Designated by CAS registry number 87691-88-1 and molecular formula C₁₁H₁₃N₃S·HCl (formula weight 255.77 g·mol⁻¹), 3-(1-Piperazinyl)-1,2-benzisothiazole monohydrochloride is a heteroarylpiperazine intermediate deployed primarily in the convergent assembly of second-generation atypical antipsychotics. The molecule comprises a 1,2-benzisothiazole heterocycle substituted at the 3-position with a piperazine ring, isolated as the monohydrochloride salt. Commercial lots are typically manufactured via nucleophilic aromatic substitution between 3-chloro-1,2-benzisothiazole and piperazine in a high-boiling aprotic solvent, followed by hydrochloride salt formation and multi-solvent recrystallization to achieve single-impurity profiles below 0.10 area-%. The salt form ensures a crystalline morphology with a melting endotherm onset at 256–260°C (differential scanning calorimetry, 10 K·min⁻¹ ramp, nitrogen purge), a processing advantage over the free base, which exhibits hygroscopic amorphization tendencies when stored below 40% RH. As a key raw material in active pharmaceutical ingredient (API) syntheses governed by Current Good Manufacturing Practice (cGMP), the compound is supplied under full technical packages referencing Ph.Eur. general monographs and ICH Q3A threshold guidelines for genotoxic impurity control.
Can Residual Piperazine Derivatization Skew the Potency Assay of the Downstream API?
The monohydrochloride salt is specified with a free piperazine ceiling of ≤0.30% w/w (quantified by hydrophilic interaction chromatography with charged aerosol detection, LOD 0.05 µg·mL⁻¹). Elevated residual piperazine, a common carry-over from stepwise quenching protocols in batch reactors equipped with 3:1 height-to-diameter ratio and retreat-curve impeller agitators, participates in downstream reductive amination side-reactions during ziprasidone final assembly, generating an N-alkylated piperazine dimer. In one production-scale investigation across a 2000 L glass-lined vessel, a residual piperazine load of 0.52% w/w in the intermediate lot correlated with a potency reduction of 1.2% in the final hydrochloride salt monohydrate API when assayed against USP reference standard lot F068N0 via HPLC Method USP43-NF38 monograph “Ziprasidone Hydrochloride”. Forced degradation studies confirm that the dimer co-elutes under standard octadecylsilane (C18) isocratic conditions with the parent API, necessitating an orthogonal phenyl-hexyl column configuration (150 mm × 4.6 mm, 3 µm) and a 0.05 M ammonium acetate:acetonitrile gradient to resolve the interfering peak. Thus, the piperazine specification in the benzisothiazole intermediate is not merely an in-process control parameter but a direct determinant of pharmacopeial assay compliance for the finished dosage form.
Specification Framework Anchored to ICH Q6A Decision Tree #1
The monohydrochloride is routinely released against a suite of tests harmonized across API supply chains. A representative certificate-of-analysis profile appears below.
| Attribute | Acceptance Criterion | Analytical Procedure Reference |
|---|---|---|
| Appearance | Off-white to pale yellow crystalline powder | Visual; Ph.Eur. 2.2.1 |
| Identification (IR) | Conforms to reference spectrum; peak at 1635 cm⁻¹ (C=N stretch) | ATR-FTIR; Ph.Eur. 2.2.24 |
| Assay (anhydrous, solvent-free basis) | 98.0–102.0% | HPLC, C18, 210 nm; USP ⟨621⟩ |
| Chromatographic Purity (total impurities) | ≤0.40% | HPLC area normalization; Q3A reporting threshold 0.05% |
| Individual Specified Impurity: 3-Chloro-1,2-benzisothiazole | ≤0.10% (genotoxic alert, nitrenium ion formation) | GC-MS SIM; LOD 1 ppm |
| Water Content | ≤0.5% w/w | Karl Fischer coulometry; USP ⟨921⟩ Method Ia |
| Residue on Ignition (Sulfated Ash) | ≤0.1% | Ph.Eur. 2.4.14 |
| Heavy Metals | ≤10 ppm | ICP-MS; ICH Q3D elemental impurities Option 1 |
| Residual Solvents (IPA, toluene, dichloromethane) | Class 2 limits per ICH Q3C; DCM ≤600 ppm | Headspace GC-FID; USP ⟨467⟩ Procedure A |
| Particle Size Distribution (D₉₀) | ≤150 µm | Laser diffraction, dry dispersion; ISO 13320 |
When this intermediate is designated for a high-potency API filing requiring a polymorphic stability dossier, an additional XRPD diffractogram is provided. The monohydrochloride salt crystallizes in the triclinic space group P1̄ with characteristic Bragg reflections at 2θ = 12.8°, 16.5°, and 23.4° (Cu Kα radiation, 40 kV/40 mA). Crushing force applied during D₉₀ milling must remain below 12 N to avoid amorphization of surface layers beyond a depth of 50 nm (confirmed by grazing-incidence wide-angle X-ray scattering), a factor that directly alters dissolution kinetics in the ensuing nucleophilic coupling step.
