Co-pyrolysis of a coal/biomass blend into biofuel: optimization of operational parameters using central composite design

被引:2
作者
Onay, Ozlem [1 ]
机构
[1] Eskisehir Tech Univ, Porsuk Vocat Sch, TR-26140 Eskisehir, Turkey
来源
BIOFUELS BIOPRODUCTS & BIOREFINING-BIOFPR | 2022年 / 16卷 / 04期
关键词
coal; biomass blends; optimization; pyrolysis; BIO-OIL PRODUCTION; DENSITY POLYETHYLENE; BIOMASS; SIMULATION; WASTE; SLOW;
D O I
10.1002/bbb.2353
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Researchers are attempting to replace fossil and petro-based fuels with renewable and green fuels. Knowing the optimum values of pyrolysis parameters during the production of biofuel from biomass/coal blends is important to obtain biofuel in the desired yield and quality. In this study, a central composite design was used in order to optimize pyrolysis parameters to obtain biofuel from the co-pyrolysis of a coal (lignite)/biomass (pistachio seeds) mixture in a well-swept resistance fixed bed reactor. Knowing the optimum values of different parameters affecting the biofuel yield and quality is very important in terms of the most efficient conditions and the economical production of energy. The effects of some operational parameters, like final temperature (factor A), heating rate (factor B) and percentage of lignite (factor C), were optimized through the central composite design method, and their behaviors were analyzed using analysis of variance. While the linear and quadratic effects of the final temperature and heating rate on the biofuel yield were significant, only the linear effect of the percentage of lignite was found to be important; on the other hand, the effects of the binary interaction between the factors were found to be insignificant. A quadratic equation was proposed to predict the behavior of the process under various conditions with an R-2 of 98.19. The best condition was predicted at a final temperature of 595 degrees C, a heating rate of 458 degrees C/min and a percentage lignite of 16.7% with maximum biofuel yield of 61.23%. (c) 2022 Society of Chemical Industry and John Wiley & Sons, Ltd
引用
收藏
页码:1015 / 1024
页数:10
相关论文
共 50 条
  • [1] Co-pyrolysis of biomass and coal blend by TG and in a free fall reactor
    Cui Quan
    Shaoping Xu
    Yi An
    Xiaolong Liu
    Journal of Thermal Analysis and Calorimetry, 2014, 117 : 817 - 823
  • [2] Co-pyrolysis of biomass and coal blend by TG and in a free fall reactor
    Quan, Cui
    Xu, Shaoping
    An, Yi
    Liu, Xiaolong
    JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2014, 117 (02) : 817 - 823
  • [3] Co-pyrolysis characteristic of biomass and bituminous coal
    Li, Shuaidan
    Chen, Xueli
    Liu, Aibin
    Wang, Li
    Yu, Guangsuo
    BIORESOURCE TECHNOLOGY, 2015, 179 : 414 - 420
  • [4] Product distributions from isothermal co-pyrolysis of coal and biomass
    Weiland, Nathan T.
    Means, Nicholas C.
    Morreale, Bryan D.
    FUEL, 2012, 94 (01) : 563 - 570
  • [5] Co-pyrolysis of Biomass and Pingshuo Coal
    Wang, Jian
    Zhang, Shouyu
    Dong, Aixia
    Guo, Xi
    Chen, Chuan
    Xiong, Shaowu
    2013 INTERNATIONAL CONFERENCE ON MATERIALS FOR RENEWABLE ENERGY AND ENVIRONMENT (ICMREE), VOLS 1-3, 2013, : 694 - 697
  • [6] Predicting co-pyrolysis of coal and biomass using machine learning approaches
    Wei, Hao
    Luo, Kun
    Xing, Jiangkuan
    Fan, Jianren
    FUEL, 2022, 310
  • [7] Co-pyrolysis of biomass and coal in a free fall reactor
    Zhang, Li
    Xu, Shaoping
    Zhao, Wei
    Liu, Shuqin
    FUEL, 2007, 86 (03) : 353 - 359
  • [8] Influence of minerals and added calcium on the pyrolysis and co-pyrolysis of coal and biomass
    Stojanowska, G
    Jones, JM
    JOURNAL OF THE ENERGY INSTITUTE, 2005, 78 (03) : 126 - 138
  • [9] CO-PYROLYSIS OF COAL, BIOMASS AND WASTE PLASTICS
    MIURA, K
    HASHIMOTO, K
    MAE, K
    INOUE, S
    KAGAKU KOGAKU RONBUNSHU, 1994, 20 (06) : 918 - 925
  • [10] Characteristics and application of co-pyrolysis of coal/biomass blends with solid heat carrier
    Guo, Min
    Bi, Ji-Cheng
    FUEL PROCESSING TECHNOLOGY, 2015, 138 : 743 - 749