کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
151078 | 456461 | 2011 | 9 صفحه PDF | دانلود رایگان |

Electrical resistance tomography (ERT) was employed to study the solid–liquid mixing in a slurry reactor equipped with a top-entering axial-flow impeller. The ERT data were used to reconstruct the tomogram using the linear back projection algorithm and calculate the degree of homogeneity. In this study, the effects of the impeller speed (252–400 rpm), impeller pumping mode (downward and upward), impeller type (A310, A100, A200, A320, A315, 3AM), impeller off-bottom clearance (T/3.8–T/2.5, where T is the tank diameter), impeller diameter to tank diameter ratio (D/T = 0.29–0.47), particle size (5.2–9.1 μm), and solids concentration (15–30 wt%) on the degree of homogeneity of micron sized latex particles in a slurry reactor were explored. The results showed that the level of homogeneity in a solid–liquid mixing system improved with the increase in impeller speed. However, after achieving the maximum level of homogeneity, any further rise in the impeller speed had a detrimental effect on the level of homogeneity. A310 impeller, with D/T ratio of 0.31, demonstrated the highest level of homogeneity while the upward pumping direction was found to be more efficient than the downward one. In addition, a clearance of T/3 proved to create the highest level of homogeneity. The results also showed that a rise in the size and concentration of particles decreased the level of homogeneity. Thus, 5.2 μm latex particles with the concentration of 15 wt% demonstrated the highest level of homogeneity.
► Tomograms were utilized to measure the degree of homogeneity in a slurry reactor.
► A310 impeller demonstrated the highest level of homogeneity.
► Upward pumping direction was more efficient for the mixing of the latex particles.
► A clearance of T/3 with D/T ratio of 0.31 produced the maximum homogeneity.
► Applying the finding of this study will lead to more efficient use of power in reactors.
Journal: Chemical Engineering Journal - Volume 172, Issue 1, 1 August 2011, Pages 517–525