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[Fine Chemicals] Summary of OPRD case studies on aromatic/heteroaromatic nitration processes

Yuki Tanaka
Published on 2026-11-12

[Fine Chemicals] Summary of OPRD case studies on aromatic/heteroaromatic nitration processes

1.2 Case summary table
No. Reference Drug/candidate Company Substrate Nitrating reagent Scale Yield
1 Marterer 2003, 7, 318 Quinoxaline intermediate Novartis 8-Methylquinoxaline H2SO4/HNO3 (65%) Pilot 77–82%
2 De Jong 2001, 5, 216 CI-972/CI-1000 Pfizer 2-Amino-6-chloropyrimidinol 90% HNO3/H2SO4 Continuous flow 82%
3 Hardouin 2019, 23, 1932 Ampakine API Oril Industrie Bromoterephthalic acid H2SO4/HNO3 Multi-kg Moderate
4 Allwein 2012, 16, 148 CEP-28122 Cephalon Xylene anisole derivative Mixed acid (blocking strategy) 31 kg Good
5 Andreozzi 2006, 10, 1199 Mesalazine intermediate Univ. Napoli Salicylic acid HNO3/AcOH Lab ~50%
6 Kowalczyk 1997, 1, 355 Roche candidate Roche Dichloroethylidenedioxybenzene HNO3/TFA Pilot 88%
7 Lu 2006, 10, 272 PNU-288038 Pfizer Morpholine-substituted benzene ring HNO3/AcOH Pilot Good
8 Hoare 2016, 20, 683 DNAM U.S. Army Melamine Ac2O/HNO3 Hundred-gram Moderate
9 Boros 2007, 11, 899 HIV integrase inhibitor GSK Pyridone 90% HNO3/TFA 0.5 kg 61%
10 Walker 2010, 14, 108 SB-406725A GSK Dichloroisoquinoline NO2BF4 30 kg Good
11 Beutner 2014, 18, 1812 BMS project intermediate BMS 4-Bromopyrrole-2-carboxylate NaNO3/SO3-Py Large batch Good
12 Pelleter 2009, 13, 698 AZ project intermediate AZ 3-Alkylpyrazole HNO3/H2SO4 100 g Good
13 Zhang 2007, 11, 861 Roche candidate Roche Methoxyphenylmorpholine HNO3 salt/H2SO4 Pilot 95%
14 Kulkarni 2008, 12, 995 Mesalazine intermediate NCL India Salicylic acid HNO3/AcOH Continuous flow 60% selectivity
15 Kulkarni 2009, 13, 999 Nitrobenzaldehyde NCL India Benzaldehyde HNO3/H2SO4 Continuous flow Good
16 Gage 2012, 16, 930 API intermediate Asymchem Substituted aminopyridine HNO3/H2SO4 100 kg 50–59%
17 Knapkiewicz 2012, 16, 1430 Hoveyda-Grubbs ligand Apeiron 2-Isopropoxybenzaldehyde Fuming HNO3 13 g/h 87% selectivity
18 Brocklehurst 2011, 15, 1447 Novartis project Novartis 8-Bromoquinolin-2-one Fuming HNO3/AcOH 97 g/h Good
19 Kockinger 2020, 24, 2217 Osimertinib AZ/Graz 4-Fluoro-2-methoxyaniline AcOH/HNO3 flow 0.46 kg/h 83%
20 Petho 2022, 26, 1223 Afigabar EGIS Fluorobenzothiophene aromatic ring Mixed acid (flow) 12 g/h 97% purity
21 Murray 2022, 26, 657 General methodology BMS Arylboronic acid Fuming HNO3 (ipso) Lab Efficient
22 Di Somma 2012, 16, 2001 Safety study Univ. Napoli Methyl benzoate HNO3/H2SO4 Lab Safety assessment
23 Lunghi 2002, 6, 926 Safety study SSC Italy Industrial nitration process Industrial mixed acid Industrial scale Safety assessment
24 Rhode-Poulenc 1998, 2, 27 Safety study Rhode-Poulenc Organic nitro compounds Not applicable Safety assessment Review
25 Hansen 2009, 13, 198 M1 agonist Eli Lilly Aminostilbenol Safe nitration method Multi-kg Good
26 Wen 2017, 21, 1843 TFMB intermediate DICP CAS Trifluoromethoxybenzene HNO3/H2SO4 Continuous flow Good
27 Yu 2013, 17, 438 Drug intermediate Zhejiang Univ p-Difluorobenzene Fuming HNO3/H2SO4 Continuous flow 98%
28 Joshi 2003, 7, 95 General method Hebrew Univ Phenols 6% HNO3/PTC Lab High selectivity

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  • Wei Zhang 2026-11-12 13:59
    Precise optimization of continuous flow parameters achieves both yield and efficiency gains. Systematic optimization of key parameters such as reaction temperature, acid dosage, and residence time determined the optimal process conditions: PPD to sulfuric acid mass ratio 1:5.5, PPD to nitric acid molar flow ratio 1:1.1, reaction temperature 40°C, residence time 290 s. Under these conditions, conversion reached over 99.5%, selectivity remained above 96.8%, and the reaction solution yield was as high as 97.5%. The reaction time was shortened from several hours in the traditional batch to less than 5 minutes, greatly improving production efficiency. Optimized workup and material recycling balance yield and greenness. Given that NPPD contains a hydroxyl group and has some water solubility, the optimal dilution and washing water amounts were selected: dilution water at 10 times the mass of PPD, washing water at 12 times the mass of PPD. This ensures full crystallization of the product while effectively removing residual acid, yielding a qualified product with purity >98%. Meanwhile, a material recycling process was developed: washing water is recovered as dilution water, and waste sulfuric acid is concentrated by distillation and reused to dissolve PPD. This operation has no significant impact on product yield or purity, greatly reducing industrial water use and waste emissions, making the process greener. The process has significant advantages and broad prospects for industrial application. Compared with the traditional batch process, the newly developed continuous flow nitration process shows comprehensive advantages: Substantially higher yield: isolated yield reaches 92.4%, 12.4% higher than the highest reported value in the literature, directly improving economic benefits. Higher reaction efficiency: residence time is only 290 s, far shorter than the 1–2 hours of the traditional process, and continuous production is possible, suitable for scale-up. Better safety: precise temperature and mass transfer control completely solves the local overheating problem of traditional batch reactions and avoids the safety risks of nitro compound decomposition and explosion. Greener: material recycling greatly reduces waste emissions, meeting modern pharmaceutical chemical manufacturing's green requirements. More controllable operation: the continuous flow system enables precise regulation of reaction parameters, higher product quality consistency, and easy automation. The research team also verified the superiority of the new process through comparative experiments. In the traditional AcOH/HNO₃ system, adjusting nitric acid concentration cannot balance nitration ability and oxidative side reactions, and the pyrimidine ring opening problem is difficult to solve. In contrast, the H₂SO₄/HNO₃ system with a low-concentration combination ensures nitration efficiency while maximally suppressing oxidative side reactions, which is the core reason for the high yield of the new process. Significance and application value. This study achieved continuous flow nitration synthesis of NPPD for the first time, providing an efficient, safe, and green new process for the industrial production of ticagrelor, improving the production efficiency and market supply capacity of this antithrombotic drug, and also providing an important technical reference for the nitration of pyrimidine compounds. The successful application of continuous flow technology in the nitration synthesis of pharmaceutical intermediates further confirms its unique advantages in solving strongly exothermic, high-risk organic reactions, and provides new ideas and examples for the continuous, green, and intelligent upgrading of the pharmaceutical chemical industry.
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