کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
6475973 1424977 2017 11 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Heat and mass transfer within thermogravimetric analyser: From simulation to improved estimation of kinetic data for char gasification
ترجمه فارسی عنوان
انتقال گرما و جرم در دستگاه آنالایزر ترموگرافی: از شبیه سازی به منظور برآورد بهتر داده های جنبشی برای گاز زدن ماهیت
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
چکیده انگلیسی


- Gasification experiments of HOK lignite char with CO2 in TGA are conducted.
- CFD reactor simulation of the char gasification in TGA is presented.
- Char conversion including heat and mass transfer near the sample is modeled.
- Detailed particle-resolved simulations of char within crucible validate the model.
- Diffusion limitation are considered for estimation of kinetic parameters.

Thermogravimetric analysis is a standard experimental method to determine kinetic data for heterogeneous coal char reactions. However, it is necessary to implement a sample holder to weigh the char sample, which may influence the mass and heat transfer towards the crucible. Thus, in this work the heat and mass transfer phenomena in a TGA were investigated. Experiments were carried out with hearth furnace char at temperatures between 1073 and 1273 K and a pressure of 1 bar. Based on the experiments, computational fluid dynamics was utilized to study the macroscopic transport mechanism employing a heterogeneous reaction on the external surface at a temperature of 1100 K. For the species transport it is shown that convection plays a minor role in the crucible and diffusion is predominant. The aim of the work is to present a methodology for evaluating the resultant kinetic data taking the resistances in heat and mass transfer into account. For this purpose, the true species concentration and temperature at the sample were calculated. Therefore, the relevant heat and mass transport phenomena were modeled using a zero-dimensional approach considering spatially uniform concentrations and temperatures in the transient process. The model was validated by detailed CFD simulations of the reacting packed bed of char particles in the range of 900-1250 K. It was found out that the concentration of the gasification agent was about 14% lower than expected as the maximal deviation. Thus, the consideration of diffusional effects within the crucible resulted in higher activation energies and different reaction orders when the kinetic parameters were determined.

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ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Fuel - Volume 187, 1 January 2017, Pages 338-348
نویسندگان
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