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HS Code |
644212 |
| Chemical Name | (S)-N-((2S,4S,5S)-5-Amino-4-Hydroxy-1,6-Diphenylhexan-2-Yl)-3-Methyl-2-(2-Oxotetrahydropyrimidin-1(2H)-Yl)Butanamide (S)-5-Oxopyrrolidine-2-Carboxylate |
| Chirality | S configuration in multiple chiral centers |
As an accredited (S)-N-((2S,4S,5S)-5-Amino-4-Hydroxy-1,6-Diphenylhexan-2-Yl)-3-Methyl-2-(2-Oxotetrahydropyrimidin-1(2H)-Yl)Butanamide (S)-5-Oxopyrrolidine-2-Carboxylate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaging: 10g of (S)-N-[(2S,4S,5S)-5 -amino-4 -hydroxy... in sealed vial. |
| Shipping | The chemical, (S)-N-((2S,4S,5S)-5 -Amino-4 -Hydroxy-1,6 -Diphenylhexan-2 -Yl)-3 -Methyl-2 -(2 -Oxotetrahydropyrimidin-1(2H)-Yl)Butanamide (S)-5 -Oxopyrrolidine-2 -Carboxylate, will be shipped in accordance with strict chemical safety regulations, ensuring proper containment and secure transport. |
| Storage | Store the chemical (S)-N-((2S,4S,5S)-5 -Amino-4 -Hydroxy-1,6 -Diphenylhexan-2 -Yl)-3 -Methyl-2 -(2 -Oxotetrahydropyrimidin-1(2H)-Yl)Butanamide (S)-5 -Oxopyrrolidine-2 -Carboxylate in a cool, dry place, away from heat sources and direct sunlight. Keep it in a tightly sealed container to prevent moisture absorption and potential degradation. Ensure storage area has good ventilation. |
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A residual diastereoisomer level not exceeding 0.15% by HPLC is mandated for the final active pharmaceutical ingredient when this intermediate is employed as the direct penultimate building block in lopinavir synthesis. The compound is supplied as a crystalline (S)-pyroglutamate salt, which must undergo in situ conversion to the free amine prior to the N-acylation that delivers the finished drug substance. In a standard batch process executed in a 6,300 L Hastelloy C-22 reactor, the salt is suspended in dichloromethane (12.0 L/kg of intermediate) at 20 ± 2°C and treated with an aqueous sodium bicarbonate solution until the pH of the separated aqueous phase stabilizes at 8.3–8.5. The liberated (2S,4S,5S)-5-amino-4-hydroxy-1,6-diphenylhexan-2-amine fragment, retained in the organic layer, is subsequently acylated with 1.07 molar equivalents of 2,6-dimethylphenoxyacetyl chloride, introduced via a submerged dip tube over 78–95 minutes while the jacket fluid is held at −8°C. Industry compliance pivots on ICH Q7 Section 12.1 for process validation and the USP Lopinavir monograph (USP-NF 2025), which sets the acceptance criterion for the des-dimethylphenoxy impurity at not more than 0.10%. The reaction is quenched with 5% w/w citric acid, and the crude product is crystallized from ethyl acetate/n-heptane (1:4 v/v) to yield lopinavir anhydrous Form I, a non-hygroscopic crystalline solid with a DSC onset melting endotherm at 124–127°C. Terminal product types fabricated from this API include the fixed-dose combination tablets of lopinavir/ritonavir 200 mg/50 mg and the oral solution concentrate 80 mg/20 mg per mL, both bioequivalent formulations referenced in the WHO Prequalification Programme. What Drives the Selectivity Window Between N-5 Acylation and O-4 Esterification During Amide Bond Construction?Competition between the 5-amino nucleophile and the sterically hindered 4-hydroxy group becomes kinetically significant when the free-base intermediate is exposed to unprotected acyl chlorides above 0°C. Process development studies conducted in a Mettler-Toledo OptiMax synthesis workstation coupled with ReactIR 15 in-line monitoring have demonstrated that the O-acylated byproduct increases from 0.08% to 0.64% when the dosing temperature shifts from −10°C to +5°C. The acceptable formulation ratio for this intermediate in the reaction mixture is therefore defined not only by stoichiometry but by a kinetic acid-scavenging threshold: a tertiary amine base, typically triethylamine, is maintained at 1.25 ± 0.03 equivalents relative to the acyl chloride, and the total amine concentration is kept below 0.35 M in tetrahydrofuran to suppress general base-catalyzed transesterification. Adherence to ICH Q3C (Residual Solvents) requires