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- W3216991710 abstract "An extensive literature review shows a lack of comprehensive research work regarding the distribution of poly-disperse solids in Newtonian and non-Newtonian fluids. In this investigation, the efficiency of a coaxial reactor (a high rotational speed central axial-flow impeller and a low speed wall-scrapping anchor impeller) in distributing the poly-disperse particles in water (Newtonian) and carboxymethyl cellulose (CMC) solutions (non-Newtonian) was assessed employing a flow-visualization methodology (electrical resistance tomography). The solids hold-up profiles were measured by making use of the tomograms. The critical rotational speed of a central stirrer in achieving the just suspension state for various operating conditions was determined via measuring the particle bed height. The extent of axial distribution of poly-disperse particles was characterized utilizing the data from tomography measurement. The effects of some key variables such as poly-disperse ratio, impeller rotational mode, and CMC loading on the distribution of poly-disperse particles in coaxial agitated systems were extensively analyzed. The capability of the coaxial impellers in distributing the poly-disperse solids in water and CMC solutions was compared to that with a traditional single agitator. Overall, an improved level of distribution of poly-disperse particles in water and CMC solutions was obtained at lower power usage employing the coaxial impellers." @default.
- W3216991710 created "2021-12-06" @default.
- W3216991710 creator A5019206894 @default.
- W3216991710 creator A5064840804 @default.
- W3216991710 date "2022-02-01" @default.
- W3216991710 modified "2023-10-14" @default.
- W3216991710 title "Using tomography to examine the distribution of poly-disperse solid particles in Newtonian and non-Newtonian fluids with the coaxial impellers" @default.
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- W3216991710 doi "https://doi.org/10.1016/j.cherd.2021.11.032" @default.
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