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.
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页数:13
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共 40 条
  • [31] Present status and overview of Chemical Looping Combustion technology
    Nandy, Anirban
    Loha, Chanchal
    Gu, Sai
    Sarkar, Pinaki
    Karmakar, Malay K.
    Chatterjee, Pradip K.
    [J]. RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2016, 59 : 597 - 619
  • [32] National Energy Technology Laboratory, 2015, DOENETL20151723, V1a
  • [33] Recent developments in oxygen carrier materials for hydrogen production via chemical looping processes
    Protasova, Lidia
    Snijkers, Frans
    [J]. FUEL, 2016, 181 : 75 - 93
  • [34] Experimental and kinetic analysis for particle scale modeling of a CuO-Fe2O3-Al2O3 oxygen carrier during reduction with H2 in chemical looping combustion applications
    Riley, Jarrett
    Siriwardane, Ranjani
    Tian, Hanjing
    Benincosa, William
    Poston, James
    [J]. APPLIED ENERGY, 2018, 228 : 1515 - 1530
  • [35] Progress in oxygen carrier development of methane-based chemical-looping reforming: A review
    Tang, Mingchen
    Xu, Long
    Fan, Maohong
    [J]. APPLIED ENERGY, 2015, 151 : 143 - 156
  • [36] vale, VAL BUS
  • [37] Walas S, 1989, CHEM PROCESS EQUIPME
  • [38] Woods D.R., 2007, Rules of Thumb in Engineering Practice, DOI DOI 10.1002/9783527611119
  • [39] worldfeightrates, WORLD FREIGHT RAT FR
  • [40] Chemical looping processes - particle characterization, ionic diffusion-reaction mechanism and reactor engineering
    Zeng, Liang
    Luo, Siwei
    Sridhar, Deepak
    Fan, Liang-Shih
    [J]. REVIEWS IN CHEMICAL ENGINEERING, 2012, 28 (01) : 1 - 42