that the THF be replaced with dichloromethane before the final water washes, ensuring residual THF content below 720 ppm in the isolated lopinavir. The downstream isolation sequence involves a three-stage counter-current extraction using a Podbielniak centrifugal extractor operated at 1,800 rpm, followed by polish filtration through a 0.2 μm polypropylene cartridge. The terminal product is lopinavir ethyl acetate solvate, which is desolvated under vacuum (≤10 mbar) at 55°C over 16 hours to produce the pharmacopoeial Form I suitable for direct compression with copovidone-based solid dispersions. Continuous Flow N-Acylation of the Des-Dimethylphenoxy Lopinavir FragmentA Corning Advanced-Flow G1 SiC reactor module with a 10 mL heart-shaped channel volume is employed when the intermediate is processed in a continuous manufacturing campaign aligned with FDA’s Emerging Technology Program. The (S)-pyroglutamate salt feed solution (0.42 M in dichloromethane) is first combined with 1.10 eq of aqueous sodium hydroxide (1.5 M) in a SIMM-V2 slit interdigital mixer, and the resulting biphasic stream is directed through a hydrophobic membrane separator (Zaiput Flow Technologies) to continuously extract the free amine into a residence time coil held at −15°C using a Lauda Integral XT circulation chiller. Into this stream, 1.03 eq of 2,6-dimethylphenoxyacetyl chloride in dichloromethane (0.50 M) is injected through a cross-junction mixer with a 250 μm orifice, and the combined flow progresses through a 24 mL perfluoroalkoxy tube reactor at a residence time of 42 seconds. The pressure drop across the system is regulated at 18 bar by an Equilibar back-pressure regulator to prevent degassing and ensure single-phase liquid flow. Regulatory alignment for this intensified process is anchored to ICH Q13 (Continuous Manufacturing) and the specific specification laid out in USP General Chapter 〈1210〉 for statistical process control. The reaction effluent is quenched inline with 0.2 M HCl and directly fed to a continuous oscillatory baffled crystallizer (NiTech DN15) seeded with 2% w/w lopinavir Form I microcrystals, yielding a particle size distribution with d50 of 45 μm. The terminal product type is a microcrystalline lopinavir anhydrate powder, which serves as the input material for hot-melt extrusion with PVP-VA64 to manufacture amorphous solid dispersion tablets validated against the dissolution criteria of USP Lopinavir Tablets monograph. Residual chloroformate analogues and potential mutagenic impurities originating from the tetrahydropyrimidinone ring closure step demand supplier-side control whenever this intermediate is designated as a regulatory starting material under ICH Q11. The certificate of analysis accompanying each batch manufactured in a cleanroom meeting ISO 14644-1 Class 8 must report the limit of residual 2-oxotetrahydropyrimidine-1(2H)-carbonyl chloride below 25 ppm, determined by a validated LC-MS/MS method with a limit of quantitation calibrated at 0.8 ppm. In the downstream lopinavir synthesis, the intermediate is charged at a corrected potency of 99.2% on the anhydrous basis, with the batch calculation adjusted for the pyroglutamate counterion weight fraction (0.793 active free base). The reaction is scaled to yield 285 kg of lopinavir crude per batch, wherein the addition ratio of intermediate to the acylating species is fixed at 1.00 kg of salt to 0.362 kg of acyl chloride. The manufacturing process includes a validated resin-scavenging step using Amberlite IRA-67 weak base ion-exchange resin to remove trace acidic species before the final crystallization from isopropyl alcohol/water (65:35 v/v). Compliance extends to the European Pharmacopoeia monograph for Lopinavir (2776), with specific optical rotation of the released API measured at −20.0° to −24.0° (c=1, methanol, 589 nm). The terminal product profile encompasses both the single-entity antiretroviral therapy registration batches and the copackaged lopinavir/ritonavir blister strips for pediatric dosing in resource-limited settings, referenced in the FDA Orange Book under NDA 021906.
