Chemical Looping Combustion of different types of biomass in a 0.5 kWth unit

被引:65
|
作者
Mendiara, T. [1 ]
Perez-Astray, A. [1 ]
Izquierdo, M. T. [1 ]
Abad, A. [1 ]
de Diego, L. F. [1 ]
Garcia-Labiano, F. [1 ]
Gayan, P. [1 ]
Adanez, J. [1 ]
机构
[1] Inst Carboquim ICB CSIC, Dept Energy & Environm, Miguel Luesma Castan 4, Zaragoza 50018, Spain
关键词
NETs; BECCS; Chemical Looping Combustion (CLC); Biomass; Low-cost oxygen carrier; Tar; OXYGEN-CARRIER; SOLID FUELS; IRON-ORE; FLUIDIZED-BED; CO2; CAPTURE; LARGE-SCALE; SYSTEM; EXPERIENCE; ILMENITE; STORAGE;
D O I
10.1016/j.fuel.2017.09.113
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
Chemical Looping Combustion (CLC) using renewable solid fuels appears as an important option to reach negative carbon emissions. In this work, three types of forest and agricultural residues (pine sawdust, olive stone and almond shell) were tested between 900-980 degrees C in a 0.5 kW(th) unit with an iron ore as oxygen carrier (Tierga ore) working under In situ Gasification-Chemical Looping Combustion (iG-CLC) mode. Specific solids inventories lower than 1000 kg/MWth were tested as they were consider more representative of what can be used in a larger CLC unit. CO2 represented about 70% in the fuel reactor outlet gas stream, followed by unburnt compounds: H-2, CO and CH4. CO2 capture efficiencies increased with the fuel reactor temperature achieving almost 100% of capture with the three biomasses at temperatures above 950 degrees C. In contrast, no clear trend with the fuel reactor temperature was observed for the total oxygen demand, achieving values about 25%. The major contribution to this value comes from the unburned volatiles with a small contribution coming from tar (approximate to 1%). Regarding tar, naphthalene was the major compound found at the different operating conditions. The present results support the consideration of the CLC process with biomass (bio-CLC) as a promising Bio-Energy with Carbon Capture (BECCS) technology.
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页码:868 / 875
页数:8
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