MAXIMUM THROUGHPUT IN MULTISTAGE MIXER-SETTLER EXTRACTION COLUMN

被引:11
作者
TAKAHASHI, K
NAKASHIMA, H
NII, S
TAKEUCHI, H
机构
[1] Dept. of Chem. Eng., Nagoya Univ., Nagoya
关键词
EXTRACTION; EXTRACTION COLUMN; MAXIMUM THROUGHPUT; MULTISTAGE COLUMN; COALESCENCE OF DROP;
D O I
10.1252/kakoronbunshu.19.440
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A multistage mixer-settler extraction column, which achieved larger throughput at higher agitation rate, was developed. Each stage consisted of an upper settler chamber and a lower mixer chamber with a lifter-turbine impeller. The continuous phase was led through a downspout from the settler to the mixer of lower stage, and the dispersed phase through a riser from the settler to the mixer of upper stage. The large throughput is produced by the suction pressure with the lifter-turbine impeller, which was ascertained by the measurements of pressure in the column. The operation was stabilzed by installing a drop coalescer between the settler and the mixer, and a lattice of mesh sheet coated with PTFE gave superior performance as the coalescer.
引用
收藏
页码:440 / 445
页数:6
相关论文
共 7 条
[1]  
BAILES PJ, 1987, CHEM ENG RES DES, V65, P514
[2]  
GAUBINGER W, 1983, GER CHEM ENG, V6, P74
[3]   FLOODING, HOLDUP, AND DROP SIZE MEASUREMENTS IN A MULTISTAGE COLUMN EXTRACTOR [J].
KIROU, VI ;
TAVLARIDES, LL ;
BONNET, JC ;
TSOURIS, C .
AICHE JOURNAL, 1988, 34 (02) :283-292
[4]  
SCHEIBEL EG, 1948, CHEM ENG PROG, V44, P681
[5]  
Steiner L., 1984, AICHE S SER, V80, P130
[6]   HOLDUP OF DISPERSED PHASE IN A MIXER-SETTLER EXTRACTION COLUMN [J].
TAKAHASHI, K ;
TAKEUCHI, H .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1990, 23 (01) :12-17
[7]  
TAKAHASHI K, 1992, SOLVENT EXTRACTION 1, P1357