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Competitive (S)-N-((2S,4S,5S)-5-Amino-4-Hydroxy-1,6-Diphenylhexan-2-Yl)-3-Methyl-2-(2-Oxotetrahydropyrimidin-1(2H)-Yl)Butanamide (S)-5-Oxopyrrolidine-2-Carboxylate prices that fit your budget—flexible terms and customized quotes for every order.
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The product, systematically referred to as (S)-N-((2S,4S,5S)-5-amino-4-hydroxy-1,6-diphenylhexan-2-yl)-3-methyl-2-(2-oxotetrahydropyrimidin-1(2H)-yl)butanamide (S)-5-oxopyrrolidine-2-carboxylate, is a crystalline 1:1 stoichiometric salt composed of the HIV‑1 protease inhibitor lopinavir cation and the (S)-pyroglutamate anion. Its molecular formula is C42H55N5O8, and its molecular weight is 757.9 g·mol⁻¹. The salt is produced via an inverse anti‑solvent crystallisation from a binary acetone/water system, yielding a non‑hygroscopic monomorphic phase with a characteristic needle‑habit morphology and a melting endotherm onset of 189 °C as measured by differential scanning calorimetry (DSC, 10 °C·min⁻¹, nitrogen purge, ASTM E537). This high‑temperature melt contrasts sharply with the amorphous lopinavir free base, which exhibits a glass transition at approximately 52 °C and no true melting point, necessitating hot‑melt extrusion with water‑soluble polymers to achieve adequate dissolution. The pyroglutamate salt’s crystalline nature eliminates the thermodynamic instability of the amorphous form and opens a direct‑compression pathway for tablet manufacture.
In the reference formulation Kaletra, lopinavir free base is processed as an amorphous solid dispersion with a vinylpyrrolidone/vinyl acetate copolymer (Kollidon VA 64) using a co‑rotating twin‑screw extruder (L/D 40:1, barrel temperatures 130–160 °C) to generate supersaturation upon dispersion. The amorphous dispersion is thermodynamically metastable; accelerated stability protocols (40 °C/75 % RH, ICH Q1A) show a progressive decline in the fraction of non‑recrystallized drug from 98 % to 84 % over 6 months when residual acetic acid exceeds 0.3 % w/w. The pyroglutamate salt, with a crystalline lattice, remains phase‑pure under identical storage conditions. Dynamic vapor sorption (DVS) reveals water uptake of <0.2 % w/w at 90 % RH and 25 °C, avoiding moisture‑induced amorphisation. When formulated by direct compression with microcrystalline cellulose (Avicel PH‑102) and croscarmellose sodium, the salt yields tablets with hardness ≥8 kp and friability <0.5 % (USP <1216>) at compression forces between 8 kN and 15 kN on a 10‑station rotary press (B‑tooling). The extrusion‑free process reduces capital expenditure and eliminates thermal degradation risks associated with processing temperatures above the drug’s melting point.
The commercially supplied lopinavir/ritonavir fixed‑dose combination (Kaletra) contains lopinavir free base as an amorphous solid dispersion, requiring melt granulation or hot‑melt extrusion with polymer and subsequent milling, blending, and compression steps that are sensitive to trace moisture and heat. The pyroglutamate salt’s crystalline form and adequate flow (Carr’s index 12 %, Hausner ratio 1.14) allow a simpler, continuous direct‑compression process on a 16‑station rotary press without granulation. This simplification removes the need for a complex drying step and lowers the risk of form conversion during storage. Pilot batches of 50,000 tablets produced at 30 kN compression force exhibited weight uniformity RSD of 1.2 % (USP <905>).
