采用水热法添加模板剂十六烷基三甲基溴化铵(CTAB)和配合剂柠檬酸(CA)制备了Mo VTe Nb O系列催化剂,并将其应用于丙烯一步氧化制备丙烯酸的反应.结果表明,CA的添加量对催化剂的形貌、孔结构、比表面积及催化性能具有明显的影响.当n(CA)/...采用水热法添加模板剂十六烷基三甲基溴化铵(CTAB)和配合剂柠檬酸(CA)制备了Mo VTe Nb O系列催化剂,并将其应用于丙烯一步氧化制备丙烯酸的反应.结果表明,CA的添加量对催化剂的形貌、孔结构、比表面积及催化性能具有明显的影响.当n(CA)/n(Mo)=0.36时,Mo VTe Nb O催化剂为介孔纳米催化剂,其平均孔径为4.9 nm,具有较高的比表面积(37.8 m2/g)和较小的催化剂晶粒(粒径范围为10~16 nm),与常规水热法制备的催化剂相比,Mo VTe Nb O介孔纳米催化剂的晶粒变小、催化性能得到了显著提高,丙烯一步氧化制丙烯酸的转化率可由53.9%提高至71.2%,丙烯酸收率可提高到45.8%.展开更多
A new technology was developed to recover multiple valuable elements from the spent Al2O3-based catalyst by X-ray phase analysis and exploratory experiments. The experimental results show that in the condition of roas...A new technology was developed to recover multiple valuable elements from the spent Al2O3-based catalyst by X-ray phase analysis and exploratory experiments. The experimental results show that in the condition of roasting temperature of 750℃ and roasting time of 30 min, molar ratio of Na2O to Al2O3 of 1.2, the leaching rates of alumina, vanadium and molybdenum in the spent catalyst are 97.2%, 95.8% and 98.9%, respectively. Vanadium and molybdenum in sodium aluminate solution can be recovered by precipitators A and B, and the precipitation rates of vanadium and molybdenum are 94.8% and 92.6%. Al（OH）3 was prepared from sodium aluminate solution in the carbonation decomposition process, and the purity of Al2O3 is 99.9% after calcination, the recovery of alumina reaches 90.6% in the whole process; the Ni-Co concentrate was leached by sulfuric acid, a nickel recovery of 98.2% and cobalt recovery over 98.5% can be obtained under the experimental condition of 30% H2SO4, 80℃, reaction time 4 h, mass ratio of liquid to solid 8, stirring rate 800r/min.展开更多
文摘采用水热法添加模板剂十六烷基三甲基溴化铵(CTAB)和配合剂柠檬酸(CA)制备了Mo VTe Nb O系列催化剂,并将其应用于丙烯一步氧化制备丙烯酸的反应.结果表明,CA的添加量对催化剂的形貌、孔结构、比表面积及催化性能具有明显的影响.当n(CA)/n(Mo)=0.36时,Mo VTe Nb O催化剂为介孔纳米催化剂,其平均孔径为4.9 nm,具有较高的比表面积(37.8 m2/g)和较小的催化剂晶粒(粒径范围为10~16 nm),与常规水热法制备的催化剂相比,Mo VTe Nb O介孔纳米催化剂的晶粒变小、催化性能得到了显著提高,丙烯一步氧化制丙烯酸的转化率可由53.9%提高至71.2%,丙烯酸收率可提高到45.8%.
基金Project(2003 UDBEA00C020) supported by the Collaborative Project of School and Province of Yunnan Province
文摘A new technology was developed to recover multiple valuable elements from the spent Al2O3-based catalyst by X-ray phase analysis and exploratory experiments. The experimental results show that in the condition of roasting temperature of 750℃ and roasting time of 30 min, molar ratio of Na2O to Al2O3 of 1.2, the leaching rates of alumina, vanadium and molybdenum in the spent catalyst are 97.2%, 95.8% and 98.9%, respectively. Vanadium and molybdenum in sodium aluminate solution can be recovered by precipitators A and B, and the precipitation rates of vanadium and molybdenum are 94.8% and 92.6%. Al（OH）3 was prepared from sodium aluminate solution in the carbonation decomposition process, and the purity of Al2O3 is 99.9% after calcination, the recovery of alumina reaches 90.6% in the whole process; the Ni-Co concentrate was leached by sulfuric acid, a nickel recovery of 98.2% and cobalt recovery over 98.5% can be obtained under the experimental condition of 30% H2SO4, 80℃, reaction time 4 h, mass ratio of liquid to solid 8, stirring rate 800r/min.
