粉煤灰浓硫酸焙烧法提取Al2O3工艺中焙烧过程十分重要,研究发现适当提升硫酸浓度、酸灰质量比和温度可增大Al转化率,而延长焙烧时间影响并不显著;在硫酸浓度80%、酸灰质量比1.5：1、温度270℃和时间60 min条件下,Al转化率可达92%~95%。T...粉煤灰浓硫酸焙烧法提取Al2O3工艺中焙烧过程十分重要,研究发现适当提升硫酸浓度、酸灰质量比和温度可增大Al转化率,而延长焙烧时间影响并不显著;在硫酸浓度80%、酸灰质量比1.5：1、温度270℃和时间60 min条件下,Al转化率可达92%~95%。TG/DSC与XRD分析表明,焙烧过程反应主要分为3个阶段：80~206℃时形成中间产物Al（HSO4）3及H2O气化;206~241℃时生成Al（HSO4）3及Al2（SO4）3·H2O;241~304℃时由Al2（SO4）3·H2O和Al（HSO4）3二者分解转化成Al2（SO4）3。由Kissinger微分法与Ozawa积分法分别计算出3个阶段表观活化能后取二者平均值,分别为52.61、74.11、96.08 k J·mol-1,并获得频率因子、反应级数和动力学方程,所获结果可为粉煤灰硫酸焙烧法提取Al2O3焙烧工艺设计和过程优化提供理论参考和基础数据。展开更多
To provide a theoretical basis for a suitable process to extract gold from refractory gold concentrates, process mineralogy on the acid leaching residue of gold calcine was studied by chemical composition, X-ray diffr...To provide a theoretical basis for a suitable process to extract gold from refractory gold concentrates, process mineralogy on the acid leaching residue of gold calcine was studied by chemical composition, X-ray diffraction, scanning electron microscopy-energy spectrum, and mineral dissociation analysis. The results showed that the acid leaching residue contained Au 68.22 g/t, Ag 92.71 g/t, Fe 0.44%, As 0.10%, and S 0.55%. Gold and silver minerals existed as native gold, argentite, and proustite. Quartz, the main gangue mineral, accounted for 78.33 wt/%. The dissociation degree analysis showed that the proportions of monomer and exposed gold in acid leaching residue were 96.66 wt%. The cyanidation results showed that the cyanide gold leaching rate of acid leaching residues was close to 100 wt%. However, the maximum cyanide gold leaching rate of gold calcine was only 85.31 wt%. This suggests that acid leaching can increase the gold dissolution rate in the cyanide process.展开更多
文摘粉煤灰浓硫酸焙烧法提取Al2O3工艺中焙烧过程十分重要,研究发现适当提升硫酸浓度、酸灰质量比和温度可增大Al转化率,而延长焙烧时间影响并不显著;在硫酸浓度80%、酸灰质量比1.5：1、温度270℃和时间60 min条件下,Al转化率可达92%~95%。TG/DSC与XRD分析表明,焙烧过程反应主要分为3个阶段：80~206℃时形成中间产物Al（HSO4）3及H2O气化;206~241℃时生成Al（HSO4）3及Al2（SO4）3·H2O;241~304℃时由Al2（SO4）3·H2O和Al（HSO4）3二者分解转化成Al2（SO4）3。由Kissinger微分法与Ozawa积分法分别计算出3个阶段表观活化能后取二者平均值,分别为52.61、74.11、96.08 k J·mol-1,并获得频率因子、反应级数和动力学方程,所获结果可为粉煤灰硫酸焙烧法提取Al2O3焙烧工艺设计和过程优化提供理论参考和基础数据。
基金supported by the funding project of Xinjiang high technology research and development program(No.201515108)funding project for Xinjiang autonomous region's strategic emerging industries(No.201552)
文摘To provide a theoretical basis for a suitable process to extract gold from refractory gold concentrates, process mineralogy on the acid leaching residue of gold calcine was studied by chemical composition, X-ray diffraction, scanning electron microscopy-energy spectrum, and mineral dissociation analysis. The results showed that the acid leaching residue contained Au 68.22 g/t, Ag 92.71 g/t, Fe 0.44%, As 0.10%, and S 0.55%. Gold and silver minerals existed as native gold, argentite, and proustite. Quartz, the main gangue mineral, accounted for 78.33 wt/%. The dissociation degree analysis showed that the proportions of monomer and exposed gold in acid leaching residue were 96.66 wt%. The cyanidation results showed that the cyanide gold leaching rate of acid leaching residues was close to 100 wt%. However, the maximum cyanide gold leaching rate of gold calcine was only 85.31 wt%. This suggests that acid leaching can increase the gold dissolution rate in the cyanide process.
