化工学报
化工學報
화공학보
CIESC Jorunal
2015年
10期
3940-3949
,共10页
王洪华%孙丽媛%邢隆飞%张亚飞%马通%巩雁军
王洪華%孫麗媛%邢隆飛%張亞飛%馬通%鞏雁軍
왕홍화%손려원%형륭비%장아비%마통%공안군
分子筛%烷烃%催化(作用)%ZSM-5 晶粒尺寸%正庚烷%费-托石脑油%催化裂化∕裂解%低碳烯烃
分子篩%烷烴%催化(作用)%ZSM-5 晶粒呎吋%正庚烷%費-託石腦油%催化裂化∕裂解%低碳烯烴
분자사%완경%최화(작용)%ZSM-5 정립척촌%정경완%비-탁석뇌유%최화열화∕렬해%저탄희경
molecular sieves%alkane%catalysis%ZSM-5 zeolite crystal size%n-heptane%F-T naphtha%catalytic cracking%light olefins
设计合成了纳米、亚微米和微米级晶粒尺寸ZSM-5分子筛,并研究了其在两种反应温度下(510,650℃)对正庚烷催化制低碳烯烃反应行为。结果表明,在反应初始阶段,两种反应温度下晶粒尺寸对正庚烷转化率和产物选择性影响较小。但随着反应进行,纳米和亚微米ZSM-5在510℃下反应性能(低碳烯烃选择性及反应活性稳定性)相近且均高于微米ZSM-5;而650℃下,具有更短扩散路径和更大外表面积的纳米ZSM-5则体现出更高的反应性能。微米ZSM-5在两种温度下虽具有相对较高的低碳烯烃选择性,但其活性稳定性最低。进一步研究晶粒尺寸对费-托过程中石脑油催化裂解性能的影响发现,亚微米 ZSM-5表现出最高的催化反应性能,这可能与反应原料的组成及相关反应途径变化有关。
設計閤成瞭納米、亞微米和微米級晶粒呎吋ZSM-5分子篩,併研究瞭其在兩種反應溫度下(510,650℃)對正庚烷催化製低碳烯烴反應行為。結果錶明,在反應初始階段,兩種反應溫度下晶粒呎吋對正庚烷轉化率和產物選擇性影響較小。但隨著反應進行,納米和亞微米ZSM-5在510℃下反應性能(低碳烯烴選擇性及反應活性穩定性)相近且均高于微米ZSM-5;而650℃下,具有更短擴散路徑和更大外錶麵積的納米ZSM-5則體現齣更高的反應性能。微米ZSM-5在兩種溫度下雖具有相對較高的低碳烯烴選擇性,但其活性穩定性最低。進一步研究晶粒呎吋對費-託過程中石腦油催化裂解性能的影響髮現,亞微米 ZSM-5錶現齣最高的催化反應性能,這可能與反應原料的組成及相關反應途徑變化有關。
설계합성료납미、아미미화미미급정립척촌ZSM-5분자사,병연구료기재량충반응온도하(510,650℃)대정경완최화제저탄희경반응행위。결과표명,재반응초시계단,량충반응온도하정립척촌대정경완전화솔화산물선택성영향교소。단수착반응진행,납미화아미미ZSM-5재510℃하반응성능(저탄희경선택성급반응활성은정성)상근차균고우미미ZSM-5;이650℃하,구유경단확산로경화경대외표면적적납미ZSM-5칙체현출경고적반응성능。미미ZSM-5재량충온도하수구유상대교고적저탄희경선택성,단기활성은정성최저。진일보연구정립척촌대비-탁과정중석뇌유최화렬해성능적영향발현,아미미 ZSM-5표현출최고적최화반응성능,저가능여반응원료적조성급상관반응도경변화유관。
The ZSM-5 zeolites with nano, submicron and micron crystal size, denoted as N-ZSM-5, S-ZSM-5 and M-ZSM-5, respectively, were synthesizedvia hydrothermal method. The effect of crystal size on the product selectivity in catalytic cracking ofn-heptane to light olefins reaction was also studied at 510℃ and 650℃, respectively. The results showed that the crystal size of ZSM-5 zeolites had little effect on then-heptane conversion and the selectivity to olefins at the initial phase at the above two temperatures. At 510℃, however, the submicron and nanometer ZSM-5 zeolites exhibited higher and almost similar selectivity to olefins and stability of reaction activity than the micron sample along with the reaction time. Nevertheless, the N-ZSM-5 zeolite displayed the best performance of selectivity to olefins and stability of reaction activity at 650℃ due to the short diffusion path length and the large external surface area compared to the S-ZSM-5 and M-ZSM-5. The micron-sized M-ZSM-5 zeolite presented the relatively higher selectivity to olefins than the other zeolites, but it also owned the lowest stability of reaction activity at both temperatures. In the catalytic cracking reaction of F-T naphtha, the S-ZSM-5 zeolite gave the best performance of selectivity to olefins and the stability of reaction activity and it may attribute to the complex components of the naphtha materials and their various reaction paths to olefins.