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Gasification Characteristics of Municipal Solid Wastes in a Batch Type Fixed Reactor

机译:批型固定反应器中城市固体废物的气化特性

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To provide reasonable operation conditions for the gasification of municipal solid waste (MSW), the effect of reaction temperature, residence time and air supply ratio were evaluated with a batch type fixed reactor. The reactor of 0.21m~3 was heated by external electric heater. Sample of 500g was inserted on the stoker that was placed at 150 mm above the bottom of reactor. K-type thermocouples were used to measure temperature inside reactor and sample. Air supply ratio was controlled 0 to 0.5 with nitrogen and air, and they were supplied to stoker from the bottom of reactor. MSW sample used in this experiment was consisted of garbage, plastics, paper and woods. Each component in sample was grinded below 10mm in diameter. The generation rate of gas was measured by differential pressure detector. Gaseous product was collected with gasbag at interval of five minutes, and then analyzed by using GC-TCD (HP5890-2). The generation rate, ignition loss and calorific value of solid products were also estimated. As the moisture of MSW evaporated in initial step, gaseous products was seems to decrease with elapsing residence time. It was also decreased as air supply ratio increased. Most of gaseous products were composed of CO, CO_2 and hydrocarbon including CH_4. All of hydrocarbon was decreased except CO as air supply ratio increased. The ignition loss and calorific value of solid products were 60~80% and 4,900~5,200kcal/kg respectively. Most of gasification reactions were almost finished within 15 minutes in this experimental condition.
机译:为为城市固体废物(MSW)气化提供合理的操作条件,用批型固定反应器评价反应温度,停留时间和空气供应比的影响。外部电加热器加热0.21m〜3的反应器。将500g的样品插入到置于反应器底部的150mm处。 K型热电偶用于测量反应器和样品内的温度。空气供应比用氮气和空气控制0至0.5,它们从反应器的底部供应到Dister。本实验中使用的MSW样品由垃圾,塑料,纸和森林组成。样品中的每种组分在直径10mm以下研磨。通过差压检测器测量气体的产生速率。在5分钟的间隔时使用气囊收集气囊,然后通过使用GC-TCD(HP5890-2)分析。还估计了固体产品的产生率,点火损失和热值。随着在初始步骤中蒸发的MSW水分,气态产物似乎随着经过的停留时间而降低。随着空气供应比增加,它也减少了。大多数气态产物由包括CH_4的CO,CO_2和烃组成。除了空气供给比增加,除了CO之外,所有烃除外。固体产物的点火损失和热值分别为60〜80%和4,900〜5,200kcal / kg。在该实验条件下,大多数气化反应几乎在15分钟内完成。

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