绿色氨合成工艺负载调节策略的动态模拟与优化

IF 3.8 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Limei Wen, Chao Huang, Zhongde Dai, Lihong Nie, Xu Ji, Yiyang Dai
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引用次数: 0

摘要

由可再生能源电力驱动的绿色合成氨工艺是备受推崇的脱碳途径。由于风能和太阳能等可再生能源固有的随机性、不稳定性和间歇性,绿色电力负荷也随之波动。考虑到大规模储氢和储电可能会带来经济和技术上的困难,通常采用小型储氢系统结合氨合成装置的动态负荷调节来适应这些波动。与传统合成氨厂相比,这种绿色合成氨工艺会导致更频繁的过渡状态操作,如负荷调节情景。优化负荷调节策略可有效缩短过渡时间,提高经济效益。这项工作采用了严格的动态模拟,以检查与各种负荷调节方案相关的潜在不可行性和运行风险。该模型的可靠性通过工业数据进行了验证。在此动态模型的基础上,提出了一种两步优化法来改进过渡策略。首先,进行工艺优化,考虑工艺拓扑和控制方案的修改,以提高工艺稳定性和可操作性。随后,在优化流程的基础上进行操作优化,最大限度地缩短操作时间,使系统迅速达到稳定状态,生产出高质量的产品。通过对实际设计的绿色合成氨工艺进行案例研究,证明了所提方法具有显著的操作和经济效益。结果表明,与工业标准策略相比,使用优化负载调节策略可大幅降低能源成本、减少由无碳氢气和氮气组成的原料气浪费和氢气储存,同时将过渡时间缩短 27-30%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Dynamic Simulation and Optimization for Load Regulation Strategies of the Green Ammonia Synthesis Process

Dynamic Simulation and Optimization for Load Regulation Strategies of the Green Ammonia Synthesis Process
The green ammonia synthesis process driven by renewable electricity represents a highly regarded decarbonization pathway. Due to the inherent randomness, volatility, and intermittency of renewable energy sources, such as wind and solar power, the green power load fluctuates accordingly. Considering that large-scale storage of hydrogen and electricity could introduce economic and technical difficulties, a small-scale hydrogen storage system combined with dynamic load regulation of the ammonia synthesis unit is commonly adopted to accommodate these fluctuations. This green ammonia process results in more frequent transition state operations, such as load regulation scenarios, compared with traditional ammonia plants. Optimizing load regulation strategies can effectively reduce the transition time and enhance economic benefits. This work employs a rigorous dynamic simulation to examine potential infeasibilities and operational risks associated with various load regulation scenarios. The model’s reliability is validated using industrial data. Based on this dynamic model, a two-step optimization approach is proposed to improve transition strategies. First, process optimization, considering process topology and control scheme modifications, is conducted to enhance the process stability and operability. Subsequently, operation optimization is performed to minimize the duration of operations based on the optimized process, enabling the system to swiftly reach a steady state and produce high-quality products. A case study of a realistically designed green ammonia synthesis process demonstrates the significant operational and economic benefits of the proposed methodology. Results indicate that energy costs, waste of the feed gas composed of carbon-free hydrogen and nitrogen, and hydrogen storage can be substantially reduced, while transition time is shortened by 27–30% using optimized load regulation strategies compared to the industrial standard strategies.
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来源期刊
Industrial & Engineering Chemistry Research
Industrial & Engineering Chemistry Research 工程技术-工程:化工
CiteScore
7.40
自引率
7.10%
发文量
1467
审稿时长
2.8 months
期刊介绍: ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.
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