Simulation of increasing of light olefins production yield from methanol using HZSM-5 zeolite catalysis

Subject Areas :

محمد رستمی زاده ^{1 *} , پیمان تقوی ² , حسین حضرتی ³

1 - استادیار، دانشکده مهندسی شیمی، دانشگاه صنعتی سهند، شهر جدید سهند، تبریز، ایران
2 - لیسانس، دانشکده مهندسی شیمی، دانشگاه صنعتی سهند، شهر جدید سهند، تبریز، ایران
3 - استادیار، دانشکده مهندسی شیمی، دانشگاه صنعتی سهند، شهر جدید سهند، تبریز، ایران

Received: 2017-12-03 Accepted : 2018-04-01 Published : 2019-02-20

Keywords: Simulation, catalyst, Olefin, Optimization. ZSM-5,

Abstract :

Light olefins (ethylene, propylene, and butylene) can be produced from methanol through non-oil route. In this study, HZSM-5 catalyst was synthesized by hydrothermal method and characterized using X-ray diffraction (XRD), Field emission scanning electron microscopy (FE-SEM), N2 adsorption-desorption (BET), Fourier transform infrared spectroscopy (FT-IR), and NH3 temperature programmed desorption (NH3-TPD) analysis. The catalysis included microsphere morphology which led to mesoporous structure formation and acceleration of diffusion. Based on characterization, the catalysis represented high crystallinity, high surface area and appropriate acidity properties. The results showed that the catalysis provided high methanol conversion (99.5%), selectivity of light olefins (82%), and long-term catalytic lifetime (72h). In order to increase the production yield, suitable reaction groups and kinetics in consistent with the catalysis performance was determined and methanol to olefin (MTO) process was simulated. The simulation results showed well agreement with the experimental data. Optimization of kinetic and operational parameters of MTO resulted in high methanol conversion and light olefins selectivity as 100 % and 94.1 %, respectively. The catalysis performance in the MTO process under the optimized operational conditions was confirmed the simulation results which indicated practicality of applied simulation and optimization

References:

[1] Tian, P.; Wei, Y.; Ye, M.; Liu, Z.; ACS Catalysis 5, 1922-1938, 2015.
[2] Rostamizadeh, M.; Taeb, A.; Journal of Industrial and Engineering Chemistry 27, 297-306, 2015.
[3] Wang, Y.; Ma, J.; Ren, F; Du, J.; Li, R.; Microporous and Mesoporous Materials 240, 22-30, 2017.
[4] Sedighi, M.; Ghasemi, M.; Sadeqzadeh, M.; Hadi, M.; Powder Technology 291, 131-139, 2016.
[5] Wei, R.; Li, C.; Yang, C., Shan, H., Journal of Natural Gas Chemistry, 20, 261-265, 2011.
[6] Rostamizadeh, M.; Yaripour, F.; Journal of the Taiwan Institute of Chemical Engineers 71, 454-463, 2017.
[7] Freiding, J.; Kraushaar-Czarnetzki, B.; Applied Catalysis A: General 391, 254-260, 2011.
[8] Sun, C.; Du, J.; Liu, J.; Yang, Y.; Ren, N.; Shen, W.; Xu, H.; Tang, Y.; Chemical Communications 46, 2671-2673, 2010.
[9] Rostamizadeh, M.; Taeb, A.; Synthesis and Reactivity in Inorganic, Metal-Organic, and Nano-Metal Chemistry 46, 665-671, 2016.
[10] Rostami, R.B.; Lemraski, A.S.; Ghavipour, M.; Behbahani, R.M.; Shahraki, B.H.; Hamule, T.;, Chemical Engineering Research and Design 106, 347-355, 2016.
[11] Sedighi, M.; Bahrami, H.; Towfighi, J.; Journal of Industrial and Engineering Chemistry 20, 3108-3114, 2014.
[12] Hadi, N.; Niaei, A.; Nabavi, S.R.; Farzi, A.; Shirazi, M.N.; Chemical and Biochemical Engineering Quarterly 28, 53-63, 2014.
[13] Chen, L.; Zhu, S.Y.; Wang, Y.M.; He, M.Y.; New Journal of Chemistry 34, 2328-2334, 2010.
[14] Rostamizadeh, M.; Yaripour, F.; Fuel 181, 537-546, 2016.
[15] Gil, B.; Mokrzycki, Ł.; Sulikowski, B.; Olejniczak, Z.; Walas, S.; Catalysis Today 152, 24-32, 2010.
[16] O'Malley, A.J.; Parker, S.F.; Chutia, A.; Farrow, M.R.; Silverwood, I.P; Garcia-Sakai, V.; Catlow, C.R.A.; Chemical Communications 52, 2897-2900, 2016.
[17] Campbell, S.M.; Jiang, X.Z.;Howe, R.F.; Microporous and Mesoporous Materials 29, 91-108, 1999.
[18] Phung, T.K.; Radikapratama, R.; Garbarino, G.; Lagazzo, A.; Riani, P.; Busca, G.; Fuel Processing Technology 137, 290-297, 2015.
[19] Yaripour, F.; Shariatinia, Z.; Sahebdelfar, S.; Irandoukht, A.; Microporous and Mesoporous Materials 203, 41-53, 2015.
[20] Hosseininejad, S.; Afacan, A.; Hayes, R.E.; Chemical Engineering Research and Design 90, 825-833, 2012.
[21] Xu, A.; Ma, H.; Zhang, H.;Ying, W.; Fang, D.; Polish Journal of Chemical Technology 15, 95-101, 2013.
[22] Bleken, F.L.; Barbera, K.; Bonino, F.; Olsbye, U.; Lillerud, K.P.; Bordiga, S.; Beato, P.; Janssens, T.V.W.; Svelle, S.; Journal of Catalysis 307, 62-73, 2013.
[23] Bjorgen, M.; Svelle, S.; Joensen, F.; Nerlov, J.; Kolboe, S.; Bonino, F.; Palumbo, L.; Bordiga, S.; Olsbye, U.; Journal of Catalysis 249, 195-207, 2007.
[24] Svelle, S.; Olsbye, U.; Joensen, F.; Bjørgen, M.; The Journal of Physical Chemistry C 111, 17981-17984, 2007.
[25] Gayubo, A.G.; Aguayo, A.T.; Alonso, A.; Atutxa, A.; Bilbao, J.; Catalysis Today 106, 112-117, 2005.
[26] Soltanali, S.; Halladj, R.; Rashidi, A.M.; Bazmi, M.; Bahadoran, F.; Chemical Engineering Research and Design 106, 33-42, 2016.
[27] Ying, L.; Yuan, X.; Ye, M.; Cheng, Y.; Li, X.; Liu, Z; Chemical Engineering Research and Design 100, 179-191, 2015.

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