Techno-economic evaluation of an ammonia-based post-combustion process integrated with a state-of-the-art coal-fired power plant

被引:19
作者
Jilvero, Henrik [1 ]
Eldrup, Nils-Henrik [2 ]
Normann, Fredrik [1 ]
Andersson, Klas [1 ]
Johnsson, Filip [1 ]
Skagestad, Ragnhild [2 ]
机构
[1] Chalmers Univ Technol, Dept Energy & Environm, S-41296 Gothenburg, Sweden
[2] Tel Tek, N-3901 Porsgrunn, Norway
关键词
Post-combustion; CO2; capture; Ammonia; Coal power plant; CAPEX; OPEX; AQUEOUS AMMONIA; CO2; CAPTURE; COST; CCS;
D O I
10.1016/j.ijggc.2014.09.023
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A techno-economic evaluation of the application of an ammonia-based post-combustion CO2 capture system to an existing, state-of-the-art, coal-fired power plant. The study comprised an assessment of the ammonia based capture process together with a detailed cost analysis, based on which the overall design of the capture process is presented, including a power plant integration strategy and estimates of the specific CO2 capture cost ((sic)/tCO(2)). The evaluations of the power plant and the CO2 capture plant were based on process modeling. The cost analysis was based on the installed cost of each unit in the equipment list derived from the process simulation, which was determined using detailed-factor estimation. We show that the steam required for a CO2 capture efficiency of 90% lowers the electric output from 408.0 MWel to 341.8 MWel. The capital expenditure related to the retrofit of the reference power plant with CO2 capture is 230M(sic) and the operating expenditure is determined to be 66.5M(sic)/year, corresponding to a relative capture cost of 35(sic)/tCO(2). Furthermore, the present work proposes design improvements that may reduce the cost of capture to 31(sic)/tCO(2). (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:87 / 95
页数:9
相关论文
共 23 条
  • [1] Process simulation of aqueous MEA plants for post-combustion capture from coal-fired power plants
    Ahn, Hyungwoong
    Luberti, Mauro
    Liu, Zhengyi
    Brandani, Stefano
    [J]. GHGT-11, 2013, 37 : 1523 - 1531
  • [2] ARNOLD DS, 1982, OIL GAS J, V80, P130
  • [3] Calvert S., 1972, SCRUBBER HDB, V1
  • [4] CO2 capture using aqueous ammonia: kinetic study and process simulation
    Darde, Victor
    van Well, Willy J. M.
    Stenby, Erling H.
    Thomsen, Kaj
    [J]. 10TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, 2011, 4 : 1443 - 1450
  • [5] European Commission, 2013, 2 QUART 2013 2013, V6
  • [6] Jilvero H., 2014, INT J GREENH G UNPUB
  • [7] Jilvero H., 2014, 12 C GREENH GAS CONT
  • [8] The Rate of CO2 Absorption in Ammonia-Implications on Absorber Design
    Jilvero, Henrik
    Normann, Fredrik
    Andersson, Klas
    Johnsson, Filip
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2014, 53 (16) : 6750 - 6758
  • [9] Heat requirement for regeneration of aqueous ammonia in post-combustion carbon dioxide capture
    Jilvero, Henrik
    Normann, Fredrik
    Andersson, Klas
    Johnsson, Filip
    [J]. INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2012, 11 : 181 - 187
  • [10] Thermal Integration and Modelling of the Chilled Ammonia Process
    Jilvero, Henrik
    Normann, Fredrik
    Andersson, Klas
    Johnsson, Filip
    [J]. 10TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, 2011, 4 : 1713 - 1720