矿冶工程
礦冶工程
광야공정
2014年
5期
84-88
,共5页
赵昌明%宁志强%李军丽%翟玉春%李胜利
趙昌明%寧誌彊%李軍麗%翟玉春%李勝利
조창명%저지강%리군려%적옥춘%리성리
硅酸盐型红土镍矿%Ca2 SiO4%碱熔融%机理%熔出
硅痠鹽型紅土鎳礦%Ca2 SiO4%堿鎔融%機理%鎔齣
규산염형홍토얼광%Ca2 SiO4%감용융%궤리%용출
silicate-type lateritic nickel ore%Ca2 SiO4%molten alkali%mechanism%dissolution
以CaSiO3和CaO为原料,采用固相法合成Ca2 SiO4,研究其在熔融NaOH中的熔出行为。通过正交实验,优化Ca2 SiO4在熔融NaOH中的熔出反应条件,得出最佳实验条件为:反应温度600℃,反应时间180 min,碱矿比6∶1。在优化实验基础上,考察了搅拌强度、反应温度、碱矿比对熔出过程的影响,利用液?固多相收缩未反应核模型研究了体系的熔出过程动力学。结果表明:Ca2SiO4在熔融NaOH中的熔出过程受固体产物层扩散控制,表观活化能为13.08 kJ/mol,得出了450~600℃实验温度范围内熔出过程的动力学方程。
以CaSiO3和CaO為原料,採用固相法閤成Ca2 SiO4,研究其在鎔融NaOH中的鎔齣行為。通過正交實驗,優化Ca2 SiO4在鎔融NaOH中的鎔齣反應條件,得齣最佳實驗條件為:反應溫度600℃,反應時間180 min,堿礦比6∶1。在優化實驗基礎上,攷察瞭攪拌彊度、反應溫度、堿礦比對鎔齣過程的影響,利用液?固多相收縮未反應覈模型研究瞭體繫的鎔齣過程動力學。結果錶明:Ca2SiO4在鎔融NaOH中的鎔齣過程受固體產物層擴散控製,錶觀活化能為13.08 kJ/mol,得齣瞭450~600℃實驗溫度範圍內鎔齣過程的動力學方程。
이CaSiO3화CaO위원료,채용고상법합성Ca2 SiO4,연구기재용융NaOH중적용출행위。통과정교실험,우화Ca2 SiO4재용융NaOH중적용출반응조건,득출최가실험조건위:반응온도600℃,반응시간180 min,감광비6∶1。재우화실험기출상,고찰료교반강도、반응온도、감광비대용출과정적영향,이용액?고다상수축미반응핵모형연구료체계적용출과정동역학。결과표명:Ca2SiO4재용융NaOH중적용출과정수고체산물층확산공제,표관활화능위13.08 kJ/mol,득출료450~600℃실험온도범위내용출과정적동역학방정。
With CaSiO3 and CaO as raw materials, Ca2 SiO4 was prepared by solid phase extraction at high temperature. The dissolution behavior of Ca2 SiO4 in molten NaOH was discussed. By orthogonal experiment, the optimal conditions for dissolution reaction of Ca2 SiO4 in molten NaOH were investigated and obtained, including reaction at a temperature of 600 ℃ for 180 min, with liquid/solid ratio at 6∶1. Effects of stirring speed, reaction temperature and alkali?to?ore ratio on the dissolution process were investigated based on the optimal condition tests. The kinetics of dissolution procedure was studied with unreacted shrinking core model. Results showed that the dissolution of Ca2 SiO4 in molten NaOH was affected by the diffusion through the solid product layer. The apparent activation energy was calculated to be 13. 08 kJ/mol and the kinetics model at 450~600 ℃ was expressed.