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Modeling of a steam boiler operation using the boiler nonlinear mathematical model

机译:使用锅炉非线性数学模型对蒸汽锅炉运行进行建模

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The subject of this paper is the steam boiler nonlinear mathematical model. The furnace chamber heat transfer is modelled assuming that the flue gas temperature across the entire furnace chamber is constant. Only radiation heat transfer to the boiler waterwalls is modelled. Distributed parameter mathematical models are developed of the steam superheater individual stages: the superheater first stage, the platen superheater, the second and third stage of the superheater. In the same way, the boiler two-stage economizer is modelled. The flue gas and air temperatures downstream the air heater individual stages are determined using the epsilon-NTU method (effectiveness epsilon - the number of transfer units NTU).Due to such arrangement of the boiler heating surfaces and the heat transfer nonlinear character, iterative calculations of the steam, flue gas, and air temperatures are necessary. The developed mathematical model makes it also possible to determine temperatures of the tube outer and inner surfaces and external fouling for all heating surfaces of the boiler.The developed non-linear mathematical model of the entire boiler has high practical importance. The proposed mathematical model can be used to simulate the boiler operation in various conditions, allowing to determine and correct selection the parameters of boiler operation. A non-linear mathematical model of the boiler can also be used to design the individual stages of the superheater properly so as to achieve the desired temperature behind the individual stages. Determination of the local temperature of the tube wall allows selecting an appropriate grade of steel for the individual stages of the superheater. Also, the developed non-linear mathematical model can be used for boiler operation monitoring in on-line mode. (C) 2019 Elsevier Ltd. All rights reserved.
机译:本文的主题是蒸汽锅炉非线性数学模型。假设整个炉膛内的烟气温度恒定,对炉膛传热进行建模。仅将辐射热传递到锅炉水冷壁进行建模。建立了蒸汽过热器各个阶段的分布参数数学模型:过热器第一阶段,压板过热器,过热器的第二和第三阶段。同样,对锅炉两级节能器进行了建模。空气加热器各级下游的烟气和空气温度使用epsilon-NTU方法确定(有效epsilon-传热单元数量NTU)。由于锅炉受热面的这种布置和传热非线性特性,需要进行迭代计算蒸汽,烟道气和空气温度是必需的。建立的数学模型还可以确定锅炉所有受热面的管道内外表面温度和外部结垢温度。整个锅炉的非线性数学模型具有很高的实际意义。所提出的数学模型可用于模拟各种条件下的锅炉运行,从而可以确定并正确选择锅炉运行的参数。锅炉的非线性数学模型也可以用于适当地设计过热器的各个阶段,以便在各个阶段后获得所需的温度。通过确定管壁的局部温度,可以为过热器的各个阶段选择合适的钢种。而且,开发的非线性数学模型可以用于在线模式下的锅炉运行监控。 (C)2019 Elsevier Ltd.保留所有权利。

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