Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
50599 | Catalysis Communications | 2012 | 4 Pages |
A series of boron isomorphously framework-substituted ZSM-5 (Bx–Al–ZSM-5, Si/Al = 200, B/Al = X) were synthesized and used to selectively transform methanol to propylene (MTP). The catalytic stability can be significantly influenced by B incorporation. In comparison with the conventional ZSM-5, the B1–Al–ZSM-5 catalyst afforded a 7-time-long catalytic life under a space velocity of WHSV 1.8 h− 1 (700 h for B1–Al–ZSM-5 and 100 h for ZSM-5, respectively). The enhancement of catalytic stability can be attributed to the increase of weak acid sites on the ZSM-5 catalysts.
Graphical abstractConversion of methanol (a) and selectivity of propylene (b) over zeolites B0–Al–ZSM-5 (□), B0.5–Al–ZSM-5 (■), B1–Al–ZSM-5 (▽), B2–Al–ZSM-5 (▼). Reaction conditions: WHSV = 1.8 h−1, T = 460 °C, n (CH3OH) : n (H2O) = 1 : 3, Ptotal = 1 atm.Figure optionsDownload full-size imageDownload as PowerPoint slideHighlights► ZSM-5 zeolite catalysts with tunable acidity are synthesized. ► Weak acid amount is adjusted whereas strong acid amount keeps constant. ► Acidity is tuned to improve catalytic stability and product selectivity. ► Catalytic stability is remarkably enhanced after B incorporation in MTP reaction.