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机构地区:[1]大连理工大学精细化工国家重点实验室,辽宁大连116012 [2]辽宁省高校石油化工技术与装备重点实验室,辽宁大连116012
出 处:《工业催化》2009年第12期1-5,共5页Industrial Catalysis
基 金:国家自然科学基金重点基金(20333030);国家自然科学基金青年基金(20503003);国家自然科学基金(20773020);辽宁省中青年学科带头人和教育部博士点专项基金资助项目
摘 要:以硝酸铬或重铬酸钾为Cr源,采用浸溃法制备了SiO2负载的Cr基催化剂[Cr(Ⅲ)/SiO2和Cr(Ⅵ)/SiO2],并用共浸溃法制备了K2O改性的Cr(Ⅲ)/SiO2催化剂[K-Cr(Ⅲ)/SiO2]。分别以叔丁基过氧化氢和O2作氧化剂,考察了三种催化剂催化四氢萘合成α-四氢萘酮的反应性能。结果表明,以叔丁基过氧化氢作氧化剂时,Cr(Ⅲ)/SiO2表现出最高的反应活性和选择性,K-Cr(Ⅲ)/SiO2与Cr(Ⅵ)/SiO2活性相近。紫外可见漫反射光谱表征结果表明,Cr(Ⅲ)/SiO2具有最高的低价Cr物种(Cr[L])和高价Cr物种(Cr[H])比例,K2O的引入抑制了Cr[L]物种的生成。推测以叔丁基过氧化氢作氧化剂时,四氢萘氧化生成α-四氢萘醇是反应速率控制步骤,Cr[L]物种可能是催化该反应的活性中心。以O2作氧化剂时,Cr(Ⅲ)/SiO2与Cr(Ⅵ)/SiO2催化剂性能相近,说明O2在相界面传质和(或)在催化剂表面吸附可能是反应的控制步骤。SiO2 supported Cr-based catalysts were prepared by impregnation method using Cr( NO3 )3 or KECr2O2(denoted as Cr ( m )/siO2 or Cr ( Ⅵ)/SiO2, respectively) as the chromium source. For comparison, K2O modified Cr ( Ⅲ )/SiO2 ( K-Cr method. Catalytic behaviors of the three sorts of (Ⅲ)/SiO2 ) was also prepared by co-impregnation catalysts for oxidation of tetralin to α-tetralone, using tert-butyl hydroperoxide (TBHP) or O2 as the oxidants, were investigated. The results indicated that when TBHP was used as the oxidants, Cr( Ⅲ )/SiO2 exhibited the highest activity and the selectivity to ct-tetralone, while K-Cr( m )/sio2 and Cr( VI )/SiO2 exhibited similar catalytic behavior. The UV-vis results indicated that Cr( Ⅲ)/SiO2 had the highest low valence Cr species ( Cr[ L] ) to high valence Cr species (Cr[ H]) ratio, and introduction of K2O inhibited formation of Cr[ L]. It was supposed that oxidation of tetralin to α-tetralol was the rate controlling step and might be catalyzed by Cr[ L] species. Cr( Ⅲ)/SiO2 and Cr( Ⅵ )/SiO2 behaved similarly when O2 was used as the oxidant, suggesting that O2 transfer between the phase interfaces and/or adsorption of O2 over the catalysts might be the rate controlling step in this case.
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