“…This non-dimensional parameter has a range of [0, 1] with respect to the inner pipe diameter 𝐷 and is hereinafter referred to as the liquid level time series at a fixed position 𝑥, denoted by ℎ 𝐿 (𝑡) (Olbrich et al, 2021a;Schmelter et al, 2021a). It reveals the dynamics of the spatial distribution of the two phases in the pipe and can therefore reliably indicate slugs, waves or other liquid structures, similarly to the hold-up parameter, see Olbrich et al (2021b). Typically, for analyses of hold-up or liquid level time series, the conventional length and time scales of slug flow are calculated by simple thresholding procedures, see Zhao et al (2015), Baba et al (2018), Schmelter et al (2021a) and Olbrich et al (2020Olbrich et al ( , 2021b and Fig.…”