When the Free Base Exacerbates Emulsion Formation in the Alkylation Reactor
A direct comparison between the monohydrochloride salt and the corresponding free base, 3-(1-piperazinyl)-1,2-benzisothiazole (CAS 87691-87-0), reveals a critical process selectivity divergence. The free base, a viscous orange oil at ambient temperature with a pKa of the piperazine secondary amine of approximately 8.2 (calculated by SPARC v4.2), undergoes unintended N-acylation at both the proximal and distal piperazine nitrogens when treated with chloroacetyl chloride in dichloromethane‑water biphasic systems. This yields a statistical mixture of mono- and bis-adducts which cannot be resolved by fractional distillation. In contrast, the monohydrochloride, suspended in dichloromethane with 0.5 M aqueous sodium carbonate in a 500 L jacketed reactor operated at −5°C to 0°C, undergoes smooth mono-chloroacetylation at the free piperazine nitrogen to yield the desired 2-(chloroacetyl)-3-(1-piperazinyl)-1,2-benzisothiazole intermediate with a diastereomeric excess approaching 100% and an isolated yield exceeding 91% after phase separation and antisolvent precipitation. The salt form suppresses the pH-dependent solubility of the free base in the aqueous layer (log D7.4 reduction from 1.7 to 0.3), minimizing micelle-assisted cross-phase transfer that otherwise stabilizes persistent rag layers at the liquid–liquid interface. Published data for emulsion breakage times in the free-base process indicate batch filtration delays of 4–6 h on a 0.5 µm sintered polypropylene filter cartridge, whereas salt-based batches clarify within 30 min.
Thermal Hazard Thresholds During Piperazine Charge and HCl Salt Isolation
The exothermic neutralization step—introducing 37% w/w hydrochloric acid to a methanol solution of the free base at 20–25°C—releases a crystallization enthalpy of −98.5 kJ·mol⁻¹ (reaction calorimetry, Mettler-Toledo RC1e, 1 L isothermal mode). If the acid addition rate exceeds 0.8 mol·h⁻¹ per kg reaction mass, the localized temperature spike can surpass 45°C within the addition zone, instigating acid-catalyzed ring-opening of the benzisothiazole heterocycle and generating a dark-brown 2-mercaptobenzamide sulfonic acid decomposition product that stains crystalline product. To contain this, manufacturing instructions specify a titan-grade Hastelloy C-276 reactor with jacket temperature control to ±1.5°C, a dilute HCl feed (6 M pre-cooled to 5°C), and a pitched-blade turbine delivering an agitation power number of 1.3 to maintain a bulk Reynolds number above 10⁴. Under these parameters, the crystal size distribution exhibits a volume-mean diameter (D[4,3]) of 85 ± 12 µm, optimal for vacuum filtration on a 316L stainless steel Nutsche filter with a polyethylene cloth of pore size 10 µm. Deviation from the prescribed temperature envelope during acid addition increases fines (<10 µm) fraction to >25%, resulting in filter cloth blinding and wet cake residual moisture above 2.0%, which prolongs the subsequent fluid-bed drying cycle from 4 h to 9 h (Glatt WSG-30 dryer, inlet air 60°C, dew point −20°C).
Comparative Aqueous Solubility and Its Impact on Coupling with Anhydride Electrophiles
A structural congener, 3-chloro-1,2-benzisothiazole, exhibits a solubility of less than 0.01 mg·mL⁻¹ in water at 25°C, which forces heterogeneous reaction conditions with piperazine and yields significant hydrolysis of the chloro substituent to the benzisothiazolinone byproduct. The monohydrochloride, by contrast, has an aqueous solubility of 12 mg·mL⁻¹ (shake-flask method, HPLC-UV quantitation) in unbuffered deionized water, translating to a dissolved fraction sufficient for homogeneous acylation under Schotten–Baumann protocols with glutaric anhydride. This difference is exploited in the manufacture of ziprasidone: the monohydrochloride is reacted with glutaric anhydride in a 1:1.05 molar ratio in tetrahydrofuran‑water (4:1 v/v) at 0–5°C, yielding the intermediate 5-{2-[4-(1,2-benzisothiazol-3-yl)piperazin-1-yl]ethyl}-5-oxopentanoic acid hydrochloride with an isolated purity of 99.2 area-% after a simple isopropyl alcohol wash. The free base demands a strictly anhydrous tetrahydrofuran system and 3 Å molecular sieves to achieve similar conversion; even then, the absence of the hydrochloride counterion results in partial salt formation with the glutaric acid half-ester, creating a complex mixture that requires column chromatography (silica gel, chloroform‑methanol 9:1) and reduces isolated yield to 65–72%.
In controlled-chamber photostability studies conforming to ICH Q1B Option 2, the pale-yellow monohydrochloride powder exhibits a 0.3% increase in total chromatographic impurities after an exposure dose of 1.2 million lux·h visible light and 200 W·h·m⁻² near-ultraviolet radiation in a Suntest CPS+ device. This stability is attributable to the salt bridge which rigidifies the crystal lattice and quenches excited-state proton-transfer pathways. In solution, however, the free base degrades by 8.5% under identical irradiance, forming a major photoproduct identified as dibenzo[b,f][1,4]thiazepine by high-resolution QTOF mass spectrometry. Consequently, storage of the monohydrochloride raw material is specified in amber HDPE drums with a PET/aluminum foil/LDPE laminated liner, closed under nitrogen overlay (O₂ < 0.5% v/v headspace), and warehoused below 25°C. Under these conditions, retest dating of 36 months is supported by real-time stability batch data (three production lots, storage condition 25°C/60% RH).