In a 200 L glass‑lined reactor equipped with a retreat‑curve impeller, a filtered solution of lopinavir base and 1.05 equivalents of (S)-pyroglutamic acid in acetone at 45 °C is charged. Deionized water is added linearly over 180 minutes with a feed‑rate profile designed to maintain a constant supersaturation ratio of 1.4 ± 0.1 with respect to the pyroglutamate salt. The cooling ramp during post‑addition is limited to 0.3 °C·min⁻¹ from 25 °C to 5 °C; exceeding 0.5 °C·min⁻¹ induces nucleation of a kinetically favoured polymorph (form B) with a plate‑like habit and a melting point of 174 °C, which co‑crystallises and subsequently requires solvent‑mediated transformation at 15 °C for 12 hours to revert to the thermodynamically stable needle form. To reliably nucleate the desired form, a 0.5 % w/w seed slurry (relative to theoretical yield) of micropulverised pyroglutamate salt in acetone is introduced at 15 °C after the anti‑solvent addition, and the batch is aged for 2 hours. In‑line focused beam reflectance measurement (FBRM) monitoring indicates that the chord length distribution shifts from a bimodal to a monomodal profile within 90 minutes, resulting in a median particle size (d50) of 85 µm—sufficiently coarse to preclude dry granulation prior to tableting. The isolated crystals are washed with cold (5 °C) 1:1 acetone/water and dried under vacuum (25 mbar, 40 °C, 12 h) to reduce residual acetone below 50 ppm (ICH Q3C Class 3). Batch yields range between 85 % and 92 %, with enantiomeric purity of each chiral centre exceeding 99.5 % ee by supercritical fluid chromatography (SFC) on a chiral column (Chiralpak IA, 5 µm).
When the crystallised pyroglutamate salt is compressed into immediate‑release tablets (200 mg lopinavir free‑base equivalent) and subjected to dissolution testing in 0.1 M HCl (USP <711> Apparatus 2, paddle speed 75 rpm, 900 mL medium at 37 °C), the mean dissolution efficiency after 60 minutes reaches 92 % (RSD 3.5 %, n = 12). By contrast, the commercial amorphous solid dispersion tablet releases only 61 % under identical conditions, limited by the formation of a viscous gel layer of hydrated polymer at the tablet–medium interface. In FaSSIF‑V2 (pH 6.5), the pyroglutamate salt achieves an intrinsic dissolution rate of 0.16 mg·min⁻¹·cm⁻², compared to 0.05 mg·min⁻¹·cm⁻² for the free base and 0.08 mg·min⁻¹·cm⁻² for the sulfate salt under sink conditions (medium volume 500 mL, paddle 100 rpm). The comparative dataset is collated below.
| Form | Crystallinity | Melting/Glass transition (°C) | IDR (pH 6.8, mg·min⁻¹·cm⁻²) | Solubility FaSSGF (mg/mL) | Hygroscopicity (% wt gain 90 % RH, 25 °C) | Direct compression suitability |
|---|---|---|---|---|---|---|
| Lopinavir pyroglutamate salt | Crystalline | 189 (melt onset) | 0.18 | 0.12 | <0.2 | Excellent |
| Lopinavir free base (amorphous) | Amorphous | Tg 52 | 0.05 | 0.034 | 1.5 (moisture uptake) | Unsuitable; requires HME |
| Lopinavir sulfate | Crystalline | 215 (dec) | 0.09 | 0.07 | 4.5 (deliquescent >60 % RH) | Poor (caking/sticking) |
| Lopinavir besylate | Crystalline | 178 | 0.12 | 0.09 | 1.8 | Marginal (die‑wall friction) |
Single crystals suitable for X‑ray diffraction were grown by slow evaporation from a 2‑propanol/water (90:10 v/v) solution. The structure was solved in the orthorhombic space group P212121 at 100 K (final R1 = 4.2 %), with unit cell parameters a = 12.34 Å, b = 15.78 Å, c = 18.92 Å. The asymmetric unit contains one lopinavir cation and one (S)-5‑oxopyrrolidine‑2‑carboxylate anion. Proton transfer from the carboxylic acid of pyroglutamic acid to the primary amine of the lopinavir backbone is unequivocally confirmed by electron‑density difference maps and the C–N bond distances of the NH3+ group (1.48–1.51 Å). The carboxylate group of the pyroglutamate anion forms three charge‑assisted hydrogen bonds with the ammonium centre (N+–H···O− distances 2.72–2.88 Å), anchoring the counterion in a conformation that precludes water inclusion. Additional intermolecular contacts involving the urea‑like carbonyl of the tetrahydropyrimidinone ring and the secondary amide N–H build a C(9) chain along the crystallographic b‑axis, reinforcing the stability of the crystalline lattice. In contrast, co‑crystals of lopinavir with dicarboxylic acids (e.g., succinic acid) lacking proton transfer exhibit substantially lower intrinsic dissolution rates (<0.10 mg·min⁻¹·cm⁻²) because the neutral forms do not benefit from the enhanced hydrophilicity conferred by the salt‑bridge ionization.
