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作 者:张光旭[1] 欧华强[1,2] 胡昌林[1] 徐文涛[1]
机构地区:[1]武汉理工大学化学工程学院,湖北武汉430070 [2]中国天辰工程有限公司,天津300400
出 处:《石油化工》2011年第5期486-491,共6页Petrochemical Technology
基 金:武汉理工大学自主创新研究基金项目(2010-ZY-HG-004)
摘 要:采用浸渍法和混烧法,以γ-Al2O3或Al-MCM-41为载体分别负载B2O3和WO3活性组分,制备了可用于环己酮催化氧化合成ε-己内酯的固体酸催化剂,通过XRD、N2吸附-脱附、SEM和TEM等技术对催化剂进行了表征,并利用ε-己内酯合成实验评价了催化剂的性能。实验结果表明,混烧法制备的B2O3/γ-Al2O3催化剂对环己酮氧化合成ε-己内酯具有较高的活性。在B2O3/γ-Al2O3催化剂用量为0.8 g,第一步反应中丙酸65.19 g、双氧水25.00 g、48.13 kPa、3 h,第二步反应中环己酮5.40 g、50℃、常压、2 h的条件下,ε-己内酯的选择性和收率分别达95.80%和85.97%。在该催化反应中,催化剂的比表面积、孔径及孔体积等结构参数对催化活性影响不大,而高温焙烧过程中B2O3进入γ-Al2O3晶相后产生的晶格缺陷是该催化剂高活性的关键。The supported B2O3 or WO3 catalysts with γ-Al2O3 or Al-MCM-41 as supports for catalytic oxidation of cyclohexanone to ε-caprolactone were prepared by impregnation and cocalcination methods separately. The catalysts were characterized by means of XRD, N2 adsorptiondesorption, SEM and TEM. Their catalytic performances in the synthesis of ε-caprolactone were investigated. The results showed that B2 O3/γ-Al2O3 catalyst prepared by co-calcination had better catalytic activity than the others. Under the conditions: in the first step reaction, catalyst dosage 0.8 g, propionic acid dosage 65.19 g, hydrogen peroxide dosage 25.00 g, pressure 48.13 kPa and time 3 h, and in the second step reaction, cyclohexanone dosage 5.40 g, temperature 50 ℃, normal pressure and time 2 h, the selectivity and the yield of ε-caprolactone could reach 95. 80% and 85. 97%, respectively. In the catalytic reaction, the effects of specific surface area, pore diameter and pore volume of the catalysts on its activity were little. The crystal defects in the B2 O3/γ-Al2O3 catalyst, which were formed due to introduction of B2O3 active constituent to γ-Al2O3 crystalline phase during the high temperature co-calcination process, were the key factor of high activity of the catalyst.
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