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The authors proposed a correlation equation between the particle segregation coefficient V in a fluidized bed with a paralleltube distributor and the dimensio-nless concentration distribution C along the bed height. Through the cold model experiments, the factors influencing the segregation process in a fluidized bed with a parallel - tube distributor were discussed. On the basis of cold model experiments, the authors added an ash burn-out bed with a porallel - tube distributor to a 35T/H Fluidized Bed Boiler,... The authors proposed a correlation equation between the particle segregation coefficient V in a fluidized bed with a paralleltube distributor and the dimensio-nless concentration distribution C along the bed height. Through the cold model experiments, the factors influencing the segregation process in a fluidized bed with a parallel - tube distributor were discussed. On the basis of cold model experiments, the authors added an ash burn-out bed with a porallel - tube distributor to a 35T/H Fluidized Bed Boiler, with the ash burn-out, the total thermal efficiency of the boiler is around 80% ( 7-8% higher than before ) , and the withdrawal ash temperature is 200℃ lower than before. 本文提出了风管布风床层中沸腾区的颗粒分层参数V与沿床层高度无因次浓度分布c的相关式;通过试验讨论了对风管布风床的颗粒分层的影响因素。在冷态试验基础上,对萍乡一台35T/H流化床锅炉进行改装,增设灰渣燃烬冷却床,使该炉在燃用热值为1600~1700kcal/kg的洗矸时,锅炉热效率可达80%,较之改装前提高7~8%,同时排渣温度可下降约200℃。 In this paper some problems existing in designing and operating large fluidizeal-beds are discussed. Several approaches to the problems are suggested to be adopted to improve the design, e.g.,use of fuel spreading air,use of secondary air to intensify the combustion in the freeboard, rational design of the location of spillway, and so on. The combustion fraction in the fluidization zone is also discussed. 本文讨论了大型流化床锅炉在设计和运行中出现的一些问题。提出了改善措施,如采用播煤风、采用二次风强化悬浮段燃烧,合理选用烧燃分额,并给出了设计和运行的参数值。另外指出了大型流化床锅炉溢流口设置应注意的一些问题。 Considerations of the design and operation of large size FBD boiler are discussed in the paper. The use of coal distributing air, secondary air supported combustion in free board and some other methods are proposed as the improvement measures together with their design and operating data. The effect of in-bed tube structure on bed fluidization as well as that of the fluid-bed combustion on heating surface arrangement is also discussed in the paper. 本文讨论了大型流化床锅炉在设计和运行中出现的一些问题。提出了改善措施,如采用播煤风,采用二次风强化悬浮段燃烧。并给出了设计和运行的参数值。论述了埋管结构对流化质量的影响,以及沸腾层燃烧份额对受热面布置的影响。
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