Optimisation of post-combustion CO2 capture for flexible operation

被引:32
|
作者
Mac Dowell, N. [1 ,2 ]
Shah, N. [1 ]
机构
[1] Univ London Imperial Coll Sci Technol & Med, Ctr Proc Syst Engn, London SW7 2AZ, England
[2] Univ London Imperial Coll Sci Technol & Med, Ctr Environm Policy, London SW7 1NA, England
来源
12TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, GHGT-12 | 2014年 / 63卷
关键词
CCS; CO2; capture; flexible CCS; SC-PCC; amine-scrubbing; SAFT; rate-based modelling; dynamic optimisation; POWER-PLANTS; CCS; SOLVENT; COST; DESIGN;
D O I
10.1016/j.egypro.2014.11.162
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
In order to accommodate the increasing penetration of intermittent renewable electricity generation capacity, it is becoming increasingly clear that decarbonized fossil-fired power plants will have to operate in a highly flexible fashion. In this study, using detailed mathematical models of a coal-fired power plant integrated with a MEA-based post-combustion CO2 capture plant, we present a technical and economic analysis of several distinct modes of flexible operation. Using multi-period dynamic optimization techniques, we evaluate solvent storage, exhaust gas venting and time-varying solvent regeneration using average carbon intensity and profitability as key constraints and objective functions, respectively. Load following operation of the power plant with a tightly integrated capture plant is used as our base case scenario. We find that solvent storage is 4% more profitable than the base case, whereas exhaust gas venting is 17% more costly and appears incapable of meeting our decarbonisation targets. Time varying solvent regeneration is 16% more profitable than the base case and the electricity generated has an average carbon intensity which is approximately 5.5% lower than that of the base case. (C) 2014 The Authors. Published by Elsevier Ltd.
引用
收藏
页码:1525 / 1535
页数:11
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