Mixing time for different diameters of impeller at a high solid concentration in an agitated vessel

被引:9
|
作者
Takenaka, K
Takahashi, K
Bujalski, W
Nienow, AW
Paolini, S
Paglianti, A
Etchells, AW
机构
[1] Yamagata Univ, Dept Chem & Chem Engn, Yonezawa, Yamagata 9928510, Japan
[2] Univ Birmingham, Sch Chem Engn, Birmingham B15 2TT, W Midlands, England
[3] Univ Pisa, Dipartimento Ingn Chim, I-56126 Pisa, Italy
[4] DuPont Co Inc, DuPont Engn Technol, Philadelphia, PA 19106 USA
关键词
mixing time; high solid concentration; Chemineer HE-3; impeller diameter;
D O I
10.1252/jcej.38.309
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In the previous studies, it has been found that there is a significant influence of the solids on the liquid phase mixing time at high solid concentrations. This is due to the appearance of a clear liquid layer above the cloud solid layer at a certain specific power input. The state of solids suspension and the mixing time affect the purity, productivity and selectivity of the reaction and the size distribution and morphology of the precipitation and crystallisation. Consequently, more information in these conditions is necessary in order to operate properly the reactor handling particle suspensions. In this study, the effect of D/T ratio (the ratio of impeller to tank diameter) on solid suspension and mixing time has been investigated in a stirred tank equipped with Chemineer HE-3 impeller, which is typically used for solid-liquid mixing at high solid concentrations. The maximum mixing time for the largest D/T employed in this study is the longest despite almost the same specific power input and height of interface. However, to use the large D/T has led a high degree of homogeneous suspension and fast mixing time with a small increase in power input. On the contrary, large power input is necessary to disappear the cloud layer when the small D/T is used.
引用
收藏
页码:309 / 315
页数:7
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