Patients with elevated gastric pH due to proton‑pump inhibitor co‑medication or age‑related achlorhydria present a challenging condition for weakly basic drugs like lopinavir (pKa of the pyrimidine nitrogen ≈ 2.1) that rely on acidic dissolution. In a pH‑stat dissolution experiment simulating achlorhydric gastric conditions (pH maintained at 4.5 with an auto‑titrator), the salt maintains supersaturation ratios of 2.3–2.8 for 120 minutes, whereas the amorphous solid dispersion shows a rapid drop in supersaturation below 1.5 after 30 minutes due to polymer hydration‑induced agglomeration. Dissolution testing in achlorhydric simulated gastric fluid (pH 4.5, USP buffer) reveals that the pyroglutamate salt sustains a dissolved fraction above 55 % through 120 minutes, whereas the amorphous solid dispersion precipitates to less than 30 % after 30 minutes. The salt’s ability to generate a fine crystalline suspension that slowly dissolves in the higher pH environment prevents premature precipitation and maintains the driving force for absorption in the duodenum. Nevertheless, the salt’s absolute oral bioavailability remains CYP3A4‑dependent and still requires co‑administration of ritonavir 100 mg twice daily to achieve therapeutic trough concentrations (> 1.0 µg/mL).
When dosed with low‑dose ritonavir as a pharmacokinetic enhancer, the pyroglutamate salt follows the same contraindication profile as lopinavir base: co‑administration with potent CYP3A4 inducers (rifampicin, carbamazepine, St. John’s wort) is contraindicated because of ≥80 % reduction in trough concentrations observed in drug‑interaction trials. Concomitant use with strong CYP3A4 inhibitors such as ketoconazole or clarithromycin requires monitoring for potential lopinavir toxicity (elevated transaminases, pancreatitis) due to increased exposure. Dose adjustment in renal impairment (creatinine clearance < 30 mL/min) is not required based on negligible renal clearance of the parent compound, but the salt should be used with caution in severe hepatic impairment (Child‑Pugh class C) due to elevated exposure. Physiologically based pharmacokinetic simulations utilising measured solubility‑dissolution parameters predict an approximately 15–22 % increase in fasted‑state AUC0–∞ versus the amorphous commercial tablet; however, published head‑to‑head in vivo data for this specific salt are limited, and confirmatory fed‑fasted studies are under review.
The lopinavir pyroglutamate salt is controlled against the following pharmacopoeial and ICH limit specifications.
| Parameter | Limit | Test method |
|---|---|---|
| Assay (anhydrous basis) | 98.0–102.0 % | HPLC, USP <621> |
| Chiral purity (any diastereomer) | ≤ 0.5 % | SFC, Chiralpak IA |
| Water content (Karl Fischer) | ≤ 0.5 % | USP <921> |
| Residual solvents: acetone | ≤ 50 ppm | USP <467> Class 3 |
| Residual solvents: dichloromethane | ≤ 600 ppm | USP <467> Class 2 |
| Elemental impurities (Class 1, 2A, 2B) | According to ICH Q3D | ICP‑MS, USP <233> |
| Polymorphic identity | Conform to reference diffractogram | XRPD (Cu Kα, 2.5–40° 2θ) |
| Microbial limits | TAMC ≤ 100 CFU/g, TYMC ≤ 10 CFU/g, absent E. coli | USP <61>, <62> |