现代化工
現代化工
현대화공
MODERN CHEMICAL INDUSTRY
2009年
z1期
196-199
,共4页
郭宇%张雄福%邹红叶%刘海鸥%王金渠
郭宇%張雄福%鄒紅葉%劉海鷗%王金渠
곽우%장웅복%추홍협%류해구%왕금거
无机膜%钯膜%沸石%氢气分离%化学镀
無機膜%鈀膜%沸石%氫氣分離%化學鍍
무궤막%파막%비석%경기분리%화학도
inorganic membrane%Pd membrane%zeolite%hydrogen separation%electroless plating
以大孔α-Al_2O_3陶瓷管(平均孔径为3μm)为载体,采用水热合成法在其表面形成一层纯硅沸石(Silicalite-1)修饰层,利用化学镀法在经过纯硅沸石修饰后的载体表面成功制备出致密钯复合膜,钯膜厚度约为5 μm.利用SEM对复合膜的结构和形貌进行了分析,并在350~500℃范围内对基于纯硅沸石修饰层的钯复合膜进行气体渗透测试表明,该沸石层修饰法制备的钯复合膜具有良好的氢渗透性.在500℃时,氧气渗透通量可达为0.12mol/(m~2·s),理想气体分离因子α(H_2/N_2)达到420.并对该钯膜与在载体表面直接制备的钯复合膜性能的差异进行了讨论.
以大孔α-Al_2O_3陶瓷管(平均孔徑為3μm)為載體,採用水熱閤成法在其錶麵形成一層純硅沸石(Silicalite-1)脩飾層,利用化學鍍法在經過純硅沸石脩飾後的載體錶麵成功製備齣緻密鈀複閤膜,鈀膜厚度約為5 μm.利用SEM對複閤膜的結構和形貌進行瞭分析,併在350~500℃範圍內對基于純硅沸石脩飾層的鈀複閤膜進行氣體滲透測試錶明,該沸石層脩飾法製備的鈀複閤膜具有良好的氫滲透性.在500℃時,氧氣滲透通量可達為0.12mol/(m~2·s),理想氣體分離因子α(H_2/N_2)達到420.併對該鈀膜與在載體錶麵直接製備的鈀複閤膜性能的差異進行瞭討論.
이대공α-Al_2O_3도자관(평균공경위3μm)위재체,채용수열합성법재기표면형성일층순규비석(Silicalite-1)수식층,이용화학도법재경과순규비석수식후적재체표면성공제비출치밀파복합막,파막후도약위5 μm.이용SEM대복합막적결구화형모진행료분석,병재350~500℃범위내대기우순규비석수식층적파복합막진행기체삼투측시표명,해비석층수식법제비적파복합막구유량호적경삼투성.재500℃시,양기삼투통량가체위0.12mol/(m~2·s),이상기체분리인자α(H_2/N_2)체도420.병대해파막여재재체표면직접제비적파복합막성능적차이진행료토론.
Macroporous α-Al_2O_3 tubes as supports are modified with zeolite silicalite-1 layer by hydrothermal treatment.A dense palladium membrane with thickness of around 5 μm is successfully deposited on the modified support.Comparison between palladiuin membrane prepared directly on the support and that on the modified support is carried out.In addition,the structure and morphology of palladium composite membranes are characterized by SEM.It is indicated that a dense palladium membrane can be hardly obtained on a marcroporous support directly.The gas permeation performance is tested at the temperature range of 350-500℃.At 500℃,the highest hydrogen flux of 0.12 mol·m~(-2)·s~(-1) can be obtained,correspondingly the ideal separation factor α(H_2/N_2)is up to 420.