|
|
methanol to propylene (mtp) process modeling and calculation of effectiveness parameters
|
|
|
DOR
|
20.1001.2.9919199705.1399.11.1.94.9
|
نویسنده
|
- - ,- - ,- - ,- -
|
منبع
|
كنگره مهندسي شيمي - 1399 - دوره : 11 - یازدهمین کنگره بین المللی مهندسی شیمی - کد همایش: 99191-99705
|
چکیده
|
In this work, based on the kinetics obtained in previous work and the experimental data of a fixed bed reactor and by providing a one-dimensional model for the reactor and optimizing by genetic algorithm, the effectiveness factors for the zsm-5 catalyst were obtained at 420-450 ° c# it was observed that the temperature changes at this range had negligible effect on the effectiveness parameters# by using the obtained factors at 480 and 500 ° c and comparing the result of model and experiments data at these temperatures, these factors were confirmed# in the next step, the mathematic modeling of the methanol to propylene fixed bed reactors has performed in two level; one-dimensional and two-dimensional# the results of model were compared with the experiment result of the mtp pilot plant in npc-rt company# the comparison is shown that both models are well predicted the reactor behavior#
|
کلیدواژه
|
propylene ,methanol ,zsm-5 catalyst ,effectiveness factor ,fixed bed reactor modeling
|
آدرس
|
college azad eslamic university (sourth tehran), iran, sharif university of technology, iran, research institute of petroleum industry (ripi), iran, college azad eslamic university (sourth tehran), iran
|
|
|
|
|
|
|
|
|
|
|
|
|
|
Authors
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|