Global S&T Development Trend Analysis Platform of Resources and Environment
DOI | 10.2172/1131945 |
报告编号 | None |
来源ID | OSTI ID: 1131945 |
Bench-Scale Silicone Process for Low-Cost CO{sub 2} Capture | |
Wood, Benjamin; Genovese, Sarah; Perry, Robert; Spiry, Irina; Farnum, Rachael; Sing, Surinder; Wilson, Paul; Buckley, Paul; Acharya, Harish; Chen, Wei; McDermott, John; Vipperia, Ravikumar; Yee, Michael; Steele, Ray; Fresia, Megan; Vogt, Kirk | |
2013-12-31 | |
出版年 | 2013 |
语种 | 英语 |
国家 | 美国 |
领域 | 地球科学 |
英文摘要 | A bench-scale system was designed and built to test an aminosilicone-based solvent. A model was built of the bench-scale system and this model was scaled up to model the performance of a carbon capture unit, using aminosilicones, for CO{sub 2} capture and sequestration (CCS) for a pulverized coal (PC) boiler at 550 MW. System and economic analysis for the carbon capture unit demonstrates that the aminosilicone solvent has significant advantages relative to a monoethanol amine (MEA)-based system. The CCS energy penalty for MEA is 35.9% and the energy penalty for aminosilicone solvent is 30.4% using a steam temperature of 395 °C (743 °F). If the steam temperature is lowered to 204 °C (400 °F), the energy penalty for the aminosilicone solvent is reduced to 29%. The increase in cost of electricity (COE) over the non-capture case for MEA is ~109% and increase in COE for aminosilicone solvent is ~98 to 103% depending on the solvent cost at a steam temperature of 395 °C (743 °F). If the steam temperature is lowered to 204 °C (400 °F), the increase in COE for the aminosilicone solvent is reduced to ~95-100%. |
URL | 查看原文 |
来源平台 | US Department of Energy (DOE) |
引用统计 | |
文献类型 | 科技报告 |
条目标识符 | http://119.78.100.173/C666/handle/2XK7JSWQ/6004 |
专题 | 地球科学 |
推荐引用方式 GB/T 7714 | Wood, Benjamin,Genovese, Sarah,Perry, Robert,et al. Bench-Scale Silicone Process for Low-Cost CO{sub 2} Capture,2013. |
条目包含的文件 | 条目无相关文件。 |
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