Performance and costs of advanced sustainable central power plants with CCS and H2 co-production

被引:57
作者
Li, Mu [1 ]
Rao, Ashok D. [1 ]
Samuelsen, G. Scott [1 ]
机构
[1] Univ Calif Irvine, Adv Power & Energy Program, Irvine, CA 92697 USA
基金
美国国家科学基金会;
关键词
Hydrogen coproduction; IGCC; IGFC; SOFC; Catalytic hydro-gasification; CO2; capture; COMMERCIALLY READY TECHNOLOGY; THERMODYNAMIC ANALYSIS; HYDROGEN; COAL; ELECTRICITY; CO2;
D O I
10.1016/j.apenergy.2011.09.009
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
With increasing concerns over global climate change caused by GHG emissions, carbon capture and storage (CCS) has become imperative for coal based power plants. Meanwhile, with the development and deployment of hybrid vehicles, electric vehicles, and alternative fuel vehicles, GHG reduction efforts in the power industry can also benefit the transportation sector. Power plants with H-2 co-production capability can contribute significantly in such development trends because H-2 powered fuel cell hybrid vehicles are very promising for future "zero emissions vehicles". This work investigates the thermodynamic performance and cost advantage of employing advanced technologies currently under development for central power plants that (1) employ coal and biomass as feed stock; (2) co-produce power and high purity H-2; (3) capture most of the CO2 evolved within the plants. Two system designs are developed: the first "base" case is an integrated gasification combined cycle (IGCC) system consisting of commercially ready technologies; the second "advanced" case is an integrated gasification fuel cell (IGFC) system. The feedstock employed consists of Utah bituminous coal along with two typical biomass resources, corn stover and cereal straw. The IGFC plant produces significantly higher amount of electricity for the same amounts of feedstock and H-2 export while the cost of producing the H-2 using a cost of electricity of $135/MW h is $1178/tonne for the IGFC case versus $2620/tonne for the IGCC case. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:43 / 50
页数:8
相关论文
共 19 条
  • [1] [Anonymous], [No title captured]
  • [2] Hydrogen from biomass - Present scenario and future prospects
    Balat, Havva
    Kirtay, Elif
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2010, 35 (14) : 7416 - 7426
  • [3] Co-production of hydrogen, electricity and CO2 from coal with commercially ready technology.: PartA:: Performance and emissions
    Chiesa, P
    Consonni, S
    Kreutz, T
    Williams, R
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2005, 30 (07) : 747 - 767
  • [4] HENRICH E, 2008, PROGR THERMOCHEMICAL
  • [5] KLRTAY E, 2011, ENERG CONVERS MANAGE, V52, P1778
  • [6] Kreutz T, 2005, INT J HYDROGEN ENERG, V30, P769, DOI 10.1016/j.ijhydene.2004.08.001
  • [7] A thermodynamic analysis of electricity and hydrogen co-production using a solid oxide fuel cell
    Leal, Elisangela M.
    Brouwer, Jack
    [J]. JOURNAL OF FUEL CELL SCIENCE AND TECHNOLOGY, 2006, 3 (02): : 137 - 143
  • [8] Effects of carbon capture on the performance of an advanced coal-based integrated gasification fuel cell system
    Li, M.
    Rao, A. D.
    Brouwer, J.
    Samuelsen, G. S.
    [J]. PROCEEDINGS OF THE INSTITUTION OF MECHANICAL ENGINEERS PART A-JOURNAL OF POWER AND ENERGY, 2011, 225 (A2) : 208 - 218
  • [9] Application of a detailed dimensional solid oxide fuel cell model in integrated gasification fuel cell system design and analysis
    Li, Mu
    Brouwer, Jacob
    Rao, Ashok D.
    Samuelsen, G. Scott
    [J]. JOURNAL OF POWER SOURCES, 2011, 196 (14) : 5903 - 5912
  • [10] Design of highly efficient coal-based integrated gasification fuel cell power plants
    Li, Mu
    Rao, Ashok D.
    Brouwer, Jacob
    Samuelsen, G. Scott
    [J]. JOURNAL OF POWER SOURCES, 2010, 195 (17) : 5707 - 5718