首页> 外文会议>6th European Conference on Industrial Furnaces and Boilers Vol.3, Apr 2-5, 2002, Estoril-Lisboa, Portugal >MODELLING OF A SLAB REHEATING FURNACE RETROFITTED WITH REGENERATIVE BURNERS
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MODELLING OF A SLAB REHEATING FURNACE RETROFITTED WITH REGENERATIVE BURNERS

机译:蓄热式燃烧炉改造的平板加热炉的建模

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Several measures are currently under consideration, in the steel manufacturing industry, in order to reduce its CO_2 production. Namely, in the hot mills, introducing still-warm slabs in the reheating furnace and increasing heat recuperation on the furnace flue gas , appear rather obvious. However, to be economically attractive, they should be implemented through an increase of furnace capacity. This may be achieved by retrofitting regenerative burners in existing furnaces. The aim of this work, was to develop a tool allowing to quickly assess the furnace performance for different configurations of burners and different operating conditions, in order to select the most appropriate one(s). In particular, regarding the added regenerative burners, the following conditions are liable to an investigation ( location in the furnace, burner individual capacity, excess air,extracted" flue gas flow rate,regenerator efficiency). In the cases at hand, the reheating furnace is of the walking beam type. The furnace model is 1-D steady-state, taking into account the flow distribution as well as the heat generation, transfer and losses. As to the regenerators and the recuperators, they are modelled simply in terms of effectiveness. A problem arises in modelling as steady-state the operation of regenerative burners, since these devices are fundamentally cyclical. To take the measure of this problem, we have simulated ― separately ― the different phases of operation and compared the results. Such a study will be presented in the paper. Among the different industrial cases simulated with this model, we will present the following two ones : 1. Replacing all the existing (standard) burners by regenerative burners; 2. Replacing the burners of one heating zone only. It will be shown that for both schemes and for realistic burner performances, the efficiency of the whole installation is improved, and the furnace capacity is increased. If done properly, the latter configuration appears very attractive indeed.
机译:在钢铁制造业中,目前正在考虑采取几种措施,以减少其CO_2的产量。即,在热轧机中,在再加热炉中导入仍热的板坯并提高炉烟气的热回收率是很明显的。但是,为了在经济上具有吸引力,应通过提高熔炉容量来实施它们。这可以通过在现有熔炉中改装蓄热式燃烧器来实现。这项工作的目的是开发一种工具,该工具可以针对不同的燃烧器配置和不同的运行条件快速评估炉子性能,从而选择最合适的炉子。特别是,对于增加的蓄热式燃烧器,需要检查以下条件(炉中的位置,燃烧器的单个容量,过量空气,抽出的“烟道气流量”,蓄热器效率)。考虑到流分布以及热量的产生,传递和损失,炉模型是一维稳态的,对于蓄热​​室和换热室,它们的建模简单:由于这些装置从根本上来说是周期性的,因此在将再生式燃烧器的运行建模为稳态时会出现问题,为解决这个问题,我们分别模拟了运行的不同阶段并比较了结果。在该模型模拟的不同工业案例中,我们将介绍以下两个案例:1.更换所有现有(标准)燃烧器通过蓄热式燃烧器; 2.仅更换一个加热区的燃烧器。将显示出,对于两种方案以及对于实际的燃烧器性能而言,整个装置的效率都得到了提高,并且熔炉容量得到了提高。如果做得好,后一种配置确实确实很有吸引力。

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