Mineral evolution and porous kinetics of nitric acid pressure leaching limonitic laterite

被引:19
作者
He, Fei
Ma, Baozhong [1 ]
Wang, Chengyan [1 ]
Chen, Yongqiang
机构
[1] Univ Sci & Technol Beijing, State Key Lab Adv Met, Beijing 100083, Peoples R China
基金
中国国家自然科学基金;
关键词
Mineral evolution; Kinetic models; Porous; Laterite; Nitric acid; Nickel; FLUID-SOLID REACTIONS; NICKEL; REDUCTION; COBALT; MODEL; ORE; DISSOLUTION; CHEMISTRY; METALS;
D O I
10.1016/j.mineng.2022.107544
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Nitric acid pressure leaching (NAPL) of limonitic laterite is a recently developed technology by our group, which is in line with the concept of clean and sustainable development for the nickel industry. In this paper, an autoclave equipped with acid injection and sample withdrawal systems was used to investigate the behavior of nickel, iron, and mineral evolution during the leaching process. Afterward, a kinetic model was derived to describe the process of nickel dissolution. The results indicated that the temperature, acid concentration, and liquid-solid ratio were positively correlated with nickel extraction. Additionally, the dissolution process of goethite from a microscopic perspective was observed and confirmed, that the dissolution of goethite and the hydrolysis to produce hematite occurred simultaneously. Also, several kinetic models for characterizing the leaching of porous materials were tested. The grain model-pore diffusion control-cylindrical particle was chosen to describe nickel extraction. The kinetics equation can be summarized as X + (1 -X)ln(1 -X) = 2bF(p)(2)/3R(p)(2)rho(m)(1-epsilon)C(A,ave)D(e,A)t, with an effective diffusivity of 4.59 x 10(-10) m(2)/min at 210 degrees C. Consequently, it is concluded that the pores of goethite are the active sites and that the diffusion of the leaching agent within the pores is the controlling step of the reaction. This work serves the NAPL process for limonitic laterite and provides a foundation for more efficient extraction of nickel.
引用
收藏
页数:9
相关论文
共 44 条
[1]   Hydrometallurgical process for the separation and recovery of nickel from sulphate heap leach liquor of nickeliferrous laterite ores [J].
Agatzini-Leonardou, S. ;
Tsakiridis, P. E. ;
Oustadakis, P. ;
Karidakis, T. ;
Katsiapi, A. .
MINERALS ENGINEERING, 2009, 22 (14) :1181-1192
[2]  
BHATIA SK, 1980, AICHE J, V26, P379, DOI 10.1002/aic.690260308
[3]   E-pH diagrams for the metal-water system at 150 °C: Thermodynamic analysis and application for extraction and separation of target metals from saprolitic laterite [J].
Cao, Zhihe ;
Ma, Baozhong ;
Wang, Chengyan ;
Chen, Yongqiang ;
Liu, Bao ;
Xing, Peng ;
Zhang, Wenjuan .
MINERALS ENGINEERING, 2020, 152
[4]   EFFECTS OF PARTICLE SHAPE AND SIZE DISTRIBUTION ON THE OVERALL FLUID-SOLID REACTION RATES OF PARTICLE ASSEMBLAGES [J].
Cho, Jaehun ;
Sohn, Hong Yong .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2016, 94 (08) :1516-1523
[5]   KINETICS AND MECHANISMS OF ACID DISSOLUTION OF GOETHITE ALPHA-FEOOH) [J].
CORNELL, RM ;
POSNER, AM ;
QUIRK, JP .
JOURNAL OF INORGANIC & NUCLEAR CHEMISTRY, 1976, 38 (03) :563-567
[6]   A REACTION KINETIC-MODEL FOR THE LEACHING OF INDUSTRIAL ZINC FERRITE PARTICULATES IN SULFURIC-ACID MEDIA [J].
FILIPPOU, D ;
DEMOPOULOS, GP .
CANADIAN METALLURGICAL QUARTERLY, 1992, 31 (01) :41-54
[7]   Microwave carbothermic reduction roasting of a low grade nickeliferous silicate laterite ore [J].
Forster, J. ;
Pickles, C. A. ;
Elliott, R. .
MINERALS ENGINEERING, 2016, 88 :18-27
[8]   Effect of a thermal pretreatment on dissolution kinetics of a limonitic laterite ore in chloride media [J].
Garces-Granda, A. ;
Lapidus, G. T. ;
Restrepo-Baena, O. J. .
HYDROMETALLURGY, 2020, 196
[9]   A RANDOM CAPILLARY MODEL WITH APPLICATION TO CHAR GASIFICATION AT CHEMICALLY CONTROLLED RATES [J].
GAVALAS, GR .
AICHE JOURNAL, 1980, 26 (04) :577-585
[10]   Sulphuric acid pressure leaching of a limonitic laterite: chemistry and kinetics [J].
Georgiou, D ;
Papangelakis, VG .
HYDROMETALLURGY, 1998, 49 (1-2) :23-46