CONTROLLED COOLING CRYSTALLIZATION OF (NH4)2SO4 IN THE TERNARY-SYSTEM (NH4)2SO4-NH4NO3-H2O

被引:3
作者
CHOI, CS
KIM, IS
机构
[1] Department of Chemical Engineering, Sogang University, Seoul
关键词
D O I
10.1021/ie00055a026
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The maximum allowable undercoolings of ammonium sulfate in the ternary system ammonium sulfate-ammonium nitrate-water were measured. The nucleation parameters, which may be obtained from maximum allowable undercooling measurements, are shown to be dependent on the saturation temperature of the solution in the ternary system. These data were employed along with a supersaturation balance to calculate the optimum cooling curves in a batch cooling crystallizer. The results show that controlled cooling that takes into account the effect of the cooling rate on the maximum allowable undercooling improves the product crystal size distribution.
引用
收藏
页码:1588 / 1593
页数:6
相关论文
共 10 条
[1]   GROWTH-KINETICS OF (NH4)2SO4 IN THE TERNARY-SYSTEM (NH4)2SO4-NH4NO3-H2O [J].
CHOI, CS ;
KIM, IS .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (07) :1558-1562
[2]  
Griffiths H., 1925, J SOC CHEM IND LOND, V44, p7T
[3]   OPTIMAL OPERATION OF A BATCH COOLING CRYSTALLIZER [J].
JONES, AG .
CHEMICAL ENGINEERING SCIENCE, 1974, 29 (05) :1075-1087
[4]   PROGRAMMED COOLING CRYSTALLIZATION OF POTASSIUM SULFATE SOLUTIONS [J].
JONES, AG ;
MULLIN, JW .
CHEMICAL ENGINEERING SCIENCE, 1974, 29 (01) :105-118
[5]  
MULLIN JW, 1970, J APPL CHEM, V20, P367
[6]   PROGRAMMED COOLING OF BATCH CRYSTALLIZERS [J].
MULLIN, JW ;
NYVLT, J .
CHEMICAL ENGINEERING SCIENCE, 1971, 26 (03) :369-&
[7]  
MULLIN JW, 1972, CRYSTALLIZATION, P178
[8]   SOLVENT SELECTION AND BATCH CRYSTALLIZATION [J].
MYERSON, AS ;
DECKER, SE ;
FAN, WP .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1986, 25 (04) :925-929
[9]  
Nyvlt J., 1970, Journal of Crystal Growth, V6, P151, DOI 10.1016/0022-0248(70)90034-5
[10]  
NYVLT J, 1986, J CRYST GROWTH, V3, P377