首页> 外国专利> OPERATION METHOD FOR EXTERNAL CIRCULATING FLUIDIZED BED INCINERATOR USED FOR INCINERATOR OF WASTES WITH HIGH MOISTURE CONTENT AND VOLATILE SUBSTANCE CONTENT SUCH AS SEWAGE SLUDGE

OPERATION METHOD FOR EXTERNAL CIRCULATING FLUIDIZED BED INCINERATOR USED FOR INCINERATOR OF WASTES WITH HIGH MOISTURE CONTENT AND VOLATILE SUBSTANCE CONTENT SUCH AS SEWAGE SLUDGE

机译:污水,污泥等高水分,高挥发物垃圾焚化炉用外部循环流化床焚化炉的操作方法

摘要

PROBLEM TO BE SOLVED: To provide an operation method for a compact and low cost type circulating fluidized bed incinerator capable of the combustion with a low degree of environmental pollution of sewage and sludge having a high moisture content and a high volatile substance content with high efficiency in the circulating fluidized incinerator.;SOLUTION: In a circulating fluidized incinerator forming a bubble fluidized bed from the primary air supplied from the lower side of the fluidized bed and introducing the secondary air to a splash area to reflux the particles conveyed with the particles blowing up outside the furnace by the secondary air through a freeboard to the bubble fluidized bed area through an external circulating part, the amount of the primary air is made to be 10 to 40%, by volume, of the total air amount in distributing the total supplied air amount into the primary air and secondary air. It is characterized by the primary air amount that is 0.15 to 0.5 times the theoretical amount of air required for the complete combustion of an object to be incinerated, and moreover the location at which the secondary air is blown into the bubble fluidized bed area has the height of 1.2 m or higher from a fluidized bed air dispersion plate. The fluid medium with the mean particle diameter of 0.5 mm or smaller is used.;COPYRIGHT: (C)2002,JPO
机译:解决的问题:提供一种紧凑,低成本型循环流化床焚烧炉的操作方法,该燃烧器能够以高水分含量和高挥发性物质含量的污水和污泥进行低环境污染度的燃烧。解决方案:在循环流化焚烧炉中,由从流化床下部供给的一次空气形成气泡流化床,并将二次空气引入飞溅区,以回流随吹出颗粒而输送的颗粒二次空气通过干舷通过外部循环部分到达干馏炉外的气泡流化床区域,使一次空气的量​​占总分布空气总量的10%至40%(按体积计)供气量分为一次空气和二次空气。它的特点是一次空气量是要完全燃烧待焚烧物体所需理论空气量的0.15到0.5倍,而且二次空气吹入气泡流化床区域的位置具有离流化床空气扩散板的高度为1.2 m或更高。使用平均粒径为0.5毫米或更小的流体介质。;版权所有:(C)2002,JPO

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