首页> 外文会议>International Conference on Fluidized Bed Combustion; 20050522-25; Toronto(CA) >THE DESIGN AND OPERATION OF A NEW CLAPBOARD - TYPE INTERNAL CIRCULATING FLUIDIZED-BED GASIFIER
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THE DESIGN AND OPERATION OF A NEW CLAPBOARD - TYPE INTERNAL CIRCULATING FLUIDIZED-BED GASIFIER

机译:新型隔板型内部循环流化床气化炉的设计与运行。

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The design and operation of a new clapboard-type Internal Circulating Fluidized-Bed gasifier is introduced in this paper. By setting clapboard in the middle of gasifier, bed layer in gasifier is divided into two regions that have different fluidization velocity, the incompletely reacted fuel or carbon in the high velocity region flows to the low velocity region companying with bed medium, and gasification reaction takes place in this region; still incompletely reacted fuel or carbon returns to the high velocity region in the bottom of gasifier, then gasification reaction further occurs. By this way, internal circulation in the gasifier was formed, gasification reaction time and efficiency increased. The experimental results indicate that gas yield (1.6 ~ 1.9Nm~3/kg fuel), gas heat values (5340kJ/Nm~3 for wood chip fuel and 4880kJ/m~3 for rice husk), and gasification efficiency (70%) can be obtained using this kind of gasifier in the optimal operational temperature range of 790 ~ 850?.
机译:介绍了新型隔板式内循环流化床气化炉的设计与运行。通过在气化炉中部设置隔板,将气化炉内的床层分为流化速度不同的两个区域,高速区中不完全反应的燃料或碳与床层介质一起流向低速区,进行气化反应。在这个地区仍然没有完全反应的燃料或碳返回到气化炉底部的高速区域,然后进一步发生气化反应。这样,在气化炉中形成内部循环,气化反应时间和效率增加。实验结果表明,瓦斯产量(1.6〜1.9Nm〜3 / kg燃料),瓦斯热值(木屑燃料为5340kJ / Nm〜3和稻壳为4880kJ / m〜3),气化效率(70%)。使用这种气化炉可以在790〜850?的最佳工作温度范围内获得。

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