工业催化
工業催化
공업최화
INDUSTRIAL CATALYSIS
2014年
12期
915-921
,共7页
李淑娟%袁桂梅%薛扬%吴韬%陈胜利%王桂敏
李淑娟%袁桂梅%薛颺%吳韜%陳勝利%王桂敏
리숙연%원계매%설양%오도%진성리%왕계민
催化剂工程%硅源%ZSM-5分子筛%水热处理%低碳烯烃%催化裂解
催化劑工程%硅源%ZSM-5分子篩%水熱處理%低碳烯烴%催化裂解
최화제공정%규원%ZSM-5분자사%수열처리%저탄희경%최화렬해
catalyst engineering%silicon source%ZSM-5 zeolites%hydrothermal treatment%light olefin%catalytic cracking
为了考察硅源对ZSM-5分子筛合成和催化性能的影响,分别采用白炭黑、硅胶、硅溶胶和单分散SiO2为硅源合成ZSM-5分子筛,对合成的ZSM-5分子筛进行XRD、SEM、BET和NH3-TPD表征,并以C4烯烃为原料评价合成的ZSM-5分子筛的催化裂解性能。结果表明,以硅溶胶为硅源合成的ZSM-5分子筛具有较好的结晶度和催化活性。水热处理使分子筛酸量减少,孔容缩小,改善了分子筛的乙烯丙烯选择性。经600℃水热处理4 h的ZSM-5分子筛在常压、580℃和空速9 h-1反应条件下,丁烯催化裂解为乙烯和丙烯平均转化率为90.2%,乙烯和丙烯总收率达61.1%。
為瞭攷察硅源對ZSM-5分子篩閤成和催化性能的影響,分彆採用白炭黑、硅膠、硅溶膠和單分散SiO2為硅源閤成ZSM-5分子篩,對閤成的ZSM-5分子篩進行XRD、SEM、BET和NH3-TPD錶徵,併以C4烯烴為原料評價閤成的ZSM-5分子篩的催化裂解性能。結果錶明,以硅溶膠為硅源閤成的ZSM-5分子篩具有較好的結晶度和催化活性。水熱處理使分子篩痠量減少,孔容縮小,改善瞭分子篩的乙烯丙烯選擇性。經600℃水熱處理4 h的ZSM-5分子篩在常壓、580℃和空速9 h-1反應條件下,丁烯催化裂解為乙烯和丙烯平均轉化率為90.2%,乙烯和丙烯總收率達61.1%。
위료고찰규원대ZSM-5분자사합성화최화성능적영향,분별채용백탄흑、규효、규용효화단분산SiO2위규원합성ZSM-5분자사,대합성적ZSM-5분자사진행XRD、SEM、BET화NH3-TPD표정,병이C4희경위원료평개합성적ZSM-5분자사적최화렬해성능。결과표명,이규용효위규원합성적ZSM-5분자사구유교호적결정도화최화활성。수열처리사분자사산량감소,공용축소,개선료분자사적을희병희선택성。경600℃수열처리4 h적ZSM-5분자사재상압、580℃화공속9 h-1반응조건하,정희최화렬해위을희화병희평균전화솔위90.2%,을희화병희총수솔체61.1%。
ZSM-5 zeolites were synthesized by using fumed-silica,silica gel,silica sol and monodisperse silica as silicon sources,respectively. The influence of silicon sources on synthesis and catalytic properties of ZSM-5 zeolites was investigated. The as-synthesized zeolites were characterized by XRD,SEM,BET and NH3-TPD,and their catalytic performance was evaluated by cracking of butene. The results indicated that the zeolite prepared with silica sol as silicon source exhibited higher relative crystallinity and better catalytic performance than other three zeolites. The hydrothermal treatment made the acid amount and pore volume of ZSM-5 zeolites decrease,which was favorable to the improvement of the selectivity to ethene and propene. Under the reaction condition of atmospheric pressure,580 ℃ and WHSV 9 h-1 ,the conversion of butene was 90 . 2% and the total yield of ethene and propene was 61 . 1% over ZSM-5 zeolite treated by stream at 600 ℃ for 4 h.