室温中心气体分布器注入对 H2竖炉工艺的影响:数值研究

Processes Pub Date : 2024-08-08 DOI:10.3390/pr12081666
Lei Shao, Hongfu Yu, Chenxi Zhao
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引用次数: 0

摘要

在当前工作中,利用基于计算流体动力学的模型研究了通过安装在装置底部的中心气体分配器(CGD)注入常温 H2 的情况下 H2竖炉的性能。建模模拟了 CGD 在不同进气速率(0 至 250 Nm3/t-颗粒)下运行的情况。结果表明,适当的 CGD 气体进料率可以维持较高的温度水平,从而保持较好的内部热化学状态。然而,过高的 CGD 进料率(150 Nm3/t-颗粒或更高值)会导致一种不利的情况,即室温 CGD 气体回收的热能不足以补偿来自热风管的预热进料气体显热的减少。这最终导致在炉子中心形成一个值得注意的高 H2 含量的化学储备区,几乎没有固体还原。因此,大量的 H2 仍未被利用,并从炉顶排出。在研究条件下,当 CGD 气体进料率为 100 Nm3/t-颗粒时,最终的固体还原度升至最大值。研究结果表明,常温 CGD 气体注入操作在实际应用中大有可为。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Effects of Room-Temperature Center Gas Distributor Injection on the H2 Shaft Furnace Process: A Numerical Study
In the current work, a computational fluid dynamics-based model was utilized to investigate the performance of the H2 shaft furnace under a scenario where room-temperature H2 is injected through a center gas distributor (CGD) installed at the unit bottom. Modelling was conducted to simulate scenarios where the CGD operation is applied with different feed gas rates (ranging from 0 to 250 Nm3/t-pellet). The results showed that a high temperature level and thus a better internal thermochemical state can be maintained with a proper CGD gas feed rate. However, an overly high CGD feed rate (being 150 Nm3/t-pellet or a higher value) induces a detrimental scenario where the thermal energy recycled by the room-temperature CGD gas is insufficient to compensate for the decrease of sensible heat of the preheated feed gas from the bustle-pipe. This eventually results in a noteworthy chemical reserve zone of high H2 content and little solid reduction in the furnace center. A large quantity of H2 consequently remains unutilized and leaves the furnace from the top. Under the investigated conditions, the final solid reduction degree rises to maximal value when the CGD gas feed rate is 100 Nm3/t-pellet. The findings of this work revealed that the room-temperature CGD gas injection operation holds significant promise for practical applications.
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