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Advanced Amine and Ammonia Systems for Greenhouse Gas Control at Fossil Fuel Power Plants.

机译:用于化石燃料发电厂温室气体控制的先进胺和氨系统。

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摘要

In an effort to lower future CO2 emissions, a wide range of technologies are being developed to scrub CO2 from the flue gases of fossil fuel-based electric power and industrial plants. This thesis models two leading post-combustion CO2 capture technologies, a chilled ammonia-based CO2 capture process and an advanced amine-based CO 2 capture process, and presents performance and cost estimates of these systems on pulverized coal and natural gas combined cycle power plants.;The process modeling software package Aspen PlusRTM was used to develop performance and cost estimates for the chilled ammonia-based CO2 capture technology and general response surface equations were created for the model. Assumptions about plant financing and utilization, as well as uncertainties in cooling costs and chemical reaction rates that affect absorber cost were found to produce a wide range of cost estimates for ammonia-based CO2 capture systems. With uncertainties included, costs for a supercritical power plant with ammonia-based CO2 capture ranged from ;For the advanced amine-based CO2 capture technology, an existing amine-based response surface model developed using ProtreatRTM simulations was modified to match the performance and cost characteristics of a modern amine-based system. The response surface models of both technologies were incorporated into the Integrated Environmental Control Model for use in developing performance and cost estimates of pulverized coal and natural gas combined cycle power plants with these technologies. The baseline costs for a supercritical power plant with advanced amine-based CO2 capture was ;Both post-combustion CO2 capture technologies are then compared in terms of performance and cost for different ranges of fuel type, fuel cost, plant size, and CO2 capture system train size. A probabilistic cost difference analysis is also used to compare these technologies. The amine-based CO2 capture system is found to have a higher revenue requirement in all the case studies and only a 2% chance of having a lower revenue requirement than the advanced amine system in the probabilistic cost difference. Combined, these results suggest that the advanced amine system will have a cost advantage over the ammonia system in most cases, in the absence of significant new improvements in the ammonia system design. Finally, the importance of these estimates for policy makers is discussed.
机译:为了降低未来的CO2排放,正在开发各种各样的技术来从基于化石燃料的电力和工业厂房的烟气中清除CO2。本文对两种领先的燃烧后二氧化碳捕集技术进行了建模,分别是基于冷氨的二氧化碳捕集工艺和基于胺的先进二氧化碳捕集工艺,并介绍了这些系统在粉煤和天然气联合循环发电厂中的性能和成本估算。;使用过程建模软件包Aspen PlusRTM来开发基于冷氨的CO2捕集技术的性能和成本估算,并为该模型创建了通用响应面方程。人们发现,有关工厂融资和利用的假设,以及冷却成本和影响吸收塔成本的化学反应速率的不确定性,都会为氨基二氧化碳捕集系统带来各种各样的成本估算。包括不确定性在内的基于氨的CO2捕集的超临界发电厂的成本为;对于先进的基于胺的CO2捕集技术,对使用ProtreatRTM模拟开发的现有基于胺的响应面模型进行了修改,以匹配性能和成本特征现代基于胺的系统两种技术的响应面模型都被整合到了综合环境控制模型中,用于开发使用这些技术的煤粉和天然气联合循环发电厂的性能和成本估算。具有先进的基于胺的CO2捕集的超临界发电厂的基准成本为;然后比较了两种燃烧后的CO2捕集技术,分别针对不同类型的燃料类型,燃料成本,电厂规模和CO2捕集系统的性能和成本进行了比较。火车的大小。还使用概率成本差异分析来比较这些技术。在所有案例研究中,发现基于胺的CO2捕集系统对收入的要求更高,而在概率成本差异方面,与先进的胺系统相比,只有2%的机会具有较低的收入要求。综合起来,这些结果表明,在大多数情况下,先进的胺系统在氨系统设计上没有显着的新改进的情况下,将比氨系统具有成本优势。最后,讨论了这些估计对决策者的重要性。

著录项

  • 作者

    Versteeg, Peter L.;

  • 作者单位

    Carnegie Mellon University.;

  • 授予单位 Carnegie Mellon University.;
  • 学科 Engineering General.;Engineering Chemical.;Engineering Environmental.
  • 学位 Ph.D.
  • 年度 2012
  • 页码 237 p.
  • 总页数 237
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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