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OPERATION METHOD OF BURNING FURNACE IN CEMENT CLINKER BURNING APPARATUS

机译:水泥熟料燃烧装置中燃烧炉的操作方法

摘要

PURPOSE:To enable the continuous stable operation of a burning furnace by controlling the volume of forced air to primary and secondary cooling device in accordance with the measured grain diameters of granulated material discharged from a jet stream fluidized bed granulating furnace. CONSTITUTION:The granulated material discharged from a granulating furnace 3 is sampled and a grain dicmeater is measured by a grain size measuring instrument 13, and the measured signal is inputted to an arithmetic processor 14. For example, in the case a desired grain diameter is 2.5+ or -0.5mm, when the grain size is=2.0mm, the agglomeration temp. of burning furnace 6 is calculated from the measured grain diameter and the superficial velocity U0 of burning furnace 6 calculated from the layer temp. T2 of the burning furnace 6 and a Roots blower 12. When the temp. is lower than a burning temp. +alpha, the air flow of Roots blower 12 is increased, in accordance with this, the fuel to the burning furnace 6 is increased so that the burning temp. may become constant. The superficial velocity U0 and Umf of a fluidized bed cooler 7 is calculated, and when U0KXUmf and the temp. of fluidized bed cooler 7 is =1100 deg.C, the air flow of a Roots blower 11 is reduced. And the fuel guantity to granulating furnace 3 is controlled so that the temp. of the granulating furnace 3 may become constant.
机译:目的:通过根据从射流流化床造粒炉中排出的颗粒物料的实测粒径,控制进入一级和二级冷却装置的强制空气量,使燃烧炉能够连续稳定运行。组成:从造粒炉3排出的造粒材料被采样,用粒度测量仪13测量颗粒破碎机,并将测得的信号输入到算术处理器14。例如,在期望的粒径为2.5+或-0.5mm,当晶粒尺寸<= 2.0mm时,附聚温度。根据测得的粒径和由层温度计算出的燃烧炉6的表面速度U 0,计算出燃烧炉6的表面温度U 0。 T2的燃烧炉6和罗茨鼓风机12。低于燃烧温度。 +α,罗茨鼓风机12的空气流量增加,据此,流向燃烧炉6的燃料增加,从而燃烧温度升高。可能会变得恒定。当U0> KXUmf和温度时,计算流化床冷却器7的表面速度U0和Umf。如果流化床冷却器7的温度≤1100℃,则罗茨鼓风机11的空气流量减少。并且控制对造粒炉3的燃料污垢,以使温度保持恒定。造粒炉3的温度可以恒定。

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