“…At this stage of the study, driven by our interest in process intensification by the application of flow techniques [ 76 , 77 , 78 , 79 , 80 , 81 , 82 , 83 , 84 , 85 , 86 , 87 , 88 ], we next investigated the transition of the model carbonation of styrene oxide from batch to segmented flow conditions [ 89 , 90 ]. The in-house assembled flow apparatus consisted of a 4.42 mL spiral capillary reactor (FEP tubing; 0.75 mm ID) placed inside a thermostated bath (75 °C).…”