石油学报(石油加工)
石油學報(石油加工)
석유학보(석유가공)
ACTA PETROLEI SINICA(PETROLEUM PROCESSING SECTION)
2010年
1期
122-126
,共5页
分子氧%分子筛载体%环己烷氧化%钴
分子氧%分子篩載體%環己烷氧化%鈷
분자양%분자사재체%배기완양화%고
oxygen%zeolite support%cyclohexane oxidation%cobalt
选用具有不同结构的分子筛Y,Beta、ZSM-5、MOR和MCM-22为载体,采用离子交换法制备了一系列负载Co分子筛催化剂,并采用XRD、UV-vis和元素分析对它们进行了表征.以O_2为氧化剂,考察了所制催化剂在液相环己烷氧化反应中的催化性能.结果表明,分子筛载体的性质对制备的负载Co催化剂在液相环己烷氧化反应中的催化性能有很大影响.在相同反应条件下,所制备的5种负载Co分子筛催化剂中,Co/Y催化环己烷氧化反应的环己醇和环己酮混合物(KA油)的选择性最高.在130℃、1.2 Mpa O_2分压下反应3 h,Co/Y催化环己烷氧化反应的转化率为15.9%,KA油的选择性为79.0%.Co/Y催化剂在所考察的反应条件下具有良好的稳定性,经重复使用5次,仍保持良好的催化性能.
選用具有不同結構的分子篩Y,Beta、ZSM-5、MOR和MCM-22為載體,採用離子交換法製備瞭一繫列負載Co分子篩催化劑,併採用XRD、UV-vis和元素分析對它們進行瞭錶徵.以O_2為氧化劑,攷察瞭所製催化劑在液相環己烷氧化反應中的催化性能.結果錶明,分子篩載體的性質對製備的負載Co催化劑在液相環己烷氧化反應中的催化性能有很大影響.在相同反應條件下,所製備的5種負載Co分子篩催化劑中,Co/Y催化環己烷氧化反應的環己醇和環己酮混閤物(KA油)的選擇性最高.在130℃、1.2 Mpa O_2分壓下反應3 h,Co/Y催化環己烷氧化反應的轉化率為15.9%,KA油的選擇性為79.0%.Co/Y催化劑在所攷察的反應條件下具有良好的穩定性,經重複使用5次,仍保持良好的催化性能.
선용구유불동결구적분자사Y,Beta、ZSM-5、MOR화MCM-22위재체,채용리자교환법제비료일계렬부재Co분자사최화제,병채용XRD、UV-vis화원소분석대타문진행료표정.이O_2위양화제,고찰료소제최화제재액상배기완양화반응중적최화성능.결과표명,분자사재체적성질대제비적부재Co최화제재액상배기완양화반응중적최화성능유흔대영향.재상동반응조건하,소제비적5충부재Co분자사최화제중,Co/Y최화배기완양화반응적배기순화배기동혼합물(KA유)적선택성최고.재130℃、1.2 Mpa O_2분압하반응3 h,Co/Y최화배기완양화반응적전화솔위15.9%,KA유적선택성위79.0%.Co/Y최화제재소고찰적반응조건하구유량호적은정성,경중복사용5차,잉보지량호적최화성능.
Y, Beta, ZSM-5, MOR, and MCM-22 zeolites, with different structures and surface characteristics, were employed as supports. A series of zeolite supported Co catalysts were prepared by ion-exchange and characterized by XRD, UV-vis and elemental analysis. The catalytic performance of the prepared catalysts in liquid-phase oxidation of cyclohexane by molecular oxygen was investigated. The results showed that the properties of zeolite supports had great influence on catalytic performance of the prepared Co supported catalysts for liquid-phase oxidation of cyclohexane. Among the prepared five zeolite supported Co catalysts, Co/Y exhibited the highest selectivity for the mixture of eyclohexanol and cyclohexanone (KA oil) in cyclohexane oxidation under identical reaction conditions. About 15.9% conversion of cyclohexane and 79.0% selectivity of KA oil could be obtained in eyclohexane oxidation catalyzed by Co/Y catalyst at 130℃ under O_2pressure of 1.2 MPa after reaction of 6 h. Under the investigated reaction conditions, Co/Y was recyclable in cyclohexane oxidation and the conversion and selectivity changed slightly after five runs.