Hone Christopher A, Lopatka Pavol, Munday Rachel, O'Kearney-McMullan Anne, Kappe C Oliver
Center for Continuous Flow Synthesis and Processing (CCFLOW), Research Center Pharmaceutical Engineering (RCPE), Inffeldgasse 13, 8010, Graz, Austria.
Institute of Chemistry, University of Graz, NAWI Graz, Heinrichstrasse 28, A-8010, Graz, Austria.
ChemSusChem. 2019 Jan 10;12(1):326-337. doi: 10.1002/cssc.201802261. Epub 2018 Nov 13.
A continuous-flow protocol utilizing syngas (CO and H ) was developed for the palladium-catalyzed reductive carbonylation of (hetero)aryl bromides to their corresponding (hetero)aryl aldehydes. The optimization of temperature, pressure, catalyst and ligand loading, and residence time resulted in process-intensified flow conditions for the transformation. In addition, a key benefit of investigating the reaction in flow is the ability to precisely control the CO-to-H stoichiometric ratio, which was identified as having a critical influence on yield. The protocol proceeds with low catalyst and ligand loadings: palladium acetate (1 mol % or below) and cataCXium A (3 mol % or below). A variety of (hetero)aryl bromides at a 3 mmol scale were converted to their corresponding (hetero)aryl aldehydes at 12 bar pressure (CO/H =1:3) and 120 °C reaction temperature within 45 min residence time to afford products mostly in good-to-excellent yields (17 examples). In particular, a successful scale-up was achieved over 415 min operation time for the reductive carbonylation of 2-bromo-6-methoxynaphthalene to synthesize 3.8 g of 6-methoxy-2-naphthaldehyde in 85 % isolated yield. Studies were conducted to understand catalyst decomposition within the reactor by using inductively coupled plasma-mass spectrometry (ICP-MS) analysis. The palladium could easily be recovered using an aqueous nitric acid wash post reaction. Mechanistic aspects and the scope of the transformation are discussed.
开发了一种利用合成气(CO和H)的连续流动协议,用于钯催化的(杂)芳基溴化物还原羰基化反应,以生成相应的(杂)芳基醛。对温度、压力、催化剂和配体负载量以及停留时间进行优化,得到了该转化过程强化的流动条件。此外,在流动体系中研究该反应的一个关键优势是能够精确控制CO与H的化学计量比,该比例被确定对产率有至关重要的影响。该协议在低催化剂和配体负载量下进行:醋酸钯(1 mol%或更低)和cataCXium A(3 mol%或更低)。在12 bar压力(CO/H = 1:3)和120°C反应温度下,各种3 mmol规模的(杂)芳基溴化物在45分钟停留时间内转化为相应的(杂)芳基醛,产物产率大多良好至优异(17个实例)。特别是,在415分钟的操作时间内成功实现了2-溴-6-甲氧基萘还原羰基化反应的放大,以85%的分离产率合成了3.8 g的6-甲氧基-2-萘甲醛。通过电感耦合等离子体质谱(ICP-MS)分析进行了研究,以了解反应器内催化剂的分解情况。反应后使用硝酸水溶液洗涤可轻松回收钯。讨论了该转化反应的机理和范围。