Influence of biomass pretreatment on co-combustion characteristics with coal and biomass blends

被引:19
作者
Kim, Jong-Ho [1 ]
Jeong, Tae-Yong [1 ]
Yu, Jianglong [2 ,3 ]
Jeon, Chung-Hwan [1 ,4 ]
机构
[1] Pusan Natl Univ, Sch Mech Engn, Busan 46241, South Korea
[2] Univ Sci & Technol Liaoning, Sch Chem Engn, Key Lab Adv Coal & Coking Technol Liaoning Prov, Anshan 114051, Peoples R China
[3] Univ Newcastle, Chem Engn, Callaghan, NSW 2308, Australia
[4] Pusan Natl Univ, Pusan Clean Coal Ctr, Busan 46241, South Korea
关键词
Torrefaction; Ashless technology; NOx emission; Unburned carbon; Char reactivity; PULVERIZED COAL; KINETIC-PARAMETERS; TORREFIED BIOMASS; ALKALI-METALS; COMBUSTION; EMISSIONS; CO2; REACTIVITY; DEPOSITION; BEHAVIOR;
D O I
10.1007/s12206-019-0446-3
中图分类号
TH [机械、仪表工业];
学科分类号
0802 ;
摘要
Fuel blending is one of the most effective ways to use biomass to reduce the use of coal. In this study, co-combustion characteristics including NOx emissions, unburned carbon (UBC), and the char reactivity of coal, biomass, and pretreated biomass blends were investigated by using a lap scale drop tube furnace (DTF) and thermogravimetric analyzer (TGA) to evaluate the availability of pretreated biomass from torrefaction or ashless technology to a pulverized coal boiler. In addition, scanning electron microscopy (SEM) was used to analyze the morphology of biomass and pretreated biomass to observe the physical differences between raw samples and their chars. In the results, NOx showed a linear correlation with the content of inherent fuel-N of biomass except in blending cases with ashless biomass. This indicated that the yields of NOx in these cases were higher than both that of single coal and ashless biomass. In addition, UBC declined with increasing the biomass blending ratio for all blending cases, and this can be explained by examining the fuel ratio and SEM images of the fuel samples. Finally, blends with coal and torrefied biomass showed higher char reactivity and lower activation energy than that with ashless biomass as the blending ratio increased. Overall, this paper indicates that it is better to increase the blending ratio of pretreated biomass than raw biomass up to 30% for enhanced reactivity and reduced emissions.
引用
收藏
页码:2493 / 2501
页数:9
相关论文
共 32 条
  • [1] Kinetic parameters of the intrinsic reactivity of woody biomass and coal chars via thermogravimetric analysis
    Al-Qayim, Khalidah
    Nimmo, William
    Hughes, Kevin
    Pourkashanian, Mohammed
    [J]. FUEL, 2017, 210 : 811 - 825
  • [2] [Anonymous], 2015, 7 BASIC PLAN LONG TE
  • [3] Characterization of lignocellulosic biomass thermal degradation and physiochemical structure: Effects of demineralization by diverse acid solutions
    Asadieraghi, Masoud
    Daud, Wan Mohd Ashri Wan
    [J]. ENERGY CONVERSION AND MANAGEMENT, 2014, 82 : 71 - 82
  • [4] KINETIC PARAMETERS FROM THERMOGRAVIMETRIC DATA .2.
    COATS, AW
    REDFERN, JP
    [J]. JOURNAL OF POLYMER SCIENCE PART B-POLYMER LETTERS, 1965, 3 (11PB): : 917 - &
  • [5] Pulverized coal burnout in blast furnace simulated by a drop tube furnace
    Du, Shan-Wen
    Chen, Wei-Hsin
    Lucas, John A.
    [J]. ENERGY, 2010, 35 (02) : 576 - 581
  • [6] Biomass devolatilization at high temperature under N2 and CO2: Char morphology and reactivity
    Gil, Maria V.
    Riaza, Juan
    Alvarez, Lucia
    Pevida, Covadonga
    Rubiera, Fernando
    [J]. ENERGY, 2015, 91 : 655 - 662
  • [7] Kang N H, 2017, KOREA ENERGY HDB, P11
  • [8] A comparative reactivity and kinetic study on the combustion of coal-biomass char blends
    Kastanaki, E
    Vamvuka, D
    [J]. FUEL, 2006, 85 (09) : 1186 - 1193
  • [9] Effect of Coal Blending Methods with Different Excess Oxygen on Unburned Carbon and NOx Emissions in an Entrained Flow Reactor
    Lee, Byoung-Hwa
    Eddings, Eric G.
    Jeon, Chung-Hwan
    [J]. ENERGY & FUELS, 2012, 26 (11) : 6803 - 6814
  • [10] Influence of Coal Blending Methods on Unburned Carbon and NO Emissions in a Drop-Tube Furnace
    Lee, Byoung-hwa
    Kim, Seoung-gon
    Song, Ju-hun
    Chang, Young-june
    Jeon, Chung-hwan
    [J]. ENERGY & FUELS, 2011, 25 (11) : 5055 - 5062