共查询到15条相似文献,搜索用时 484 毫秒
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以凹凸棒粘土(AT)为载体,钨酸铵为钨源,通过浸渍法制备了WO3/AT催化剂,采用FT-IR和XRD对其进行了表征,其后以30%(质量分数)H2O2为氧源、叔丁醇(TBA)为溶剂研究了其在环戊烯(CPE)环氧化反应中的催化性能。试验结果表明,WO3均匀地分散于凹凸棒粘土载体表面;在V[30%(质量分数)H2O2]/V(CPE)=2.2,V(TBA)/V(CPE)=10的条件下,环氧化反应的适宜工艺条件为:反应温度为308 K、反应时间为24 h、催化剂用量为0.3 g/mL(CPE)、WO3负载量为40.0%(质量分数)、催化剂焙烧温度为823 K和焙烧时间为2 h,在此条件下,环戊烯环氧化物(CPO)的收率为40.2%,CPE的转化率为92.1%。该催化剂对CPE的环氧化反应展现了较好的催化活性。 相似文献
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以钨酸钠为钨源,凹凸棒粘土(AT)为载体,采用浸渍法制备了凹凸棒粘土负载WO_3(WO_3/AT)催化剂,采用FT-IR和XRD对其进行了表征。以30%H_2O_2为氧源,叔丁醇为溶剂,研究了凹凸棒粘土负载WO_3在环戊烯环氧化反应中的催化性能。结果表明,WO_3与凹凸棒粘土载体中的金属离子(Mg~(2+)、Al~(3+)和Fe~(3+))之间有强的相互作用,形成了M~+—O—W键。反应的最佳工艺条件为:反应温度308 K,反应时间24 h,催化剂用量1.5 g,WO_3负载质量分数40%,催化剂焙烧温度823 K,焙烧时间3 h。在此条件下,环戊烯环氧化物收率为42.2%,环戊烯转化率为96.3%。 相似文献
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环戊烯催化氧化合成戊二醛及其动力学 总被引:6,自引:0,他引:6
对在非水溶剂存在下过氧化氢一步催化氧化环戊烯制备戊二醛过程中的催化体系进行了研究。考察了具有脱水功能的B2O3的作用及用量,确立了具有优良催化性能的催化体系WO3-B2O3;实验测定了反应动力学数据,采用非线性回归Powel共扼法求得了反应动力学方程。在推荐的催化剂体系和工艺条件下,环戊烯转化率67%,戊二醛收率63%,选择性91%。 相似文献
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微波促进环戊烯氧化合成戊二酸 总被引:1,自引:0,他引:1
以质量分数为30%的H2O2作氧化剂,磷钨酸作催化剂,通过均匀实验,考察了微波条件下环戊烯催化氧化合成戊二酸的活性。结果表明,在微波条件下,磷钨酸在环戊烯氧化合成戊二酸的过程中显示了较高的催化活性,最佳反应条件为:n(环戊烯):一(磷钨酸):n(30%H2O2)=56.5:0.3:227.9,先在75℃条件下回流反应1h,然后在微波条件400W,90℃,反应50min,戊二酸的收率可达61.37%。此外,还研究了磷钨酸盐催化环戊烯氧化合成戊二酸的活性。 相似文献
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醋酸钯/酞菁铁催化氧化环戊烯合成环戊酮的研究 总被引:6,自引:1,他引:5
在乙腈的酸性水溶液中 ,考察了 Pd Ac2 (醋酸钯 ) /Fe Pc(酞菁铁 )催化氧化环戊烯合成环戊酮的催化活性 ,讨论了影响该反应活性的因素及其反应机理。实验结果表明 ,该催化体系对环戊烯的羰基化显示出较高的催化活性 ,反应 1 0 min,反应的平均吸氧速率为 4.2 5× 1 0 -2 mmol/min,环戊酮的收率可达 83%。在乙醇的酸性水溶液中 ,Pd Ac2 /BQ(苯醌 ) /Fe Pc催化环戊烯氧化合成环戊酮的活性高于 Pd Ac2 /Fe Pc的活性 ,反应的平均吸氧速率分别为 1 .45× 1 0 -2 mmol/min,9.0×1 0 -3 mmol/mi 相似文献
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Tungsten-containing hexagonal mesoporous silica (W-HMS) supported tungsten oxide catalysts (WOx/W-HMS) was prepared for the selective oxidation of cyclopentene with aqueous hydrogen peroxide to glutaraldehyde. X-ray diffraction (XRD) results indicated that the crystal form of the active phase (tungsten oxide) of the WOx/W-HMS catalysts was dependent on the W loading and calcination temperature. X-ray photoelectron spec- troscopy (XPS) analysis revealed that the dispersed tungsten oxides on the surface of W-HMS support consisted of a mixture of W(V) and W(VI). It was found that a high content of amorphous W species in (5+) oxidation state resuited in the high catalytic activity. When the W loading was up to 12% (by mass) or the catalyst precursor was treated at temperature of 623 K, the catalytic activity decreased due to the presence of WO3 crystallites and the oxidation of W(V) to W(VI) on the catalyst surface. Furthermore, NH3-temperature-programmed-desorption (NH3-TPD) analysis showed that the effects of W loading and calcination temperature on the acidity of the catalysts were related to the catalytic activity. A high selectivity of 80.2% for glutaraldehyde with a complete conversion of cyclopentene was obtained over 8%WOx/W-HMS catalyst calcined at 573 K after 14 h of reaction. 相似文献
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Jinjuan Xue Hengbo Yin Haixia Li Dongzhi Zhang Tingshun Jiang Longbao Yu Yutang Shen 《Korean Journal of Chemical Engineering》2009,26(3):654-659
A series of Keggin type tungsten-substituted molybdophosphoric acids (H3PMo12−n
W
n
O40·XH2O) were synthesized and characterized by ICP-AES, FT-IR, TG-DSC, and XRD. The tungsten substitution extent significantly affected
their catalytic activity in the oxidation of cyclopentene and the selectivity of the resultant products. The tungsten-substituted
molybdophosphoric acids with tungsten substitution numbers in a range of 3–6.8 exhibited high catalytic activity in the oxidation
of cyclopentene. After reaction for 8 h, the conversion of cyclopentene was up to 97%; the oxidation products mainly consisted
of glutaraldehyde, cis-1,2-cyclopentanediol and trans-1,2-cyclopentanediol with the yields of ca. 23%, 27%, and 45%, respectively. 相似文献
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