Rare earth elements were extracted using a sulfuric acid roasting-water leaching process.The effect of acid roasting on a new type of low-grade sedimentary rare earth ore found in Guizhou Province,China was analyzed u...Rare earth elements were extracted using a sulfuric acid roasting-water leaching process.The effect of acid roasting on a new type of low-grade sedimentary rare earth ore found in Guizhou Province,China was analyzed using X-ray diffraction and scanning electron microscopy.A systematic study was conducted on process parameters such as amount of acid,roasting temperature,roasting time,water leaching temperature,and leaching time.The results reveal that the total recove ry of rare earth elements reaches 81.37%,which is 3.1 times higher than that achieved through direct acid leaching,under the optimal conditions.In addition,the leaching rate of heavy rare earth elements reaches 72.53%.Rare earth elements and some other valuable metals are transformed into soluble sulfate through the local decomposition of clay minerals under the action of the sulfuric acid attack.The dissolution rates of aluminum,iron,and titanium ions are 34.94%,17.05%,and 62.77%,respectively.The precipitation rate of Ti reaches 99%,and the loss of rare earth ions in the solution is less than 1%.Meanwhile,the results of a leaching kinetics analysis indicate that the leaching process of rare ions is controlled by diffusion.Precious metal ions such as iron and aluminum in the leaching solution can reduce the adsorption of rare earth ions by kaolinite.This study efficiently recovered rare earth ions under conditions of low calcination te mperature and direct water leaching,resulting in reduced energy consumption of the extraction process and acidity of the leaching solution.These findings provide a solid foundation for the further separation and extraction of rare earth ions.展开更多
Potassium hydroxide(KOH)was introduced into the molybdenite roasting process to convert molybdenum(Mo)and sulfur(S)into water-soluble potassium molybdate(K_(2)MoO_(4))and potassium sulfate(K_(2)SO_(4)).Roasting with a...Potassium hydroxide(KOH)was introduced into the molybdenite roasting process to convert molybdenum(Mo)and sulfur(S)into water-soluble potassium molybdate(K_(2)MoO_(4))and potassium sulfate(K_(2)SO_(4)).Roasting with a 1.8-fold excess of KOH at 400℃ for 3 h enabled the leaching of over 99%of Mo from the molybdenum calcine using water.A precipitation method involving potassium–magnesium(K-Mg)salts was proposed for impurity removal.Under the conditions of pH 11,30℃,excess coefficient of 1.7 for Mg salts,and a duration of 1 h,98.37%of phosphorus(P)was removed from the K_(2)MoO_(4) solution.With post-purification,over 99%of Mo crystallized upon adjustment of pH to 1.Subsequently,S and K were recovered as K_(2)SO_(4) fertilizer from the crystalline mother liquor.An environmentally sustainable approach was proposed to conduct molybdenite production and ensure the efficient recovery of both Mo and S.展开更多
基金supported by the Guizhou Provincial Science and Technology Program ([2022]ZD006)。
文摘Rare earth elements were extracted using a sulfuric acid roasting-water leaching process.The effect of acid roasting on a new type of low-grade sedimentary rare earth ore found in Guizhou Province,China was analyzed using X-ray diffraction and scanning electron microscopy.A systematic study was conducted on process parameters such as amount of acid,roasting temperature,roasting time,water leaching temperature,and leaching time.The results reveal that the total recove ry of rare earth elements reaches 81.37%,which is 3.1 times higher than that achieved through direct acid leaching,under the optimal conditions.In addition,the leaching rate of heavy rare earth elements reaches 72.53%.Rare earth elements and some other valuable metals are transformed into soluble sulfate through the local decomposition of clay minerals under the action of the sulfuric acid attack.The dissolution rates of aluminum,iron,and titanium ions are 34.94%,17.05%,and 62.77%,respectively.The precipitation rate of Ti reaches 99%,and the loss of rare earth ions in the solution is less than 1%.Meanwhile,the results of a leaching kinetics analysis indicate that the leaching process of rare ions is controlled by diffusion.Precious metal ions such as iron and aluminum in the leaching solution can reduce the adsorption of rare earth ions by kaolinite.This study efficiently recovered rare earth ions under conditions of low calcination te mperature and direct water leaching,resulting in reduced energy consumption of the extraction process and acidity of the leaching solution.These findings provide a solid foundation for the further separation and extraction of rare earth ions.
基金financially supported by the National Natural Science Foundation of China(No.52174340)the National Key Research and Development Project of China(No.2022YFC2904505)the Hunan FURONG Scholars Project and the Basic Science Centre of the National Natural Science Foundation of China(No.72088101)。
文摘Potassium hydroxide(KOH)was introduced into the molybdenite roasting process to convert molybdenum(Mo)and sulfur(S)into water-soluble potassium molybdate(K_(2)MoO_(4))and potassium sulfate(K_(2)SO_(4)).Roasting with a 1.8-fold excess of KOH at 400℃ for 3 h enabled the leaching of over 99%of Mo from the molybdenum calcine using water.A precipitation method involving potassium–magnesium(K-Mg)salts was proposed for impurity removal.Under the conditions of pH 11,30℃,excess coefficient of 1.7 for Mg salts,and a duration of 1 h,98.37%of phosphorus(P)was removed from the K_(2)MoO_(4) solution.With post-purification,over 99%of Mo crystallized upon adjustment of pH to 1.Subsequently,S and K were recovered as K_(2)SO_(4) fertilizer from the crystalline mother liquor.An environmentally sustainable approach was proposed to conduct molybdenite production and ensure the efficient recovery of both Mo and S.
