中国有色金属学报(英文版)
中國有色金屬學報(英文版)
중국유색금속학보(영문판)
TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA
2014年
3期
861-867
,共7页
唐清%钟宏%王帅%李进中%刘广义
唐清%鐘宏%王帥%李進中%劉廣義
당청%종굉%왕수%리진중%류엄의
氧化锰矿%废茶叶%还原剂%浸出
氧化錳礦%廢茶葉%還原劑%浸齣
양화맹광%폐다협%환원제%침출
manganese oxide ore%waste tea%reductant%leaching
采用废茶叶在硫酸溶液中还原浸出加蓬和湘西氧化锰矿石,探索废茶叶用量、硫酸浓度、固液比、浸出温度和反应时间对浸出过程的影响。对加蓬氧化锰矿,优化的浸出条件为:氧化锰矿与废茶叶的质量比10:4、硫酸浓度2.5 mol/L、固液比7.5:1、浸出温度368 K、浸出时间8 h;在此条件下,加蓬氧化锰矿的浸出率几乎达100%。对于湘西氧化锰矿,优化浸出条件为:氧化锰矿与废茶叶的质量比10:1、硫酸浓度1.7 mol/L、液固比7.5:1、温度368 K、浸出时间8 h;在此条件下,锰的浸出率达到99.8%。氧化锰矿的还原浸出过程符合内扩散控制模型,加蓬和湘西氧化锰矿石的还原浸出反应表观活化能分别为38.2 kJ/mol和20.4 kJ/mol。采用X-射线衍射(XRD)和扫描电子显微镜(SEM)对浸出前、后的锰渣进行表征。
採用廢茶葉在硫痠溶液中還原浸齣加蓬和湘西氧化錳礦石,探索廢茶葉用量、硫痠濃度、固液比、浸齣溫度和反應時間對浸齣過程的影響。對加蓬氧化錳礦,優化的浸齣條件為:氧化錳礦與廢茶葉的質量比10:4、硫痠濃度2.5 mol/L、固液比7.5:1、浸齣溫度368 K、浸齣時間8 h;在此條件下,加蓬氧化錳礦的浸齣率幾乎達100%。對于湘西氧化錳礦,優化浸齣條件為:氧化錳礦與廢茶葉的質量比10:1、硫痠濃度1.7 mol/L、液固比7.5:1、溫度368 K、浸齣時間8 h;在此條件下,錳的浸齣率達到99.8%。氧化錳礦的還原浸齣過程符閤內擴散控製模型,加蓬和湘西氧化錳礦石的還原浸齣反應錶觀活化能分彆為38.2 kJ/mol和20.4 kJ/mol。採用X-射線衍射(XRD)和掃描電子顯微鏡(SEM)對浸齣前、後的錳渣進行錶徵。
채용폐다협재류산용액중환원침출가봉화상서양화맹광석,탐색폐다협용량、류산농도、고액비、침출온도화반응시간대침출과정적영향。대가봉양화맹광,우화적침출조건위:양화맹광여폐다협적질량비10:4、류산농도2.5 mol/L、고액비7.5:1、침출온도368 K、침출시간8 h;재차조건하,가봉양화맹광적침출솔궤호체100%。대우상서양화맹광,우화침출조건위:양화맹광여폐다협적질량비10:1、류산농도1.7 mol/L、액고비7.5:1、온도368 K、침출시간8 h;재차조건하,맹적침출솔체도99.8%。양화맹광적환원침출과정부합내확산공제모형,가봉화상서양화맹광석적환원침출반응표관활화능분별위38.2 kJ/mol화20.4 kJ/mol。채용X-사선연사(XRD)화소묘전자현미경(SEM)대침출전、후적맹사진행표정。
Manganese oxide ores from Gabon and Xiangxi were leached with waste tea as reductant in dilute sulfuric acid solution. The effects of waste tea dosage, concentration of sulfuric acid, liquid-to-solid ratio, leaching temperature and reaction time on leaching process were explored. The leaching efficiency of Gabonese manganese oxide ore reached almost 100%under the optimal condition which was determined as follows:manganese oxide ore to waste tea mass ratio of 10:1, sulfuric acid concentration of 2.5 mol/L, liquid-to-solid ratio of 7.5:1, leaching temperature of 368 K, time of 8 h. The leaching efficiency of Xiangxi manganese oxide ore reached 99.8%under the optimal condition which was determined as follows:manganese oxide ore to waste tea mass ratio of 10:1, sulfuric acid concentration of 1.7 mol/L, liquid-to-solid ratio of 7.5:1, leaching temperature of 368 K, time of 8 h. The leaching process followed the internal diffusion controlled kinetic model, and the apparent activation energies of Gabonese manganese oxide ore and Xiangxi manganese oxide ore were calculated to be 38.2 kJ/mol and 20.4 kJ/mol, respectively. The morphological changes and mineralogical forms of the ore before and after the chemical treatment were discussed with the support of XRD analysis and SEM analysis.