Chemical looping combustion oxygen carrier production cost study

被引:5
作者
Newby, Richard A. [1 ,2 ]
Keairns, Dale L. [1 ,3 ]
Stevens, Robert W. [1 ]
机构
[1] US DOE, Natl Energy Technol Lab NETL, 3610 Collins Ferry Rd, Morgantown, WV 26505 USA
[2] KeyLog Mission Execut & Strateg Anal MESA, 626 Cochran Mill Rd, Pittsburgh, PA 15236 USA
[3] Deloitte Consulting Mission Execut & Strateg Anal, 626 Cochran Mill Rd, Pittsburgh, PA 15236 USA
关键词
Coal; Oxygen carrier; Production; Chemical looping combustion; Power generation; Cost; HYDROGEN-PRODUCTION; PROGRESS;
D O I
10.1016/j.apenergy.2023.121293
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
The objective of this study was to estimate the cost of commercial production of oxygen carriers (OCs) for large-scale application in a mature, chemical looping combustion (CLC) power generation industry. Estimates of cost were made for two production facility scenarios: (1) build and operate an on-site, OC production facility located at a 550 MW CLC power plant site; and (2) build and operate a central production facility to produce and distribute OCs to the U.S. CLC power generation industry. Two OC production techniques were addressed: mechanical mixing and co-precipitation. Representative OCs that have production raw materials with sufficient commercial availability to support a CLC industry are ilmenite, a natural OC, and four engineered OC types, Fe2O3-based, CuO-based, NiO-based, and CuFeAlO4-based, with candidate OC support materials Al2O3 and TiO2. The costs of the OC production raw materials represent the major portion of the OC product cost; the OC pro-duction cost, in dollars per kg, has been found to be nearly a linear function of the OC raw materials cost, in dollars per kg. The estimated OC product costs can be used to estimate the maximum OC loss rate yielding a designated CLC power plant cost-of-electricity (COE) target as a development guide, and it has been found that the maximum OC makeup rate, in kg per hour, achieving a designated COE reduction goal relative to a con-ventional pulverized coal (PC) power plant, will be nearly inversely proportional to the OC production raw materials cost, in dollars per kg.
引用
收藏
页数:13
相关论文
共 40 条
  • [1] Kinetics of redox reactions of ilmenite for chemical-looping combustion
    Abad, Alberto
    Adanez, Juan
    Cuadrat, Ana
    Garcia-Labiano, Francisco
    Gayan, Pilar
    de Diego, Luis F.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2011, 66 (04) : 689 - 702
  • [2] Spanning the flow regimes: Generic fluidized-bed reactor model
    Abba, IA
    Grace, JR
    Bi, HT
    Thompson, ML
    [J]. AICHE JOURNAL, 2003, 49 (07) : 1838 - 1848
  • [3] Chemical looping combustion of solid fuels
    Adanez, J.
    Abad, A.
    Mendiara, T.
    Gayan, P.
    de Diego, L. F.
    Garcia-Labiano, F.
    [J]. PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2018, 65 : 6 - 66
  • [4] Progress in Chemical-Looping Combustion and Reforming technologies
    Adanez, Juan
    Abad, Alberto
    Garcia-Labiano, Francisco
    Gayan, Pilar
    de Diego, Luis F.
    [J]. PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2012, 38 (02) : 215 - 282
  • [5] [Anonymous], 2018, INFOMINE COMM MET PR
  • [6] [Anonymous], MET
  • [7] [Anonymous], AL MIN MET
  • [8] Heterogeneous Catalyst Deactivation and Regeneration: A Review
    Argyle, Morris D.
    Bartholomew, Calvin H.
    [J]. CATALYSTS, 2015, 5 (01) : 145 - 269
  • [9] Babcock & Wilcox Company, 2013, FE009761 DOE BABC WI
  • [10] Brannan C, 2005, RULES THUMB CHEM ENG