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Fates and roles of alkali and alkaline earth metallic species in Loy Yang brown coal during in-situ steam gasification

机译:在原位蒸汽气化过程中碱和碱土金属物种碱和碱土金属物种的作用及作用

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Mechanistic investigations were made on steam gasification of nascent chars from pyrolysis of raw Loy Yang brown coal and an acid-washed one that was free from alkali and alkaline-earth metallic (AAEM) species. The pyrolysis and in-situ gasification were performed in a novel drop-tube/fixed-bed reactor, in which an extremely thin fixed-bed of nascent char particles was exposed to steam-containing gas flowing through the bed with high linear velocity and flux. The change with time of the conversion, X, of char from the acid-washed coal was described fairly well by a first-order kinetics, dX/dt = k_a (1 -X), over the entire range of X. For the gasification of nascent char from the raw coal, specific rate of the char conversion, defined by r_(sp) = (dX/dt) / (1 -X), decreased considerably with increasing X up to a certain level, and then became constant at r_(sp) approx = k_a. The decrease in r_(sp) was due to gasification-induced loss of catalysis caused by intra-particle deactivation of AAEM species and their volatilization from the char while the intrinsic reactivity of the char, represented by the rate constant, k_a, was maintained. The time-dependent change in X was described quantitatively by assuming the presence of a single carbonaceous component undergoing non-catalytic gasification and AAEM-species-catalyzed gasification in parallel. The catalytic activity of AAEM species at the initial gasification and the rate of catalytic activity loss were influenced considerably by operating variables such as heating rate for the pyrolysis, period of isothermal heating of the char before exposure to steam, total pressure and/or partial pressure of steam, while k_a was a function of only the temperature and the partial pressure of steam.
机译:从原始LOY阳棕煤热解的蒸汽气化对蒸汽气化进行机械调查,并酸洗的酸洗型,不含碱和碱土金属(AAEM)物种。在新型滴管/固定床反应器中进行热解和原位气化,其中将含有的稀薄的焦炭颗粒的固定床暴露于含玻璃的含蒸汽的气体,具有高线性速度和通量。通过一流的动力学,DX / DT = K_A(1 -X)在整个X的整个范围内,对来自酸洗煤的转化率X的变化X的变化X.对于气化从原煤的​​爆发炭,由r_(sp)=(dx / dt)/(1-x)定义的char转换的特定速率随着x到一定水平的增加而显着降低,然后变得恒定r_(sp)约= k_a。 R_(SP)的降低是由于AAEM物种的颗粒物种内颗粒缺失引起的催化损失,并且它们维持了由速率常数K_A表示的焦炭的固有反应性,而是由Char的固有反应性。通过假设存在在平行的非催化气化和AAEM物种催化气化的单个碳质成分的存在,定量地描述了X的时间依赖性变化。通过操作变量如热解,在暴露于蒸汽,总压力和/或部分压力之前,通过操作变量,催化活性损失在初始气化的催化活性和催化活性损失率的催化活性的影响受到影响。蒸汽,而K_A是仅蒸汽的温度和部分压力的函数。

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