[1] Chen J Q, Bozzano A, Glover B, et al. Recent advancements in ethylene and propylene production using the UOP/Hydro MTO process[J]. Catalysis Today, 2005, 106: 103-107
[2] Liu Z, Sun C, Wang G, et al. New progress in R&D of lower olefin synthesis[J]. Fuel Process Technol, 2000, 62(2/3): 161-172
[3] Valle B, Alonso A, Atutxa,et al. Effect of nickel incorporation on the acidity and stability of HZSM-5 zeolite in the MTO process[J]. Catalysis Today, 2005, 106: 118-122
[4] Firoozi M, Baghalha M, Asadi M. The effect of micro and nano particle size of H-ZSM-5 on the selectivity of MTP reaction[J]. Catalysis Communications, 2009, 12: 1 582-1 585
[5] Kaarsholm M, Joensen F, Nerlov J,et al. Phosphorous modified ZSM-5: Deactivation and product distribution of MTO[J]. Chemical Engineering Science, 2007, 18/20: 5 527-5 532
[6] Bjorgen M, Svelle S, Joensen F, et al. Conversion of methanol to hydrocarbons over zeolite H-ZSM-5 on the origin of the olefinic species[J]. Journal of Catalysis, 2007, 2: 195-207
[7] Lok B M, Messina C A. Crystalline silicoaluminophosphates: US, 4440871[P]. 1984-04-03
[8] Dubois D R, Obrzut D L, Liu J, et al. Conversion of methanol to olefins over cobalt-, manganese-and nickel-incorporated SAPO-34 molecular sieves[J]. Fuel Processing Technology, 2003, 83(1/3): 203-218
[9] Lee K Y, Chae H J, Jeong S Y, et al. Effect of crystallite size of SAPO-34 catalysts on their induction period and deactivation in methanol-to-olefin reactions[J]. Applied Catalysis A: General, 2009, 369: 60-66
[10] Lok B M, Messina C A, Patton R L, et al. Silicoaluminophosphate molecular sieves: Another new class of microporous crystalline inorganic solids[J]. J Am Chem Soc, 1984, 106: 6 092-6 093
[11] Venna S R, Carrion M A. Synthesis of SAPO-34 crystals in the presence of crystal growth inhbitors[J]. J Phys Chem B, 2008, 112(51): 16 261-16 265
|