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COAL GASIFICATION REACTOR WITH A FLUID BED AND METHOD FOR COAL GASIFICATION

机译:带流化床的煤气化反应器及气化方法

摘要

Method and apparatus for production of a combustible product gas from particulate coal in a fluidized bed system. A vertically positioned vessel includes an enlarged upper section and a smaller diameter cylindrical lower separator section, of diameter d, bounded at the bottom by a perforated or porous conical distribution plate (20) inclined at 7 DEG to 15 DEG with respect to horizontal; (the plate may also form an inverted cone). Coal is injected upwardly into or at the top of the separator section through tubular inlets (12) terminating a distance l above the distributor plate. The ratio l/d is less than 2.5. Fluidizing gas is injected into the separator section through the distributor plate, maintaining a fluidization velocity in the separator section of about 1.2 Umf (where Umf is the minimum fluidising velocity). Char and ash particles are separated in the separator section, agglomerated ash being withdrawn from the bottom of the lower separator section and the char may be recycled to the combustion jet above the top of the tubular inlets. IMAGE
机译:在流化床系统中由颗粒状煤生产可燃气体的方法和设备。垂直放置的容器包括一个扩大的上部和一个直径为d的较小直径的圆柱形下部分离器部分,在底部由一个相对于水平倾斜7°至15°的多孔或多孔圆锥形分配板(20)界定。 (板也可以形成倒锥)。煤通过在分配板上方距离l终止的管状入口(12)向上注入到分离器段中或顶部。比率l / d小于2.5。流化气体通过分配板注入分离器部分,从而使分离器部分中的流化速度保持在约1.2 Umf(其中,Umf是最小流化速度)。炭和灰分颗粒在分离器部分中分离,团聚的灰分从下部分离器部分的底部排出,并且木炭可以循环到管状入口顶部上方的燃烧喷嘴。 <图像>

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