针对各种膜性能的技术经济过程优化:什么能为点源碳捕集提供真正的价值?

Joshua C. Watson, Kenneth J. Pennisi, Christine Parrish, Sudip Majumdar
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引用次数: 0

摘要

膜为重工业脱碳提供了一个独特的机会,而真正的解决方案需要最佳的系统设计。我们使用上层建筑工艺模型来最大限度地降低燃烧后碳捕集系统的资本和运营费用。我们考虑了二氧化碳渗透率在 100 到 5000 GPU 之间、二氧化碳对 N2 的选择性在 10 到 300 之间的膜。对于所研究的四个重工业代表性案例,我们发现选择性大约高于 30 的膜具有基本相同的经济性。当二氧化碳的渗透率超过 1000 GPU,选择性在 20 到 30 之间时,我们发现膜系统可以实现低捕获成本(每吨 20 到 55 美元)和高能效(每吨 150 到 500 千瓦时)。膜特性与优化工艺经济性之间的定量关系可实现商业应用的有效产品开发。
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Techno-economic process optimization for a range of membrane performances: What provides real value for point-source carbon capture?

Membranes provide a unique opportunity for heavy industry decarbonization and a real solution requires optimal system design. We use a superstructure process model to minimize capital and operational expenses for post-combustion carbon capture systems. We consider membranes having CO2 permeances between 100 and 5000 GPU and selectivities for CO2 over N2 ranging from 10 to 300. For the four heavy industry-representative cases studied, we find membranes with selectivities approximately above 30 have essentially the same economics. When the permeance of CO2 is above 1000 GPU, and the selectivity is between 20 and 30, we find that membrane systems can achieve low capture costs ($20 to $55 per ton) and high energy efficiencies (150 to 500 kWh per ton). A quantitative relationship between membrane properties and optimized process economics enables effective product development for commercial applications.

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