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催化氧化法合成环己酮技术研究进展 总被引:1,自引:0,他引:1
介绍了以环己烷为原料催化氧化合成环己酮的主要方法,分析了环己烷氧化采用的主要催化剂。环己烷硼酸催化氧化法和钴盐催化氧化法存在环己烷转化率低及结渣现象;分子筛催化氧化法、金属氧化物以及金属络合物仿生催化氧化法可提高环己烷转化率及醇酮选择性;金属络合物仿生催化氧化法具有良好的开发应用前景。 相似文献
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分别采用NaY分子筛、γ-氨丙基三乙氧基硅烷修饰的MCM-41分子筛固载双水杨醛缩乙二胺合钴(Cosahn)配合物,制备了固载型Cosahn/NaY、Cosalen/MCM-41催化剂.采用傅里叶变换红外光谱、热重-差热、X射线衍射、比表面积测定等方法对固载型分子筛催化剂的结构进行表征.结果表明,Cosalen已成功地进入分子筛孔道内.在以氧气为氧源的环己烷氧化反应中,Cosalen/MCM-41催化剂具有较好的活性和对环己醇、环己酮的选择性.该催化反应体系产物中环己基过氧化氢(CHHP)的量很少,表明Cosalen/MCM-41催化剂能加速CHHP的分解.在初始氧气压力0.80 MPa、温度130℃、环己烷用量30 g、Cosalen/MCM-41用量0.30 g、叔丁基过氧化氢0.10 g的条件下反应2 h,环己烷的转化率达到5.96%,醇酮选择性87.03%. 相似文献
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综述了国内外环己烷选择性氧化制醇酮催化剂的研究进展,对目前所用的环己烷氧化催化剂体系进行了总结及比较分析,结果表明,开发廉价、高效、清洁的新催化剂是今后的重点研究方向。 相似文献
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离子液体中TS-1分子筛催化环己烷氧化反应 总被引:1,自引:0,他引:1
以离子液体[emim]BF4为反应介质,叔丁基过氧化氢(TBHP)为氧化剂,TS-1分子筛为催化剂,进行了环己烷选择性氧化反应研究.考察了氧化剂与环己烷物质的量比、反应时间、反应温度及离子液体/催化剂体系循环使用对环己烷氧化反应的影响.实验结果表明,在TBHP/环己烷物质的量比为2,反应温度为90 ℃,反应时间为18 h时,环己烷的转化率为13.2%,目的产物环己酮与环己醇的选择率高达97.6%.离子液体/催化剂体系循环使用4次后环己烷的转化率及氧化产物的收率略有降低. 相似文献
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将柔软纤维与折皱钢网复合制成波纹式支撑骨架,将V-Ti基脱硝催化剂负载到波纹式支撑骨架上制成整体波纹式脱硝催化剂。介绍V-Ti基波纹式整体脱硝催化剂的主要制备工艺、优点以及国内外对V-Ti基波纹式整体脱硝催化剂的研究现状;对V-Ti基脱硝催化剂与贵金属脱硝催化剂的制造成本以及PCDDs/PCDFs催化分解效果进行对比,两者具有相同的催化分解效果,V-Ti基脱硝催化剂成本低得多;活性组分、V质量分数以及活性温度不同,V-Ti基脱硝催化剂催化分解PCDDs/PCDFs的效果也不同,催化分解率最高可达97.7%;研究者得出V-Ti基脱硝催化剂催化氧化Hg0的不同效果,介绍V-Ti基脱硝催化剂催化氧化Hg0的研究现状。 相似文献
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轻质烷烃异构化技术是提高汽油辛烷值的重要手段,是实现汽油清洁化生产的理想选择。异构化反应是微放热反应,低温更有利于异构化反应的进行,而轻质烷烃异构化技术应用生产的前提是获得高效、稳定的催化剂。综述当前工业应用的低温型异构化催化剂、中温型异构化催化剂和固体超强酸催化剂的发展现状,指出异构化催化剂今后的研究方向。低温型催化剂为贵金属卤化物无定型催化剂,具有温度低和活性高的特点,但腐蚀性强,其应用受到限制。中温型异构化催化剂多为贵金属负载分子筛型双功能催化剂,稳定性高,但反应温度高,单程异构转化率低。固体超强酸催化剂多为将贵金属负载到固体超强酸上制备得到,活性高,反应温度低,环境友好,具有较好的发展前景。 相似文献
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In this study, two spent catalysts from the 3rd and 4th fixed beds of the atmospheric residue desulfurization (ARDS) process and one spent catalyst from the H-Oil process employing the expanded bed were used as the starting material for preparation of hydroprocessing catalysts. The spent catalysts were used either in a coked or decoked form. The procedures involved pulverizing the spent catalysts before mixing, kneading and extruding with boehmite in the presence of peptizing agent such as HNO3. The hydrodesufurization (HDS) and hydrodemetallization (HDM) activities of the new catalysts were evaluated in the microreactor using the atmospheric residue derived from Kuwait crude. The new catalysts prepared from the spent catalysts used in the fixed bed reactors exhibited higher activity than that of commercial catalysts. The HDS activity of the new catalysts prepared from spent catalysts used in the ebullated bed reactor was much lower than that of the other catalysts. This was attributed to a high content of vanadium in the former spent catalyst. At the same time, the adverse effect of vanadium on HDM was much less evident. 相似文献
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介绍聚合物固载催化剂有6类,包括离子交换树脂催化剂,聚合物固载的相转移催化剂,聚合物固载的酸催化剂,聚合物固载的碱催化剂,聚合物固载的金属催化剂,聚合物固载的生物催化剂等。综述了近年来聚合物固载催化剂的研究进展。 相似文献
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Zhixin Yu Lars Erik Fareid Kjell Moljord Edd A. Blekkan John C. Walmsley De Chen 《Applied catalysis. B, Environmental》2008,84(3-4):482-489
Co, Mo, NiMo and CoMo catalysts supported on alumina, fishbone and platelet carbon nanofibers (CNFs) have been prepared. The dispersion of the oxide phases was qualitatively studied and compared using X-ray diffraction (XRD) and transmission electron microscopy (TEM). The reducibility of the catalysts was studied by temperature programmed reduction (TPR). Hydrodesulfurization (HDS) of thiophene was used as a model reaction to compare the activity of different catalysts. The activity tests showed that the alumina supported catalysts exhibited higher activity compared to the corresponding CNF supported catalysts, and the NiMo catalysts were more active than the corresponding CoMo catalysts. The thiophene HDS activity was correlated with the dispersion of the molybdenum species and the reducibility of different catalysts. Interestingly, the CNF supported Co catalysts have higher thiophene HDS activity than the CNF supported Co(Ni)Mo catalysts. 相似文献