采用沉淀法制备磁性γ-Fe2O3脱硝催化剂,通过瞬态动力学方法考察NH3、O2气体浓度对催化剂选择性催化还原(SCR)脱硝率的影响,在消除内外扩散阻力基础上应用稳态动力学研究方法构建SCR脱硝本征反应动力学模型。实验结果表明:NH3能快速在...采用沉淀法制备磁性γ-Fe2O3脱硝催化剂,通过瞬态动力学方法考察NH3、O2气体浓度对催化剂选择性催化还原(SCR)脱硝率的影响,在消除内外扩散阻力基础上应用稳态动力学研究方法构建SCR脱硝本征反应动力学模型。实验结果表明:NH3能快速在催化剂表面活性位上吸附活化;NO的吸附及其活性过渡中间体的形成在SCR反应中起控制作用;O2浓度小于1%时,其浓度的提高促进了磁性γ-Fe2O3催化剂SCR反应进行;在试验条件下,磁性γ-Fe2O3催化剂的NO、NH3、O2的反应级数分别为0.41、0、0.27,但当O2浓度>1%时,其反应级数为0,研究得到磁性γ-Fe2O3催化剂SCR表观反应活化能为28.77 k J/mol。展开更多
Gold bearing pyrite leaching was conducted in H2SO4-Fe2（SO4）3 system at different reaction temperatures,with different ferric ion concentrations,sulfuric acid concentrations and stirring speeds.The leaching kinetics...Gold bearing pyrite leaching was conducted in H2SO4-Fe2（SO4）3 system at different reaction temperatures,with different ferric ion concentrations,sulfuric acid concentrations and stirring speeds.The leaching kinetics and mechanism were studied.When the temperature ranged between 30-75 °C,the pyrite leaching was mainly controlled by chemical reaction with positive correlation to the ferric ion concentration.The activation energy obtained from Arrhenius empirical formula is 51.39 k J/mol.The EDS and XPS analyses suggest that the oxidation of sulfur within pyrite is through a series of intermediate stages,and eventually is oxidized to sulphate accompanied with the formation of element sulfur.This indicates a thiosulfate oxidation pathway of the gold bearing pyrite oxidation in H2SO4-Fe2（SO4）3 system.展开更多
文摘采用沉淀法制备磁性γ-Fe2O3脱硝催化剂,通过瞬态动力学方法考察NH3、O2气体浓度对催化剂选择性催化还原(SCR)脱硝率的影响,在消除内外扩散阻力基础上应用稳态动力学研究方法构建SCR脱硝本征反应动力学模型。实验结果表明:NH3能快速在催化剂表面活性位上吸附活化;NO的吸附及其活性过渡中间体的形成在SCR反应中起控制作用;O2浓度小于1%时,其浓度的提高促进了磁性γ-Fe2O3催化剂SCR反应进行;在试验条件下,磁性γ-Fe2O3催化剂的NO、NH3、O2的反应级数分别为0.41、0、0.27,但当O2浓度>1%时,其反应级数为0,研究得到磁性γ-Fe2O3催化剂SCR表观反应活化能为28.77 k J/mol。
基金Project(51474075)supported by the National Natural Science Foundation of China
文摘Gold bearing pyrite leaching was conducted in H2SO4-Fe2（SO4）3 system at different reaction temperatures,with different ferric ion concentrations,sulfuric acid concentrations and stirring speeds.The leaching kinetics and mechanism were studied.When the temperature ranged between 30-75 °C,the pyrite leaching was mainly controlled by chemical reaction with positive correlation to the ferric ion concentration.The activation energy obtained from Arrhenius empirical formula is 51.39 k J/mol.The EDS and XPS analyses suggest that the oxidation of sulfur within pyrite is through a series of intermediate stages,and eventually is oxidized to sulphate accompanied with the formation of element sulfur.This indicates a thiosulfate oxidation pathway of the gold bearing pyrite oxidation in H2SO4-Fe2（SO4）3 system.
