Pressurized Oxygen Blown Entrained-Flow Gasification of Wood Powder

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• 作者：Fredrik Weiland ; Henry Hedman ; Magnus Marklund ; Henrik Wiinikka ; Olov 脰hrman ; Rikard Gebart
• 刊名：Energy & Fuels
• 出版年：2013
• 出版时间：February 21, 2013
• 年：2013
• 卷：27
• 期：2
• 页码：932-941
• 全文大小：384K
• 年卷期：v.27,no.2(February 21, 2013)
• ISSN：1520-5029

文摘

In the present study, an oxygen blown pilot scale pressurized entrained-flow biomass gasification plant (PEBG, 1 MW_th) was designed, constructed, and operated. This Article provides a detailed description of the pilot plant and results from gasification experiments with stem wood biomass made from pine and spruce. The focus was to evaluate the performance of the gasifier with respect to syngas quality and mass and energy balance. The gasifier was operated at an elevated pressure of 2 bar(a) and at an oxygen equivalence ratio (位) between 0.43 and 0.50. The resulting process temperatures in the hot part of the gasifier were in the range of 1100鈥?300 掳C during the experiments. As expected, a higher 位 results in a higher process temperature. The syngas concentrations (dry and N₂ free) during the experiments were 25鈥?8 mol % for H₂, 47鈥?9 mol % for CO, 20鈥?4 mol % for CO₂, and 1鈥? mol % for CH₄. The dry syngas N₂ content was varied between 18 and 25 mol % depending on the operating conditions of the gasifier. The syngas H₂/CO ratio was 0.54鈥?.57. The gasifier cold gas efficiency (CGE) was approximately 70% for the experimental campaigns performed in this study. The synthesis gas produced by the PEBG has potential for further upgrading to renewable products, for example, chemicals or biofuels, because the performance of the gasifier is close to that of other relevant gasifiers.