Process engineering is based on models, which are preferably established at laboratory scale under near-service conditions. Here, for the first time, a kinetic study of the basic hydrolysis of ethyl acetate was performed with a small volume liquidliquid loop reactor satisfying these criteria. The activation energy and pre-exponential factor were determined that agreed with data from the literature. Acquired data could be successfully transferred to well-established ideal reactor models such as continuous stirred tank or plug flow reactors. It was, thus, possible to show that a simply scalable loop reactor, requiring only small amounts of substrate and producing minimum waste, can serve as a tool for kinetic studies of continuous processes.