Crystallization of calcium sulphate hemihydrate in concentrated phosphoric acid solutions

被引:26
作者
El Moussaouiti, M
Boistelle, R
Bouhaouss, A
Klein, JP
机构
[1] Univ Aix Marseille 2, Ctr Rech Mecanismes Croissance Cristalline, CRMC2, CNRS, F-13288 Marseille 09, France
[2] Univ Aix Marseille 3, Ctr Rech Mecanismes Croissance Cristalline, CRMC2, CNRS, F-13288 Marseille, France
[3] Univ Mohammed V, Fac Sci, Lab Chim Phys Gen, Rabat, Morocco
[4] Univ Lyon 1, Lab Automat & Genie Procedes, F-69622 Villeurbanne, France
[5] CPE Lyon, F-69622 Villeurbanne, France
关键词
calcium sulphate hemihydrate; crystallization; secondary nucleation;
D O I
10.1016/S1385-8947(97)00116-2
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
We aim to show the existence of agglomeration by measuring and modelling secondary nucleation and crystal growth rates of calcium sulphate hemihydrate, CaSO4-0.5 H2O, in concentrated phosphoric acid solutions, Using a batch crystallizer we measured the evolution of the population density as a function of supersaturation, H2SO4 excess and stirring rates. All experiments were carried out at 90 degrees C in solutions at 40 wt.% of P2O5, simulating the usual conditions for crystallizing hemihydrate in the industrial processes of phosphoric acid production. Nucleation and growth rates were calculated from the population number densities, using the moments analysis method. A model is presented for describing the crystallization process of hemihydrate. It is shown that secondary nucleation and growth rates are quadratic functions of supersaturation. H2SO4 concentrations affect supersaturation but at the same supersaturation the growth rates are not significantly different. Nucleation is independent of the stirring rate, whereas growth rates are slightly affected for stirring rates up to 500 rpm. Taking agglomeration into account, the moments method fits very well the experimental data. (C) 1997 Elsevier Science S.A.
引用
收藏
页码:123 / 130
页数:8
相关论文
共 22 条
[1]   CRYSTALLIZATION OF CALCIUM SULFATE FROM PHOSPHORIC ACID [J].
AMIN, AB ;
LARSON, MA .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1968, 7 (01) :133-&
[2]  
BECHMAN JR, 1987, AICHE S SERIES, V83, P85
[3]  
DAHLGREN SE, 1960, ACTA PHYS, V271, P3
[4]   WET-PROCESS PHOSPHORIC ACID - FOAM DISTRIBUTION OF SULFURIC ACID [J].
DAVENPOR.JE ;
GETSINGE.JG ;
CARROLL, F .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1965, 4 (01) :84-&
[5]   Agglomeration kinetics of calcium sulphate hemihydrate crystals in sulpho-phosphoric solutions [J].
ElMoussaouiti, M ;
Boistelle, R ;
Bouhaouss, A ;
Klein, JP .
JOURNAL OF CRYSTAL GROWTH, 1996, 169 (01) :118-123
[6]  
FROCHEN J, 1973, INF CHIMIE, V118, P105
[7]   ANALYSIS, SIMULATION, AND OPTIMIZATION OF HEMIHYDRATE PROCESS FOR PRODUCTION OF PHOSPHORIC-ACID FROM CALCAREOUS PHOSPHORITES [J].
GIOIA, F ;
MURA, G ;
VIOLA, A .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1977, 16 (03) :390-399
[8]  
GODOBOLE VV, 1980, P LECT SERIES RECENT
[9]   SOME PROBLEMS IN PARTICLE TECHNOLOGY - A STATISTICAL MECHANICAL FORMULATION [J].
HULBURT, HM ;
KATZ, S .
CHEMICAL ENGINEERING SCIENCE, 1964, 19 (08) :555-574
[10]  
JANSEN M, 1984, IND CRYSTALLIZATION, P171