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SLAGGING CHARACTERISTICS OF AUSTRALIAN BROWN COAL ASHES

机译:澳大利亚褐煤灰的结渣特性

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The behaviour of coal mineral matter must be considered when matching coals to the most appropriate gasification technology. While non-slagging gasifiers require coal processing at temperatures below ash melting or ash softening, slagging gasifiers require the mineral matter to melt and flow with a viscosity suitable for steady slag tapping. Some entrained-flow gasifiers also require the slag to form a protective layer in the water-cooled wall of the gasification chamber, which sets a minimum ash content for the feed coal.rnThe mineral matter composition of Australian brown coals is highly variable and covers a wide range of compositions in the Si-Al-Fe-Ca-Mg-O system. In this work, we investigate the slagging characteristics (e.g. phase compositions and viscosity) of typical brown coal ashes from Latrobe Valley in Victoria, Australia.rnSlag compositions were calculated using thermodynamic modelling tools and confirmed experimentally by analysis of quenched slags. Experimental slag viscosity data were obtained from 1200–1650℃. The liquid phase appearance in the low-temperature slagging region (900–1100℃) strongly depends on the slag’s chemical composition and the primary phase field, but is not directly related to ash fusion temperatures. High-silica slags typically have Newtonian slag flow behaviour and high viscosity, which may require fluxing to reduce viscosity and make them suitable for use in entrained-flow gasification (5–25 Pa·s). High iron–magnesium and high aluminium slags have low viscosities at high temperatures (above 1500℃), although the slag flow has non-Newtonian behaviour over the entire investigated temperature range. These slags need to be blended with other coals for use in entrained-flow installations.
机译:在将煤匹配到最合适的气化技术时,必须考虑煤矿物质的行为。非结渣气化炉要求在低于灰烬熔化或灰化软化的温度下进行煤炭加工,而成渣气化炉要求矿物质熔化并以适合于稳定出渣的粘度流动。一些气流床气化炉还需要炉渣在气化室的水冷壁上形成保护层,从而为进料煤设定了最小的灰分。rn澳大利亚褐煤的矿物质组成变化很大,并且覆盖了Si-Al-Fe-Ca-Mg-O系统中的成分范围很广。在这项工作中,我们调查了来自澳大利亚维多利亚州拉特罗布山谷的典型褐煤灰的结渣特性(例如相组成和粘度)。使用热力学建模工具计算了rnSlag的组成,并通过分析淬火炉渣进行了实验验证。实验炉渣粘度数据是在1200-1650℃下获得的。低温排渣区(900-1100℃)的液相外观在很大程度上取决于炉渣的化学成分和初生相场,但与灰熔融温度没有直接关系。高硅渣通常具有牛顿渣的流动特性和高粘度,可能需要通过助熔剂来降低粘度,使其适合于气流床气化(5-25 Pa·s)。尽管在整个研究温度范围内,渣流具有非牛顿性,但高铁镁渣和高铝渣在高温(1500℃以上)下的粘度较低。这些炉渣需要与其他煤混合以用于气流床装置。

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