TY - JOUR
T1 - Effect of reaction conditions on methanol to gasoline conversion over nanocrystal ZSM-5 zeolite
AU - Wan, Zhijian
AU - Li, Gang
AU - Wang, Chuanfu
AU - Yang, Hong
AU - Zhang, Dongke
PY - 2018/9/15
Y1 - 2018/9/15
N2 - A nanocrystal ZSM-5 zeolite comprising uniform single crystal particles of ~100 nm in size was synthesised and characterised using XRD, ICP-AES, SEM, TEM, solid state MAS NMR and nitrogen physisorption techniques. The catalytic performance was tested in methanol to gasoline (MTG) conversion with a particular focus on the effect of reaction conditions, namely, temperature from 300 to 450 °C, pressure from 0.1 to 2.0 MPa and WHSV from 1 to 4 h-1. Temperature showed a significant impact. At temperatures ≤350 °C, methanol conversion did not complete while the catalyst was deactivated more rapidly. Increasing temperature to above 375 °C saw complete methanol conversion and durable catalyst activity. Further increasing the reaction temperature to above 400 °C reduced gasoline yield. Pressure mainly affected the product selectivity; a higher pressure led to a lower C1-C4 selectivity but enhanced durene formation. Further increasing pressure also favoured coke formation, leading to faster loss of catalyst activity. Likewise, increasing WHSV reduced C1-C4 selectivity but promoted the formation of durene and coke, resulting in a rapid deactivation of the catalyst. The optimal reaction conditions for this nanocrystal ZSM-5 catalyst in MTG were found to be 375 °C, 1.0 MPa and WHSV of 2 h-1.
AB - A nanocrystal ZSM-5 zeolite comprising uniform single crystal particles of ~100 nm in size was synthesised and characterised using XRD, ICP-AES, SEM, TEM, solid state MAS NMR and nitrogen physisorption techniques. The catalytic performance was tested in methanol to gasoline (MTG) conversion with a particular focus on the effect of reaction conditions, namely, temperature from 300 to 450 °C, pressure from 0.1 to 2.0 MPa and WHSV from 1 to 4 h-1. Temperature showed a significant impact. At temperatures ≤350 °C, methanol conversion did not complete while the catalyst was deactivated more rapidly. Increasing temperature to above 375 °C saw complete methanol conversion and durable catalyst activity. Further increasing the reaction temperature to above 400 °C reduced gasoline yield. Pressure mainly affected the product selectivity; a higher pressure led to a lower C1-C4 selectivity but enhanced durene formation. Further increasing pressure also favoured coke formation, leading to faster loss of catalyst activity. Likewise, increasing WHSV reduced C1-C4 selectivity but promoted the formation of durene and coke, resulting in a rapid deactivation of the catalyst. The optimal reaction conditions for this nanocrystal ZSM-5 catalyst in MTG were found to be 375 °C, 1.0 MPa and WHSV of 2 h-1.
KW - Catalyst deactivation
KW - Coke formation
KW - Methanol to gasoline
KW - Nanocrystal ZSM-5 zeolite
KW - Reaction conditions
UR - http://www.scopus.com/inward/record.url?scp=85040706349&partnerID=8YFLogxK
U2 - 10.1016/j.cattod.2018.01.017
DO - 10.1016/j.cattod.2018.01.017
M3 - Article
AN - SCOPUS:85040706349
SN - 0920-5861
VL - 314
SP - 107
EP - 113
JO - Catalysis Today
JF - Catalysis Today
ER -