工业催化
工業催化
공업최화
INDUSTRIAL CATALYSIS
2014年
8期
609-613
,共5页
李季伟%姚志龙%李梦晨%孙培永%张胜红
李季偉%姚誌龍%李夢晨%孫培永%張勝紅
리계위%요지룡%리몽신%손배영%장성홍
催化化学%Y 型分子筛%稀土改性%重整芳烃%烯烃脱除%溴指数
催化化學%Y 型分子篩%稀土改性%重整芳烴%烯烴脫除%溴指數
최화화학%Y 형분자사%희토개성%중정방경%희경탈제%추지수
catalytic chemistry%Y zeolite%rare earth modification%reforming aromatics%olefin removal%bromine index
研究以 NaY 分子筛粉与 Al2 O3混合成型后离子交换,引入 AlF3和少量稀土(La、Ce)增加催化剂的酸性以提高脱烯烃性能,制备出简单高效的非临氢芳烃脱烯烃催化剂。采用 NH3- TPD、XRF、Py - IR 和 XRD 对催化剂进行表征,结果表明,引入 AlF3后,催化剂的总酸量增加和 L 酸酸量增加,B 酸酸量减少;引入适量 La 和 Ce 组分后,催化剂上中强酸量和 B 酸酸量增加。以 La 和 Ce改性的催化剂对溴指数540.0 mg·(100g 油)-1的原料脱烯烃,产品分布基本无变化,溴指数约稳定在9.0 mg·(100g 油)-1。改性催化剂总酸量多、合适中强酸量以及适当提高 B 酸酸量有利于催化剂脱烯烃性能。
研究以 NaY 分子篩粉與 Al2 O3混閤成型後離子交換,引入 AlF3和少量稀土(La、Ce)增加催化劑的痠性以提高脫烯烴性能,製備齣簡單高效的非臨氫芳烴脫烯烴催化劑。採用 NH3- TPD、XRF、Py - IR 和 XRD 對催化劑進行錶徵,結果錶明,引入 AlF3後,催化劑的總痠量增加和 L 痠痠量增加,B 痠痠量減少;引入適量 La 和 Ce 組分後,催化劑上中彊痠量和 B 痠痠量增加。以 La 和 Ce改性的催化劑對溴指數540.0 mg·(100g 油)-1的原料脫烯烴,產品分佈基本無變化,溴指數約穩定在9.0 mg·(100g 油)-1。改性催化劑總痠量多、閤適中彊痠量以及適噹提高 B 痠痠量有利于催化劑脫烯烴性能。
연구이 NaY 분자사분여 Al2 O3혼합성형후리자교환,인입 AlF3화소량희토(La、Ce)증가최화제적산성이제고탈희경성능,제비출간단고효적비림경방경탈희경최화제。채용 NH3- TPD、XRF、Py - IR 화 XRD 대최화제진행표정,결과표명,인입 AlF3후,최화제적총산량증가화 L 산산량증가,B 산산량감소;인입괄량 La 화 Ce 조분후,최화제상중강산량화 B 산산량증가。이 La 화 Ce개성적최화제대추지수540.0 mg·(100g 유)-1적원료탈희경,산품분포기본무변화,추지수약은정재9.0 mg·(100g 유)-1。개성최화제총산량다、합괄중강산량이급괄당제고 B 산산량유리우최화제탈희경성능。
Using NaY zeolite as the main active component and alumina as the binder,and introducing AlF3 and rare earth(La,Ce)to improve the acid amount of the catalysts,the catalysts for removing olefins in aromatics without the presence of hydrogen was prepared. The catalysts were characterized by NH3-TPD,XRF,Py-IR and XRD. The results showed that the total acid amount and the amount of Lewis acid of the catalyst were increased,and the amount of Brnsted acid were reduced by adding AlF3;the amount of medium strong acid and Brnsted acid of the catalysts were enhanced by introducing 0. 539% La2 O3 and 0.539%CeO2. The catalysts modified by La and Ce had the best effect of removing olefins in aromatics with bromine index of 540.0 mg·(100g-oil)-1. The bromine index could stabilize at 9. 0 mg·(100g-oil)-1 ,and the distribution of products was unchanged. The modified catalyst with more total amount of acid,suitable amount of mediumstrong acid and Brnsted acid had good performance for the removal of olefins in aromatics.