Destruction of the Tar Present in Syngas by Combustion in Porous Media

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• 作者：T. Carvalho ; M. Costa ; C. Casaca ; R. C. Catapan ; A. A. M. Oliveira
• 刊名：Energy & Fuels
• 出版年：2015
• 出版时间：February 19, 2015
• 年：2015
• 卷：29
• 期：2
• 页码：1130-1136
• 全文大小：398K
• ISSN：1520-5029

文摘

The cleaning of syngas is one of the most important challenges in the development of technologies based on gasification of biomass. Tar is an undesired byproduct because, once condensed, it can cause fouling and plugging and damage the downstream equipment. Thermochemical methods for tar destruction, which include catalytic cracking and thermal cracking, are intrinsically attractive because they are energetically efficient and no movable parts are required nor byproducts are produced. The main difficulty with these methods is the tendency for tar to polymerize at high temperatures. An alternative to tar removal is the complete combustion of the syngas in a porous burner directly as it leaves the particle capture system. In this context, the main aim of this study is to evaluate the destruction of the tar present in the syngas from biomass gasification by combustion in porous media. A gas mixture was used to emulate the syngas, which included toluene as a tar surrogate. Initially, CHEMKIN was used to assess the potential of the proposed solution. The calculations revealed the complete destruction of the tar surrogate for a wide range of operating conditions and indicated that the most important reactions in the toluene conversion are C₆H₅CH₃ + OH 鈫?C₆H₅CH₂ + H₂O, C₆H₅CH₃ + OH 鈫?C₆H₄CH₃ + H₂O, and C₆H₅CH₃ + O 鈫?OC₆H₄CH₃ + H and that the formation of toluene can occur through C₆H₅CH₂ + H 鈫?C₆H₅CH₃. Subsequently, experimental tests were performed in a porous burner fired with pure methane and syngas for two equivalence ratios and three flow velocities. In these tests, the toluene concentration in the syngas varied from 50 to 200 g/Nm³. In line with the CHEMKIN calculations, the results revealed that toluene was almost completely destroyed for all tested conditions and that the process did not affect the performance of the porous burner regarding the emissions of CO, hydrocarbons, and NO_x.