D3 subtypes in a ratio that reduces extrapyramidal side-effect liability. Unlike the benzisoxazole analogue (3-piperazin-1-yl-1,2-benzisoxazole, the risperidone fragment), the sulfur-containing benzisothiazole exhibits a 0.7–1.0 log unit higher lipophilicity (calculated log P 2.3 versus 1.5 for the benzisoxazole congener), which alters blood-brain barrier permeation kinetics without requiring extensive oxidative debenzylation. In vitro binding assays reported in peer-reviewed literature demonstrate that the benzisothiazole derivative retains a Ki of 1.5 nM at the 5-HT1A receptor while maintaining a D2 Ki of 6.8 nM; the isosteric benzisoxazole shows a 2–3-fold shift in this affinity gap. For synthetic chemists, the advantage is structural: the C–S bond in the isothiazole ring is less electronegative than the C–O bond in the isoxazole, reducing susceptibility to ring-opening during harsh N-alkylation conditions that employ alkyl halides and potassium carbonate in refluxing acetonitrile or DMF. This stability permits higher reaction temperatures—documented at 82–85°C for 18 hours—without generating the ring-scission by-products that complicate purification of the oxygenated isosteres. That difference translates directly into higher yields across the coupling step and fewer column chromatography cycles when isolating the penultimate API intermediate.
Storage presents a well-characterized stability boundary. The free base amine form enters a reversible carbon dioxide absorption cycle when exposed to ambient air at relative humidity exceeding 55%, forming a carbamate salt that reduces the assay value and introduces a 1–2°C melting point depression detectable by differential scanning calorimetry (ASTM E967). Manufacturers therefore package the material in double polyethylene liners inside fiber drums, back-flushed with nitrogen to maintain headspace oxygen below 0.5% v/v. A stability study executed in accordance with ICH Q1A(R2) at 25°C/60% RH over 24 months confirmed no significant degradation—purity change ≤0.15% area by HPLC—provided the unopened container remains sealed. Once opened, the product should be handled inside a glovebox or dry-room meeting ISO 8 classification, and any unused portion must be re-purged and re-sealed within 4 hours to avoid carbamate accumulation. These handling requirements differ from those of the corresponding hydrochloride salt (CAS 1187928-24-8), which is non-hygroscopic but introduces chloride counter-ion removal challenges during downstream free-basing steps. The choice of free base versus salt form thus becomes a process-engineering decision driven by the capabilities of the API step team: the free base eliminates an ion-exchange operation but demands stricter environmental controls on the manufacturing floor.
Quality specifications are benchmarked against individual monograph requirements issued by the European Pharmacopoeia for the downstream API. The release panel includes chromatographic purity determined by reversed-phase HPLC with a C18 column (150 mm × 4.6 mm, 5 µm particle size), mobile phase consisting of 0.1% trifluoroacetic acid in water/acetonitrile gradient, and UV detection at 230 nm. Retention time of the main peak is approximately 8.3 minutes under these conditions. Quantitation of residual piperazine is performed by ion-pair chromatography using sodium octanesulfonate, method sensitivity to a limit of quantitation of 0.02% w/w. Heavy metals are screened per USP 〈232〉/〈233〉 via ICP-MS, with acceptance limits aligned to ICH Q3D Option 1: cadmium ≤0.5 µg/g, lead ≤0.5 µg/g, arsenic ≤0.5 µg/g, mercury ≤0.3 µg/g. Any catalysts employed in the synthetic route—such as palladium on carbon if a reductive amination path is utilized—are monitored with a specific limit of residual palladium ≤10 µg/g. The specification profile is summarized in Table 1, which consolidates the critical quality attributes as they would appear on a certificate of analysis issued to a pharmaceutical recipient.
| Parameter | TestMethod/Standard | Acceptance Criterion | Typical Value |
|---|---|---|---|
| Appearance | Visual (Ph.Eur. 2.2.1) | Pale-yellow to off-white crystalline powder | Conforms |
| Identification | IR spectroscopy (ATR, 4000–400 cm−1); 1H NMR (DMSO-d6, 400 MHz) | Matches reference spectrum; chemical shifts within ±0.05 ppm | Conforms |
| Assay (HPLC, % area) | In-house HPLC method, external standard, drying basis | ≥98.0% | 99.3% |
| Melting range | DSC (ASTM E967), onset temperature | 104–108°C | 105.6°C |
| Water content | KF coulometry (ASTM E203) | ≤0.5% | 0.15% |
| Residual piperazine | Ion-pair HPLC | ≤0.3% | 0.08% |
| Residual solvents (Class 2) | HS-GC (USP 〈467〉/Ph.Eur. 2.4.24) | Acetonitrile ≤410 ppm, DMF ≤880 ppm | Acetonitrile 45 ppm, DMF 120 ppm |
| Sulfated ash | USP 〈281〉 | ≤0.1% | 0.03% |
| Heavy metals (ICH Q3D) | ICP-MS (USP 〈233〉) | As, Cd, Pb ≤0.5 µg/g; Hg ≤0.3 µg/g | All ≤0.1 µg/g |
The primary route of manufacture involves nucleophilic aromatic substitution between 3-chloro-1,2-benzisothiazole (CAS 7716-66-7) and anhydrous piperazine in refluxing toluene or n-butanol. Pilot-scale experience on a 160-L glass-lined reactor demonstrates that the molar ratio of piperazine to chloro-benzisothiazole must be kept at ≥ 3.5:1 to suppress the formation of the symmetrical bis(benzisothiazole) impurity (CAS undetermined), which precipitates as a toluene-insoluble solid that fouls the condenser and agitator blades. A jacket temperature ramp of 1°C·min−1 from 25°C to 110°C is employed, and the onset of exothermic substitution is observed at 78°C by reaction calorimetry. Post-reaction workup includes aqueous quenching at 15–20°C to precipitate the crude product while keeping excess piperazine in the aqueous phase. Multiple displacement washes with 10% brine at pH 9–10 reduce ammonium salt carryover, but if the pH drifts below 8.5 during washes, the product begins to dissolve as the hydrochloride, lowering isolated yield dramatically from a baseline 82–85% to below 60%. This pH-dependent solubility window—optimized at 9.0 ± 0.3—is a frequent root cause of batch-to-batch variability observed in technology transfer reports.
