燃料化学学报
燃料化學學報
연료화학학보
JOURNAL OF FUEL CHEMISTRY AND TECHNOLOGY
2014年
12期
1485-1492
,共8页
宋华%高慧杰%宋华林%崔雪涵%万霞%苑丹丹
宋華%高慧傑%宋華林%崔雪涵%萬霞%苑丹丹
송화%고혜걸%송화림%최설함%만하%원단단
Cu(I)-Ce(IV)-Y%制备%苯并噻吩%吸附脱硫
Cu(I)-Ce(IV)-Y%製備%苯併噻吩%吸附脫硫
Cu(I)-Ce(IV)-Y%제비%분병새분%흡부탈류
Cu( I)-Ce( IV)-Y%preparation%benzothiophene%adsorptive desulfurization
采用液相离子交换Cu、Ce离子制备了Cu( I)-Y、Ce( IV)-Y和Cu( I)-Ce( IV)-Y吸附剂,利用XRD、BET等技术对吸附剂进行了表征。通过静态实验考察了制备条件对Cu( I)-Ce( IV)-Y吸附剂脱硫性能的影响,通过固定床实验研究了吸附剂的穿透硫容,同时,在含噻吩与苯并噻吩的正辛烷模拟油中,分别加入甲苯、环己烯、吡啶配成新的模拟油,探究了吸附剂的脱硫选择性。结果表明,离子交换时间48 h,焙烧温度550℃,Cu/Ce物质的量比1∶1下制备的Cu( I)-Ce( IV)-Y吸附剂具有适宜的脱硫活性。在含甲苯、环己烯模拟油中,Cu( I)-Ce( IV)-Y吸附剂具有最好的脱硫性能,相同浓度的甲苯、环己烯和吡啶对各吸附剂脱硫性能的影响顺序为吡啶>环己烯>甲苯。引入Cu+可改善吸附剂的脱硫活性,引入Ce4+可改善吸附剂对硫化物的选择性,Cu+和Ce4+的协同作用使Cu( I)-Ce( IV)-Y兼具有高的硫容和抗芳烃、烯烃能力。
採用液相離子交換Cu、Ce離子製備瞭Cu( I)-Y、Ce( IV)-Y和Cu( I)-Ce( IV)-Y吸附劑,利用XRD、BET等技術對吸附劑進行瞭錶徵。通過靜態實驗攷察瞭製備條件對Cu( I)-Ce( IV)-Y吸附劑脫硫性能的影響,通過固定床實驗研究瞭吸附劑的穿透硫容,同時,在含噻吩與苯併噻吩的正辛烷模擬油中,分彆加入甲苯、環己烯、吡啶配成新的模擬油,探究瞭吸附劑的脫硫選擇性。結果錶明,離子交換時間48 h,焙燒溫度550℃,Cu/Ce物質的量比1∶1下製備的Cu( I)-Ce( IV)-Y吸附劑具有適宜的脫硫活性。在含甲苯、環己烯模擬油中,Cu( I)-Ce( IV)-Y吸附劑具有最好的脫硫性能,相同濃度的甲苯、環己烯和吡啶對各吸附劑脫硫性能的影響順序為吡啶>環己烯>甲苯。引入Cu+可改善吸附劑的脫硫活性,引入Ce4+可改善吸附劑對硫化物的選擇性,Cu+和Ce4+的協同作用使Cu( I)-Ce( IV)-Y兼具有高的硫容和抗芳烴、烯烴能力。
채용액상리자교환Cu、Ce리자제비료Cu( I)-Y、Ce( IV)-Y화Cu( I)-Ce( IV)-Y흡부제,이용XRD、BET등기술대흡부제진행료표정。통과정태실험고찰료제비조건대Cu( I)-Ce( IV)-Y흡부제탈류성능적영향,통과고정상실험연구료흡부제적천투류용,동시,재함새분여분병새분적정신완모의유중,분별가입갑분、배기희、필정배성신적모의유,탐구료흡부제적탈류선택성。결과표명,리자교환시간48 h,배소온도550℃,Cu/Ce물질적량비1∶1하제비적Cu( I)-Ce( IV)-Y흡부제구유괄의적탈류활성。재함갑분、배기희모의유중,Cu( I)-Ce( IV)-Y흡부제구유최호적탈류성능,상동농도적갑분、배기희화필정대각흡부제탈류성능적영향순서위필정>배기희>갑분。인입Cu+가개선흡부제적탈류활성,인입Ce4+가개선흡부제대류화물적선택성,Cu+화Ce4+적협동작용사Cu( I)-Ce( IV)-Y겸구유고적류용화항방경、희경능력。
Cu( I) Y, Ce( IV)-Y an d Cu( I)-Ce( IV)-Y adsorbents were successfully prepared by liquid-phsa e ion-exchange of Y zeolites with combined Cu and Ce ions.The adsorbents were characterized by means of X-ray d iffratc ion ( XRD ) andN 2-adsorption specific surface area measurements ( BET ) .The effect ofp reparation oc nditoi ns on the adsopr tive desulfurization properties over Cu ( I )-Ce (I V )-Y were studied by a static ed sulfurization method.The breakthrough suluf r capacities fo the da sorbents weer stud ide in a fiex d-bde reactor system.Meanwhile, adsorptive desulfurization selectivities of the adsorbents were studied through model fuels, which made up of 1-octane solution of benzot hiophene and thiophene, then respectively mixed with a certain amount of toluene, cyclohexene or pyridine.The results indicate that the optimum preparation conditions of Cu(I)-Ce(IV)-Y is ion-exchange time of 48 h, Cu/Ce molar ratio of 1, and calcination temperature of 550℃. Cu( I)-Ce( IV)-Y adsorbent exhibited the best desulfurization performance with model fuels, which contain a certain amount of toluene and cyclohexene.The effect of toluene, cyclohexene and pyridine at the same concentration, on the metal ion-exchanged Y zeolites for sulfur removal is in the order:pyridine>cyclohexene>toluene.The introduction of Cu+can improve the desulfurization activity of adsorbent, while the introduction of Ce4+can improve the selectivity of adsorbent.The synergistic effect of Cu+and Ce4+contribute to Cu ( I)-Ce ( IV)-Y not only has the high sulfur adsorption capacity but also has the ability of resistance to aromatics and olefins.