کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
6637050 | 461140 | 2014 | 6 صفحه PDF | دانلود رایگان |
عنوان انگلیسی مقاله ISI
Modeling and analysis of the pyrolysis of bio-oil aqueous fraction in a fixed-bed reactor
ترجمه فارسی عنوان
مدل سازی و تجزیه و تحلیل پریولیزه از کریستال آب زیستی روغن در یک رآکتور بستر ثابت
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کلمات کلیدی
روغن زیتون، رآکتور ثابت ثابت، پیرولیز، سینتیک واکنش مدل ریاضی،
موضوعات مرتبط
مهندسی و علوم پایه
مهندسی شیمی
مهندسی شیمی (عمومی)
چکیده انگلیسی
The pyrolysis of bio-oil is important in improving the utilization of biomass energy and the environmental protection. In this study, simulations were conducted in the Aspen Plus environment using the Gibbs reactor to simulate the equilibrium compositions of the bio-oil pyrolysis products at different temperatures. The molar heat capacity at constant pressure of the chemical balance system was calculated through simulation. The thermodynamic parameters of the reactor were determined using the thermodynamic equations and the mass balance principle. Furthermore, the temperature distribution and conversion rate of different catalyst beds were calculated by combining the Runge-Kutta method with the Matlab software. Finally, experiments were performed in a fixed bed reactor, and the experimental results were compared with the simulated results. The calculation result of the established model is in good agreement with the experimental results.
ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Fuel - Volume 133, 1 October 2014, Pages 1-6
Journal: Fuel - Volume 133, 1 October 2014, Pages 1-6
نویسندگان
Shaomin Liu, Lei Chu, Mingqiang Chen, Wentao Zhang, Wenping Xin,