工业催化
工業催化
공업최화
INDUSTRIAL CATALYSIS
2015年
5期
372-377
,共6页
李先如%罗沙%顾彬%荣欣%孙承林
李先如%囉沙%顧彬%榮訢%孫承林
리선여%라사%고빈%영흔%손승림
催化化学%γ-Al2O3水热处理%PtSnK/Al2O3催化剂%丙烷脱氢
催化化學%γ-Al2O3水熱處理%PtSnK/Al2O3催化劑%丙烷脫氫
최화화학%γ-Al2O3수열처리%PtSnK/Al2O3최화제%병완탈경
catalytic chemistry%γ-Al2O3 hydrothermal treatment%PtSnK/Al2O3 catalyst%propane dehy-drogenation
采用水热处理对γ-Al2 O3载体改性,并进行XRD、N2物理吸附-脱附、热重、NH3-TPD及H2-TPR表征。结果表明,γ-Al2 O3经过“再水合-焙烧”过程,晶型变好,表面总酸量降低, Pt-Al2 O3相互作用增加,提高了PtSnK/Al2 O3催化剂的丙烷脱氢转化率、选择性及稳定性。其中,140℃处理4 h时,氧化铝负载的PtSnK催化剂表现出最优的丙烷脱氢性能,100 h内平均转化率为33.6%,平均选择性97.3%,失活参数为15.9%。
採用水熱處理對γ-Al2 O3載體改性,併進行XRD、N2物理吸附-脫附、熱重、NH3-TPD及H2-TPR錶徵。結果錶明,γ-Al2 O3經過“再水閤-焙燒”過程,晶型變好,錶麵總痠量降低, Pt-Al2 O3相互作用增加,提高瞭PtSnK/Al2 O3催化劑的丙烷脫氫轉化率、選擇性及穩定性。其中,140℃處理4 h時,氧化鋁負載的PtSnK催化劑錶現齣最優的丙烷脫氫性能,100 h內平均轉化率為33.6%,平均選擇性97.3%,失活參數為15.9%。
채용수열처리대γ-Al2 O3재체개성,병진행XRD、N2물리흡부-탈부、열중、NH3-TPD급H2-TPR표정。결과표명,γ-Al2 O3경과“재수합-배소”과정,정형변호,표면총산량강저, Pt-Al2 O3상호작용증가,제고료PtSnK/Al2 O3최화제적병완탈경전화솔、선택성급은정성。기중,140℃처리4 h시,양화려부재적PtSnK최화제표현출최우적병완탈경성능,100 h내평균전화솔위33.6%,평균선택성97.3%,실활삼수위15.9%。
γ-Al2 O3 carriers were modified by hydrothermal treatment and characterized by XRD,N2-phys-isorption,TG,NH3-TPD and H2-TPR. The results showed that the crystallinity of γ-Al2 O3 increased after rehydration-calcination process. Hydrothermal treatment decreased the total acid amount of catalyst, enhanced the interaction of Pt-Al2 O3 ,and improved the performance of PtSnK/Al2 O3 catalyst for propane dehydrogenation. When alumina support was treated at 140 ℃ for 4 h,PtSnK/Al2 O3 catalyst exhibited the optimal propane dehydrogenation performance,and its average propane conversion,average selectivity to propene and deactivation ratio were 33. 6%,97. 3% and 15. 9%,respectively,for reaction 100 h.