Abstract

The pant-leg design is typical for higher capacity circulating fluidized bed (CFB) boilers because it allows for better secondary air penetration, maintaining good air-coal mixing and efficient combustion. However, the special risk, nominated as bed inventory overturn, remains a big challenge and it hinders the application of pant-leg CFB boilers. For a time series risk, it is critical to do the bed inventory overturn prevention to leave enough time for the adjustment. This paper proposed a new framework combing long short-term memory (LSTM) and dynamic time warping (DTW) methods to do the risk prediction. Pattern matching of data difference discrimination is employed for DTW algorithm, instead of the traditional Euclidean metric. The pattern matching has the merits in reduction of calculation and improvement of the adaptability to variables with different dimensions. After variable processing of the time series data by the variant DTW algorithm, the bed pressure drop prediction model is established based on the LSTM structure in this framework. Compared with some traditional prediction method, the framework in this paper has achieved superior results in the application of bed inventory overturn prevention.

Highlights

  • The circulating fluidized bed (CFB) boiler is believed to be an improvement over the conventional pulverized coal furnace in some respects [1]

  • THE GENERAL LAYOUT OF THE INVETIGATED BOILER This paper mainly investigates a 300MW coal-fried CFB boiler, which belongs to the 1# unit of JoinLion power plant in China

  • The long short-term memory (LSTM) algorithm has avoided this disadvantage via improving the structure, and it is displayed as Fig. 3

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Summary

Introduction

The circulating fluidized bed (CFB) boiler is believed to be an improvement over the conventional pulverized coal furnace in some respects [1]. Operation of industrial CFB boilers has confirmed some advantages like fuel flexibility, low NOx emissions, high sulphur capture efficiency and so on [2]. As for the CFB furnace, the heat import is proportional to bed cross-sectional area while the heat absorption is proportional to the perimeter of the furnace [3]. With the growing required capacity, both the furnace volume and heat transfer surface increase accompanied by the contradiction that the former increases faster, naturally in need of higher furnace height to control the temperature [4]. The furnace height of a 300MW CFB boiler is mostly limited to about 50m due to commercial consideration.

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