Figure 35 - uploaded by Karsten A Sedmera
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Image. Example velocity profile 50 mm (1.97 inches) from the outlet. 

Image. Example velocity profile 50 mm (1.97 inches) from the outlet. 

Source publication
Technical Report
Full-text available
The current study has two objectives. The first is to evaluate Roger Kilgore’s proposed procedure, which requires conducting some of the same types of tests that were run in the previous study. The new tests conducted include a wider range of parameters, such as greater plunge-height ratios and steeper pipe slopes. Previous research was limited in...

Citations

... Flows containing surcharges below this ratio are completely mixed in a vortex whilst surcharges above present two distinct flow regimes in the same flow (Guymer et al., 2005). More recent studies have utilized submerged jet theory where the jet flow starts expanding as it proceeds towards the outlet pipe due to the through-flowing water from the inlet pipe accelerating the entrained water in the manhole causing surplus discharge to be lost (Beg et al., 2017;Kerenyi et al., 2007;Mark and Ilesanmi-Jimoh, 2016;Stovin et al., 2008;Stovin et al., 2010). Beg et al. (2017) proposed that as the jet flow reaches the entrance of the outlet pipe in circular manholes it expands and a portion hits the manhole wall at the top of the outlet, proceeding vertically upward into a dead zone at the top of the manhole (Sokáč and Velísková, 2021). ...
Article
Full-text available
The transport of microplastics within urban water systems remains poorly understood, with little prior research on their behaviour within manhole configurations. This study represents the first to measure and model the transport dynamics of microplastics within circular and square manholes under different hydraulic scenarios. The transport and fate of polyethylene (PE) was quantified and compared to solutes (Rhodamine WT dye) using energy losses, residence time distributions (RTDs), and mixing models within surcharging and overflowing manholes. The bulk mass of solute and PE concentrations followed similar flow paths across all conditions except for 17.3 ± 7.9 % of PE mass that was immobilized in a dead zone above the inlet pipe for manholes with a surcharge to pipe diameter ratio ≥2. Consequently, these microplastics only exit after a significant change in hydraulic regime occurs, causing microplastics to be at risk of being contaminated over a prolonged duration. No significant mixing differences for PE and solutes were found between manhole geometries. The deconvolution method outperformed the ADZ model with goodness of fit (Rt^2) values of 0.99 (0.60) and 1.00 (0.89) for PE and solute mixing, respectively. This establishes the deconvolution method as the most accurate and appropriate model to accurately predict microplastic mixing in manholes and urban drainage systems.