مرکز اطلاعات علمی Scientific Information Database (SID) - Trusted Source for Research and Academic Resources

Persian Verion

Scientific Information Database (SID) - Trusted Source for Research and Academic Resources

video

Scientific Information Database (SID) - Trusted Source for Research and Academic Resources

sound

Scientific Information Database (SID) - Trusted Source for Research and Academic Resources

Persian Version

Scientific Information Database (SID) - Trusted Source for Research and Academic Resources

View:

801
Scientific Information Database (SID) - Trusted Source for Research and Academic Resources

Download:

0
Scientific Information Database (SID) - Trusted Source for Research and Academic Resources

Cites:

Information Journal Paper

Title

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

Pages

  77-87

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.

Cites

  • No record.
  • References

  • No record.
  • Cite

    APA: Copy

    ROSTAMIZADEH, MOHAMMAD, Taghavi, Peyman, & HAZRATI, HOSSEIN. (2019). Simulation of increasing of light olefins production yield from methanol using HZSM-5 zeolite catalysis. JOURNAL OF APPLIED RESEARCHES IN CHEMISTRY (JARC), 12(4 ), 77-87. SID. https://sid.ir/paper/180219/en

    Vancouver: Copy

    ROSTAMIZADEH MOHAMMAD, Taghavi Peyman, HAZRATI HOSSEIN. Simulation of increasing of light olefins production yield from methanol using HZSM-5 zeolite catalysis. JOURNAL OF APPLIED RESEARCHES IN CHEMISTRY (JARC)[Internet]. 2019;12(4 ):77-87. Available from: https://sid.ir/paper/180219/en

    IEEE: Copy

    MOHAMMAD ROSTAMIZADEH, Peyman Taghavi, and HOSSEIN HAZRATI, “Simulation of increasing of light olefins production yield from methanol using HZSM-5 zeolite catalysis,” JOURNAL OF APPLIED RESEARCHES IN CHEMISTRY (JARC), vol. 12, no. 4 , pp. 77–87, 2019, [Online]. Available: https://sid.ir/paper/180219/en

    Related Journal Papers

    Related Seminar Papers

  • No record.
  • Related Plans

  • No record.
  • Recommended Workshops






    Move to top