Effect of heating power on the scrap tires pyrolysis derived oil
| Autor: | Sary Awad, Khaled Loubar, Eskandar Mounif, Radwan Alkhatib, Mohand Tazerout |
|---|---|
| Přispěvatelé: | Laboratoire de génie des procédés - environnement - agroalimentaire (GEPEA), Mines Nantes (Mines Nantes)-Université de Nantes - UFR des Sciences et des Techniques (UN UFR ST), Université de Nantes (UN)-Université de Nantes (UN)-Ecole Nationale Vétérinaire, Agroalimentaire et de l'alimentation Nantes-Atlantique (ONIRIS)-Centre National de la Recherche Scientifique (CNRS), Mines Nantes (Mines Nantes) |
| Jazyk: | angličtina |
| Rok vydání: | 2015 |
| Předmět: |
Materials science
020209 energy 02 engineering and technology Analytical Chemistry 020401 chemical engineering Natural rubber Diels-Alders reaction 0202 electrical engineering electronic engineering information engineering Organic chemistry Dehydrogenation [SPI.GPROC]Engineering Sciences [physics]/Chemical and Process Engineering 0204 chemical engineering Aromatization Tar Coke Heating rate Cracking Fuel Technology Chemical engineering 13. Climate action visual_art Yield (chemistry) tyre pyrolysis visual_art.visual_art_medium Waste tire Pyrolysis |
| Zdroj: | Journal of Analytical and Applied Pyrolysis Journal of Analytical and Applied Pyrolysis, Elsevier, 2015, 116, pp.10--17. ⟨10.1016/j.jaap.2015.10.014⟩ |
| ISSN: | 0003-6676 0165-2370 1873-250X |
| DOI: | 10.1016/j.jaap.2015.10.014⟩ |
| Popis: | WOS:000366763900002; International audience; Experimental investigation is carried out in order to study the effect of power input on the pyrolysis process of waste tires (WT). Three different power input levels i.e., 750W, 1500W and 3000W have been used to heat the reactor to 500 degrees C. The part of energy that was effectively consumed for thermal cracking of rubber and in evaporating the volatile products was deduced by subtracting reactor heating energy (blank tests) from total power input. Changes in physico-chemical characteristics of products were noticed while changing power inputs, which can be the consequence of changes in energy distribution between heating and cracking processes. In addition to the liquid product yield, its tar content is considered to be one of the most important characteristics according to the European standard EN590. From one side, the yield of liquid product for both 1500W and 3000W is higher than 45% while it is around 40% for 750W. On the other side, tar content in the liquid product is higher than 35% at 1500W and 3000W power inputs while it is around 11% at 750W. When high power is introduced to the reactor, it promotes the cracking of CC and CH bonds leading to higher liquid yield and H-2 formation during the pyrolysis. Furthermore, it promotes dehydrogenation/cyclization/aromatization/reactions leading to tar and coke formation. Diels-Alders reaction mechanism explains as well the tar yield in the liquid product via dehydrogenation/aromatization/cyclization/reactions. (C) 2015 Elsevier B.V. All rights reserved. |
| Databáze: | OpenAIRE |
| Externí odkaz: |
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