Sugarcane Bagasse Torrefaction for Fluidized Bed Gasification

被引:7
|
作者
Pedroso, Daniel Travieso [1 ,2 ]
Machin, Einara Blanco [3 ]
Cabrera-Barjas, Gustavo [2 ]
Flores, Mauricio [2 ]
Urra, Hector Grandon [2 ]
de Carvalho, Felipe Solferini [4 ]
dos Santos, Maria Isabel Silva [5 ]
Machin, Adrian Blanco [5 ]
Canettieri, Eliana Vieira [5 ]
Perez, Nestor Proenza [6 ]
Teixeira Lacava, Pedro [4 ]
Ribeiro dos Santos, Leila [4 ]
Andrade de Carvalho Junior, Joao [5 ]
机构
[1] Univ Bio Bio, Fac Ingn, Dept Ingn Mecan, Concepcion 4030000, Chile
[2] Univ Concepcion, Unidad Desarrollo Tecnol, Concepcion 4030000, Chile
[3] Univ Concepcion, Fac Ingn, Dept Ingn Mecan, Concepcion 4030000, Chile
[4] Technol Inst Aeronaut ITA, Lab Combust Prop & Energy, BR-12228900 Sao Jose Dos Campos, Brazil
[5] Sao Paulo State Univ UNESP, Fac Engn Guaratingueta, Dept Energy, BR-12236130 Guaratingueta, Brazil
[6] Fed Ctr Technol Educ Celso Suckow Fonseca CEFET R, BR-23953030 Angra Dos Reis, Brazil
来源
APPLIED SCIENCES-BASEL | 2021年 / 11卷 / 13期
基金
巴西圣保罗研究基金会;
关键词
sugarcane bagasse; torrefaction; biomass; gasification; entrained flow gasifier; CANE RESIDUE; PART; PYROLYSIS; COMBUSTION; KINETICS; SYSTEM;
D O I
10.3390/app11136105
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Sugarcane bagasse has a great potential to be used as biofuel; however, its use as feedstock in fluidized bed reactors is hampered due to its fibrous nature, low apparent density, high moisture content, and difficulties with its fluidization. The present study evaluated the torrefaction of sugarcane bagasse to propose suitable process conditions that balance the properties of the fuel obtained in the torrefaction and the process's energy requirements. Based on the thermogravimetric analysis and previous reports, two final process temperatures (230 degrees C and 280 degrees C) and residence times (35 and 45 min) for the same heating rate (5 degrees C/min) and nitrogen flow (1 L/min) were evaluated. Within the experimental conditions evaluated, it can be concluded that for 30 min of residence time, the average target temperature of 230 degrees C should be high enough to produce a stable torrefacted bagasse with a 3.41% reduction in the volatile content and obtain 98.85% of energy yield. Higher temperatures increase the feedstock's carbon content and energy density, but the reduction in energy yield and the fraction of volatiles do not justify higher temperatures or longer residence times for pretreating the sugarcane bagasse.
引用
收藏
页数:14
相关论文
共 50 条
  • [21] Effect of Torrefaction on Steam Gasification of Biomass in Dual Fluidized Bed Reactor—a Process Simulation Study
    Quang-Vu Bach
    Dinh Duc Nguyen
    Chul-Jin Lee
    BioEnergy Research, 2019, 12 : 1042 - 1051
  • [22] Fluidized bed gasification of coal
    Can J Chem Eng, 2 (204):
  • [23] GAS-FLUIDIZED BED TORREFACTION OF COFFEE
    ARJONA, JL
    RIOS, GM
    GIBERT, H
    VINCENT, JC
    CAFE CACAO THE, 1979, 23 (02): : 119 - 128
  • [24] Effect of Torrefaction on Steam Gasification of Biomass in Dual Fluidized Bed Reactor-a Process Simulation Study
    Quang-Vu Bach
    Dinh Duc Nguyen
    Lee, Chul-Jin
    BIOENERGY RESEARCH, 2019, 12 (04) : 1042 - 1051
  • [25] Sewage sludge torrefaction in a fluidized bed reactor
    Atienza-Martinez, M.
    Fonts, I.
    Abrego, J.
    Ceamanos, J.
    Gea, G.
    CHEMICAL ENGINEERING JOURNAL, 2013, 222 : 534 - 545
  • [26] Sewage sludge torrefaction in a fluidized bed reactor
    Atienza-Martínez, M. (atienza@unizar.es), 1600, Elsevier B.V., Netherlands (222):
  • [27] Effect of Dry Torrefaction on Kinetics of Catalytic Pyrolysis of Sugarcane Bagasse
    Daniyanto
    Sutijan
    Deendarlianto
    Budiman, Arief
    INTERNATIONAL CONFERENCE OF CHEMICAL AND MATERIAL ENGINEERING (ICCME) 2015: GREEN TECHNOLOGY FOR SUSTAINABLE CHEMICAL PRODUCTS AND PROCESSES, 2015, 1699
  • [28] Study of reactivity reduction in sugarcane bagasse as consequence of a torrefaction process
    Granados, D. A.
    Ruiz, R. A.
    Vega, L. Y.
    Chejne, F.
    ENERGY, 2017, 139 : 818 - 827
  • [30] Comparison of Sugarcane Bagasse Conversion to Syngas in Downdraft and Fluidized Bed Gasifier Using ASPEN PLUS
    Nurtono, Tantular
    Agung, Fransiskus Budi Kurnia
    Indriani, Magistra Dwinovia
    Nanda, Hendiyansa Dwi
    Jayanti, Indita Rizky
    Winardi, Sugeng
    PROCEEDINGS OF THE 2ND INTERNATIONAL CONFERENCE ON CHEMICAL PROCESS AND PRODUCT ENGINEERING (ICCPPE) 2019, 2020, 2197