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Lignite-char gasification mechanism in mixed atmospheres of steam and CO2 at different pressures

机译:蒸汽和CO2混合气氛中不同压力下褐煤焦气化机理

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Gasification characteristics of lignite-char with steam, CO2 and their mixture in a pressurized fixed bed (PFB) reactor were investigated at different pressures (0.10 similar to 2.0 MPa, N-2 as dilute gas). The results show that char-gasification mechanism in the mixture of steam and CO2 are connected with relative partial pressures of two reactant gases. A turning value of steam partial pressure is found in char gasification, when the steam partial pressure is lower than the value, the char gasification rate firstly increase and then drops with CO2 partial pressure increase; whereas, when the steam partial pressure is higher than the value, the increase of CO2 partial pressure results in char gasification rate decrease. The reaction mechanism of lignite-char gasification in the mixture of steam and CO2 is closely related to the total pressure: under lower pressures, it is consistent with the separate reactive site reaction mechanism; while under higher pressures, it approaches to the common reactive site reaction mechanism. (C) 2015 Elsevier B.V. All rights reserved.
机译:研究了褐煤炭在压力固定床(PFB)中在不同压力(0.10类似于2.0 MPa,N-2作为稀薄气体)下与蒸汽,CO2及其混合物的气化特性。结果表明,蒸汽和二氧化碳混合气中的焦炭气化机理与两种反应气体的相对分压有关。在焦炭气化过程中发现蒸汽分压的转向值,当蒸汽分压低于该值时,焦炭气化率先升高然后随CO2分压的增加而下降;反之,当蒸汽分压高于该值时,CO2分压的增加导致炭气化率降低。蒸汽与CO2混合气中褐煤焦化的反应机理与总压力密切相关:在较低压力下,这与单独的反应中心反应机理是一致的。而在较高压力下,它趋近于常见的反应部位反应机理。 (C)2015 Elsevier B.V.保留所有权利。

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