工业催化
工業催化
공업최화
INDUSTRIAL CATALYSIS
2014年
11期
865-868
,共4页
郭超%高俊斌%靳广洲%赵如松
郭超%高俊斌%靳廣洲%趙如鬆
곽초%고준빈%근엄주%조여송
催化化学%模拟汽油%α-Al2 O3%镍催化剂%二烯烃%选择性加氢
催化化學%模擬汽油%α-Al2 O3%鎳催化劑%二烯烴%選擇性加氫
최화화학%모의기유%α-Al2 O3%얼최화제%이희경%선택성가경
catalytic chemistry%simulating gasoline%α-Al2 O3%Ni-catalyst%dienes%selective hydrogenation
以微波辐射法制得的大比表面积α-Al2 O3为载体,负载一定量 NiO 制备得到 NiO/α-Al2 O3催化剂,采用固定床微反实验装置评价NiO/α-Al2 O3催化剂用于模拟汽油选择性加氢脱二烯反应的性能,并对载体和催化剂进行XRD和BET表征。结果表明,用微波辐射法制得的Al2 O3具有α-Al2 O3的物相和大比表面积,负载NiO后的NiO/α-Al2 O3催化剂对模拟汽油选择性加氢脱二烯具有较好的反应性能,适宜的NiO负载质量分数为24%。通过对反应条件的考察,得出24%NiO/α-Al2 O3催化剂的适宜反应条件为反应温度80℃,常压,空速5.5 h-1,氢油体积比100:1。
以微波輻射法製得的大比錶麵積α-Al2 O3為載體,負載一定量 NiO 製備得到 NiO/α-Al2 O3催化劑,採用固定床微反實驗裝置評價NiO/α-Al2 O3催化劑用于模擬汽油選擇性加氫脫二烯反應的性能,併對載體和催化劑進行XRD和BET錶徵。結果錶明,用微波輻射法製得的Al2 O3具有α-Al2 O3的物相和大比錶麵積,負載NiO後的NiO/α-Al2 O3催化劑對模擬汽油選擇性加氫脫二烯具有較好的反應性能,適宜的NiO負載質量分數為24%。通過對反應條件的攷察,得齣24%NiO/α-Al2 O3催化劑的適宜反應條件為反應溫度80℃,常壓,空速5.5 h-1,氫油體積比100:1。
이미파복사법제득적대비표면적α-Al2 O3위재체,부재일정량 NiO 제비득도 NiO/α-Al2 O3최화제,채용고정상미반실험장치평개NiO/α-Al2 O3최화제용우모의기유선택성가경탈이희반응적성능,병대재체화최화제진행XRD화BET표정。결과표명,용미파복사법제득적Al2 O3구유α-Al2 O3적물상화대비표면적,부재NiO후적NiO/α-Al2 O3최화제대모의기유선택성가경탈이희구유교호적반응성능,괄의적NiO부재질량분수위24%。통과대반응조건적고찰,득출24%NiO/α-Al2 O3최화제적괄의반응조건위반응온도80℃,상압,공속5.5 h-1,경유체적비100:1。
Using α-Al2 O3 carrier with large surface area prepared by microwave radiation method,NiO/α-Al2 O3 catalysts were prepared by loading a certain amount of NiO on the carrier.α-Al2 O3 Carrier and the as-prepared catalysts were characterized by XRD and BET. The performance of NiO/α-Al2 O3 catalysts for removing dienes of simulation of gasoline by selective hydrogenation were evaluated in a fixed bed con-tinuous micro-reactor device. The results showed that Al2 O3 prepared by microwave radiation method pos-sessed α-Al2 O3 phase and large surface area. NiO/α-Al2 O3 catalyst had better catalytic performance for removing the diolefins by gasoline selective hydrogenation. The optimal loading mass fraction of NiO was 24%,and the optimum reaction condition was attained as follows:reaction temperature 80℃,atmospheric pressure,space velocity 5. 5 h-1 and volume ratio of hydrogen to oil 100:1.