When compared to alternative benzisothiazole-piperazine variants, the unsubstituted piperazine headgroup confers the highest degree of synthetic latitude for downstream diversification. The 4-methyl-piperazine analogue (CAS 178748-91-3) is sometimes selected to avoid the need for subsequent N-protection, but its inherent methyl group blocks the nitrogen required for coupling with chloroethyl-indole or -indoline electrophiles; reductive methylation of the terminal piperazine nitrogen of the target API can reverse this, adding a step that requires formaldehyde and sodium cyanoborohydride, introducing Class 2 solvent acetonitrile and potential cyanide residues into the process. The 4-Boc-protected derivative (CAS 953407-91-7) provides orthogonal protection but suffers from thermal lability: thermogravimetric analysis shows a 13% mass loss at 150°C due to isobutylene evolution, which prohibits its use in elevated-temperature alkylations above 120°C. The free base form described here maintains thermal stability up to 180°C (decomposition onset by TGA, 10°C·min−1 ramp, nitrogen atmosphere) and avoids both the deprotection and genotoxic impurity concerns associated with the Boc group. Table 2 enumerates these differentiators across a set of commercially available benzisothiazole-piperazine intermediates.
| Compound | CAS | Key Processing Advantage | CriticalLimitation | Typical Downstream Use |
|---|---|---|---|---|
| 3-Piperazin-1-yl-1,2-benzisothiazole (free base) | 87691-87-0 | Direct N-alkylation without deprotection; high thermal headroom (180°C) | Hygroscopic; requires dry atmosphere handling (≥60% RH carbonation risk) | Ziprasidone, perospirone, and generic pipeline molecules |
| 3-(4-Methylpiperazin-1-yl)-1,2-benzisothiazole | 178748-91-3 | No N-protection needed; non-hygroscopic crystalline solid | Terminal methyl blocks direct coupling with haloethyl-indole linkers; requires subsequent demethylation/reduction | N-oxide metabolites; PET tracer precursors |
| 4-(1,2-Benzisothiazol-3-yl)piperazine-1-carboxylic acid tert-butyl ester | 953407-91-7 | Boc protection masks amine during incompatible steps; simplifies chromatographic purification | Thermal lability limits coupling temperatures to ≤120°C; genotoxic potential of tert-butyl carbocation byproducts | Research-scale analog libraries; process development lot supply |
| 3-Chloro-1,2-benzisothiazole | 7716-66-7 | High electrophilicity; supports diversification into any amine nucleophile | Not a piperazine adduct; requires in situ piperazine coupling with excess piperazine and bis-adduct formation control | Late-stage diversification; parallel medicinal chemistry |
Regulatory starting-material dossiers submitted for this intermediate typically include a DMF in eCTD format, filed to the US FDA under Type II. The residual solvent profile aligns with ICH Q3C(R8) limits for acetonitrile (Class 2, 410 ppm) and N,N-dimethylformamide (Class 2, 880 ppm). No genotoxic structural alerts are present in the molecule itself; however, the synthetic history requires an absence of 3-chloro-1,2-benzisothiazole carryover, which is monitored as a potential alkylating agent impurity. TTC-based limits derived under ICH M7 define an acceptable intake of 15 µg/day for the chloro precursor, translating to a specification of ≤75 ppm in the intermediate when the maximum daily dose of the final API is 200 mg. This limit is routinely achieved by a recrystallization from isopropanol/water (7:3 v/v) that reduces chloro derivative content to below 30 ppm, demonstrated across ten consecutive validation batches. Suppliers operating under the EU REACH regulation have registered this substance at a tonnage band of 1–10 tonnes per annum; the registration dossier classifies it as a skin irritant (H315) and serious eye irritant (H319) based on in vitro reconstructed human epidermis assays performed following OECD TG 439.
Production-scale experience highlights the importance of controlling residual piperazine during the coupling step that attaches the benzisothiazole-piperazine fragment to the chloroethyl-indole (or indoline) core. In a 500-L Hastelloy reactor operating under nitrogen atmosphere at 85°C with anhydrous potassium carbonate as base, residual piperazine exceeding 0.5% w/w in the input intermediate was found to consume the alkyl chloride electrophile through a competing N-alkylation pathway, producing N-(2-chloroethyl)piperazine as a process impurity that tracks through telescoped stages and appears at the API stage as a piperazine-dimer contaminant. The dimer is chromatographically separable only on a hydrophilic interaction liquid chromatography (HILIC) column, and its removal requires a dedicated flash chromatography campaign that adds 14–18 hours to the overall production cycle time. Therefore, the acceptance criterion of ≤0.3% residual piperazine is not an arbitrary purity target; it is an economic boundary defined by purification cost curves and downstream cycle-time budgets. This interplay between intermediate quality and API step performance is a recurring theme in technology transfers, where in-house analytical development teams must establish in-process controls capable of quantifying piperazine at the 0.02% threshold using derivatization with o-phthalaldehyde and fluorescence detection if HPLC-UV sensitivity proves insufficient.