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Design Development of Integrated Methane Pyrolysis and Reforming Processes for Low-Carbon Urea Production
ACS Sustainable Chemistry & Engineering ( IF 7.1 ) Pub Date : 2024-11-20 , DOI: 10.1021/acssuschemeng.4c05611
Muhamad Reda Galih Pangestu, Usama Ahmed, Sunhwa Park, Umer Zahid

As the world’s population continues to grow, the demand for fertilizers is expected to be large. Natural gas through steam methane reforming (SMR) is a major source of greenhouse gas (GHG) emissions during traditional ammonia-urea synthesis. Especially in case of ammonia and urea production rates unbalance, CO2 emissions will increase. By contrast, methane pyrolysis (MP) offers a more sustainable alternative. Besides making solid carbon as a saleable byproduct, this method also enables the continuous synthesis of ammonia and urea with zero CO2 emissions. This research explores the technical and financial viability of incorporating MP into a traditional SMR-ammonia-urea facility by dividing the NG feed between the SMR and MP sections. A simulation model was developed using Aspen Plus to analyze the integrated system. Results indicate that the proposed model achieves an optimal methane conversion rate of 73.2%, while targeting carbon black (CB) as a coproduct in the noncatalytic MP process. In contrast to the traditional plant, the proposed model demonstrates a reduction in power consumption of approximately 5.8 MW and reduced total direct CO2 emission intensity (t-CO2/t-urea) up to 47.72%. Under conditions mirroring projected trends in the Middle East, where NG prices stand at 2 USD/MMBTU, with a CO2 tax policy of 8 USD/ton-CO2 and a CB price of 1500 USD/ton, the proposed model exhibits approximately 8 million USD/yr more profit than the base model. Sensitivity analysis further highlights that the proposed model consistently achieves a higher net present value (NPV) than the base model under varying product prices, confirming its superior economic performance across different scenarios.

中文翻译:


用于低碳尿素生产的综合甲烷热解和重整工艺的设计开发



随着世界人口的持续增长,预计对肥料的需求将很大。通过蒸汽甲烷重整 (SMR) 实现的天然气是传统氨尿素合成过程中温室气体排放的主要来源。特别是在氨和尿素生产率不平衡的情况下,二氧化碳排放量会增加。相比之下,甲烷热解 (MP) 提供了一种更可持续的替代方案。除了将固体碳作为可销售的副产品外,该方法还可以连续合成氨和尿素,实现零CO2 排放。本研究探讨了通过在 SMR 和 MP 部分之间分配 NG 进料,将 MP 纳入传统 SMR-氨-尿素设施的技术和财务可行性。使用 Aspen Plus 开发了一个仿真模型来分析集成系统。结果表明,所提出的模型实现了 73.2% 的最佳甲烷转化率,同时将炭黑 (CB) 作为非催化 MP 过程中的副产品。与传统工厂相比,所提出的模型表明,功耗降低了约 5.8 MW,并将总 CO2 直接排放强度 (t-CO2/t-尿素) 降低了 47.72%。在反映中东预测趋势的条件下,天然气价格为 2 美元/百万英热单位,二氧化碳税收政策为 8 美元/吨二氧化碳,CB 价格为 1500 美元/吨,拟议模型比基本模型多出约 800 万美元/年的利润。敏感性分析进一步强调,在不同的产品价格下,所提出的模型始终实现比基础模型更高的净现值 (NPV),证实了其在不同情景下的卓越经济表现。
更新日期:2024-11-20
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