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:

877
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

DYNAMIC MODELING OF METHYL ACETATE HYDROLYSIS PACKED BED REACTOR AND DETERMINATION OF AXIAL DISPERSION COEFFICIENTS

Pages

  65-72

Abstract

 In this work, a PACKED BED REACTOR of methyl acetate HYDROLYSIS process has been studied. First, mass transfer limitations from bulk fluid to catalyst surface and then from surface into catalyst body were investigated quantitatively. Whereas diffusion had no any limitation on the overall rate of reaction, a pseudo homogeneous one dimensional model considering AXIAL DISPERSION COEFFICIENTS was developed. A LHHW kinetic model for rate of reaction and a Longmuir model for equilibrium adsorption of species on the catalyst, developed experimentally, were used in the mathematical model. An experiment of pulse-input feed to reactor was performed and concentration of reactor product versus time was determined. The model were solved by the numerical method of lines and the absolute difference between calculated concentration profile and those measured experimentally was defined as the objective function which was optimized by Levenberg-Marquardt OPTIMIZATION algorithm. A comparison of our model with ideal Plug Flow model and also with previous model in literature shows that this model is more accurate and more comprehensive than the others and can be used in many comparable industrial cases.

Cites

  • No record.
  • References

    Cite

    APA: Copy

    EFTEKHARI, A.A., EHTESHAMI, MAHDI, RAHIMI, MAHNAZ, & JAFARI NASR, M.R.. (2010). DYNAMIC MODELING OF METHYL ACETATE HYDROLYSIS PACKED BED REACTOR AND DETERMINATION OF AXIAL DISPERSION COEFFICIENTS. JOURNAL OF APPLIED RESEARCHES IN CHEMISTRY (JARC), 4(13), 65-72. SID. https://sid.ir/paper/180206/en

    Vancouver: Copy

    EFTEKHARI A.A., EHTESHAMI MAHDI, RAHIMI MAHNAZ, JAFARI NASR M.R.. DYNAMIC MODELING OF METHYL ACETATE HYDROLYSIS PACKED BED REACTOR AND DETERMINATION OF AXIAL DISPERSION COEFFICIENTS. JOURNAL OF APPLIED RESEARCHES IN CHEMISTRY (JARC)[Internet]. 2010;4(13):65-72. Available from: https://sid.ir/paper/180206/en

    IEEE: Copy

    A.A. EFTEKHARI, MAHDI EHTESHAMI, MAHNAZ RAHIMI, and M.R. JAFARI NASR, “DYNAMIC MODELING OF METHYL ACETATE HYDROLYSIS PACKED BED REACTOR AND DETERMINATION OF AXIAL DISPERSION COEFFICIENTS,” JOURNAL OF APPLIED RESEARCHES IN CHEMISTRY (JARC), vol. 4, no. 13, pp. 65–72, 2010, [Online]. Available: https://sid.ir/paper/180206/en

    Related Journal Papers

    Related Seminar Papers

  • No record.
  • Related Plans

  • No record.
  • Recommended Workshops






    Move to top