de Souza Juliana M, Berton Mateo, Snead David R, McQuade D Tyler
Department of Chemical and Life Science Engineering, Virginia Commonwealth University, Richmond, Virginia 23284-3068, United States.
Departamento de Química, Universidade Federal de São Carlos, 13565-905 São Carlos-SP, Brazil.
Org Process Res Dev. 2020 Oct 16;24(10):2271-2280. doi: 10.1021/acs.oprd.0c00146. Epub 2020 May 13.
We demonstrate a continuous two-step sequence in which sulfenyl chloride is formed, trapped by vinyl acetate, and chlorinated further via a Pummerer rearrangement. These reactions produce a key intermediate in our new approach to the oxathiolane core used to prepare the antiretroviral medicines emtricitabine and lamivudine. During batch scale-up to tens of grams, we found that the sequence featured a strong exotherm and evolution of hydrogen chloride and sulfur dioxide. Keeping gaseous byproducts in solution and controlling the temperature led to better outcomes. These reactions are ideal candidates for implementation in a continuous mesoscale system for the sake of superior control. In addition, we found that fast reagent additions at controlled temperatures decreased byproduct formation. Herein we discuss the flow implementation and the final reactor design that led to a system with a 141 g/h throughput.
我们展示了一个连续的两步反应序列,其中次磺酰氯形成后被乙酸乙烯酯捕获,然后通过普默勒重排进一步氯化。这些反应在我们用于制备抗逆转录病毒药物恩曲他滨和拉米夫定的氧硫杂环戊烷核心的新方法中产生了一个关键中间体。在批量放大到几十克的过程中,我们发现该反应序列具有强烈的放热现象,并伴有氯化氢和二氧化硫的释放。将气态副产物保留在溶液中并控制温度可获得更好的结果。为了实现更好的控制,这些反应是在连续中试规模系统中实施的理想选择。此外,我们发现,在控制温度下快速添加试剂可减少副产物的形成。在此,我们讨论了流动实施和最终反应器设计,该设计导致了一个吞吐量为141 g/h的系统。