این سایت در حال حاضر پشتیبانی نمی شود و امکان دارد داده های نشریات بروز نباشند
صفحه اصلی
درباره پایگاه
فهرست سامانه ها
الزامات سامانه ها
فهرست سازمانی
تماس با ما
JCR 2016
جستجوی مقالات
دوشنبه 17 آذر 1404
Iranian Journal of Chemistry and Chemical Engineering
، جلد ۴۴، شماره ۱۰، صفحات ۲۵۳۳-۲۵۴۳
عنوان فارسی
چکیده فارسی مقاله
کلیدواژههای فارسی مقاله
عنوان انگلیسی
Kinetic Study of Xylene Isomerization Reaction and Ethylbenzene Conversion on Mo-Pt@ZSM5 Catalyst
چکیده انگلیسی مقاله
This research theoretically studies xylene isomerization on the Mo-Pt@ZSM5 catalyst. The inlet stream composition is similar to the actual current in the petrochemical unit. The empirical data are gas-phase compositions in the temperature range 370
o
C to 400
o
C in the catalytic reactor. Two suitable kinetic models were proposed for catalytic reactions, one incorporating adsorption terms and the other mass transfer coefficients into the rate equations. The model's predictions are acceptable compared to the laboratory error of about 1%. Using a genetic algorithm, surface adsorption equilibrium constants appearing in the denominator of the first model were evaluated for metaxylene as K
m
= 0.0012, and for ethylbenzene as K
eb
= 0.0379. In the second model, the meta and ortho mass transfer coefficients are equal, and β
M
= 1.514×10
6
cm
3
/(g
cat
.h), and β
EB
= 6.847×10
5
cm
3
/(g
cat
.h), are derived using a genetic algorithm.
The rate constants in both models are k
3
= 0.0561 mole
i
/(g
cat
.h), k
9
= 0.0285 mole
i
/(g
cat
.h), and Arrhenius constants are k
07
= 1417 mole
i
/(g
cat
.h), E
7
= 35592 J/mol, k
011
= 3.156×10
7
mole
i
/(g
cat
.h), and E
11
= 1.283×10
5
J/mol. The results show that, as expected, the metaxylene and orthoxylene decrease along the reactor, and the concentration of paraxylene increases. The results of the second model showed that the mass transfer resistance can be ignored for xylenes. But, in the case of ethylbenzene, mass transfer resistance has a greater effect. Therefore, both models have the same precision; however, they provide different information about the adsorption and mass transfer of components.
کلیدواژههای انگلیسی مقاله
Isomerization,xylene,Conversion,Ethylbenzene,catalyst
نویسندگان مقاله
Monire Kazemi |
Department of Chemical Engineering, Faculty of Engineering, Ardakan University, Ardakan, I.R. IRAN
Seyyed Hamid Esmaeili-Faraj |
Department of Material and Chemical Engineering Shahrood University of Technology, Shahrood, I.R. IRAN
Majid Emami Meibodi |
Department of Chemical Engineering, Faculty of Engineering, Ardakan University, Ardakan, I.R. IRAN
نشانی اینترنتی
https://ijcce.ac.ir/article_729011_68f5fd309a9c6871c4dd86dd0c25562f.pdf
فایل مقاله
فایلی برای مقاله ذخیره نشده است
کد مقاله (doi)
زبان مقاله منتشر شده
en
موضوعات مقاله منتشر شده
نوع مقاله منتشر شده
برگشت به:
صفحه اول پایگاه
|
نسخه مرتبط
|
نشریه مرتبط
|
فهرست نشریات