Title of article :
Kinetic Modeling and Simulation of Pyrolysis of Shrinking BiomassParticle in Fixed Bed Gasifier
Author/Authors :
Sobamowo, M. G Department of Mechanical Engineering - University of Lagos - Akoka - Lagos, Nigeria. , Ojolo, S. J Department of Mechanical Engineering - University of Lagos - Akoka - Lagos, Nigeria. , Osheku, C. A Centre for Space Transport and Propulsion - National Space Research and Development Agency - Federal Ministry of Science and Technology - FCT - Abuja, Nigeria , Kehinde, A. J Department of Mechanical Engineering - University of Lagos - Akoka - Lagos, Nigeria
Pages :
13
From page :
18
To page :
30
Abstract :
Pyrolysis plays an integrated role in the biomass conversion processes. The development of good mathematical models which in consequent leads to the design of pyrolysis reactors. The biomass gasifier is paramount in the scientific studies and understanding of the very important process in the thermochemical conversion of the solid fuels. However, due to the complexities of the biomass reaction scheme, the pyrolysis of biomass is generally modeled on the basis of apparent kinetics. Moreover, it is generally accepted that most important parameters affecting the process are temperature, concentration, residence time and heating conditions. This work presents the simulations of the pyrolysis kinetics of shrinking biomass particle under non-isothermal and isothermal heating conditions. The developed models were used to investigate the effects of shrinkage, heating conditions and heating rates on the pyrolysis of wood. There is a good agreement when the results of the developed models were compared to the experimental results. Theresults of this work could be used in estimating the optimum parameters in the pyrolysis of biomass and in the design of some pyrolysis reactors.
Farsi abstract :
پيروليز نقش جامعي در فرايندهاي تبديل بايومس ايفا مي كند . توسعه مدل هاي رياضي مناسب كه در نتيجه , منجر به طراحي راكتورهاي پيروليز مي شود . گازي فاير بايومس نقش برجسته اي در مطالعات علمي و درك فرايند هاي خيلي مهم در تبديل ترموشيميايي سوخت هاي جامد دارد . اگرچه بدليل پيچيدگي هاي طرحواره واكنش بايومس , پيروليز بايومس بطور كلي براساس سينيتيك ظاهري مدل مي شود . علاوه بر اين بطور كلي پذيرفته شده است كه مهمترين پارامترهاي تاثيرگذار بر فرايند دما , غلظت , زمان اقامت و شرايط گرمايش هستند . اين كار شبيه سازي سينيتيك پيروليز ذرات بايومس كم حجم را تحت شرايط گرمايش همدما و غيرهمدما ارايه مي دهد . مدل هاي توسعه يافته براي بررسي اثرات افت حجمي , شرايط گرمايش , شدت هاي گرمايش بر روي پيروليز چوب استفاده شده است . يك توافق خوب موجود است زماني كه نتايج مدل هاي توسعه يافته با نتايج آزمايشگاهي مقايسه شده است . نتايج اين كار توانسته در تخمين پارامترهاي بهينه در پيروليز بايومس و در طراحي بعضي از راكتورهاي پيروليز استفاده شود .
Keywords :
Shrinking Biomassparticle , Pyrolysis Kinetics , Isothermal condition , Non- isothermalheating , Numerical solutions
Journal title :
Astroparticle Physics
Serial Year :
2016
Record number :
2426730
Link To Document :
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