重力辅助热交换器的设计及其在利用有机朗肯和液化天然气系统加强余热回收中的应用

Q1 Chemical Engineering International Journal of Thermofluids Pub Date : 2024-08-22 DOI:10.1016/j.ijft.2024.100822
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引用次数: 0

摘要

余热回收是指从系统中捕捉并重新利用通常会被丢弃的热量。在制造和发电等行业中,这种方法因其减少温室气体排放和燃料消耗的潜力而日益受到重视。本文讨论了一种新型热交换器系统,该系统利用重力从废气中提取热量,为传统热回收技术所遇到的困难提供了另一种解决方案。此外,通过在该系统中加入 ORC(有机郎肯循环)和 LNG(液化天然气)循环,可以更有效地利用多余的热量,从而实现更好的能量回收。重力管道热交换器和两个循环用于组合能源回收系统,从低品位废物流中提取有用的热量。通过传热分析、能效测试和放能分析来衡量能源性能,然后进行综合参数分析。为了确定最佳运行参数,最大限度地提高能量回收率,减少能量损失,包括对 GPHE 和传统 HE 进行经济分析,开发了数学优化模型。在 35 公斤/秒的空气流速下,热交换器在约 275 ℃ 至 280 ℃ 的最佳温度下表现出良好的效率,接近 52.3%。当戊烷的质量流量为 3.3 公斤/秒时,ORC 循环在最佳运行条件下效率最高。冷凝器压力为 0.21 兆帕时,输出功率最大,达到 280 千瓦。使用戊烷时,循环的最高效率为 36.8%。然而,当冷凝器温度上升 7 °C 时,系统的能效下降了 4.94 %。随着冷凝器压力的升高,ORC 汽轮机的输出功率从 220 千瓦增至 240 千瓦,LNG 汽轮机的输出功率从 25 千瓦增至 40 千瓦。经济分析表明,所设计的 GPHE 从脏废气中回收余热在经济上是可行的。本文建立了一个理论模型来评估从废热中提取能源的几种循环,这可以减少工业中的燃料使用和温室气体排放。
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Design of gravity assisted heat exchanger and its application on enhanced waste heat recuperation utilizing organic Rankine and LNG system

Waste heat recovery involves capturing and reusing heat from a system that would typically be discarded. In industries like manufacturing and power generation, this method is gaining importance due to its potential to reduce greenhouse gas emissions and fuel consumption. This paper discusses a novel heat exchanger system that utilizes gravity to extract heat from exhaust gas, providing an alternative solution to the difficulties encountered by the conventional heat recovery techniques. Moreover, by adding both the ORC (Organic Rankine Cycle) and LNG (Liquefied Natural Gas) cycle to this system, excess heat can be used more efficiently, allowing for better energy recovery. The gravity-pipe heat exchanger and two cycles are used in the combined energy recovery system to extract useful heat from a low-grade waste stream. Energy performance is measured by using heat transfer analysis, energy efficiency testing, and exergy analysis followed by a comprehensive parametric analysis. To identify the optimal operating parameters for maximizing energy recovery and minimizing energy losses including economic analysis of GPHE with conventional HE, mathematical optimization models are developed. The heat exchanger demonstrates good effectiveness, close to 52.3 %, at an optimum temperature of approximately 275 °C to 280 °C for a 35 kg/s air flow rate. The ORC cycle is most efficient with optimum operating condition when pentane's mass flow rate is 3.3 kg/s. The maximum work output is obtained at a condenser pressure of 0.21 MPa, reaching 280 kW. When using pentane, the cycle's maximum efficiency is 36.8 %. However, the system's exergy efficiency drops by 4.94 % when the pinch temperature goes up by 7 °C. The output of ORC turbine increases from 220 kW to 240 kW, and the output of LNG turbine increases from 25 kW to 40 kW, as the condenser pressure rises. From economic analysis it's attain that the designed GPHE is economically viable for waste heat recovery from dirty exhaust gas. This paper develops a theoretical model to evaluate several cycles for extracting energy from waste heat, which could reduce fuel use and greenhouse gas emissions in industries.

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来源期刊
International Journal of Thermofluids
International Journal of Thermofluids Engineering-Mechanical Engineering
CiteScore
10.10
自引率
0.00%
发文量
111
审稿时长
66 days
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