Catalyzed pyrolysis of grape and olive bagasse. Influence of catalyst type and chemical treatment

被引:74
作者
Encinar, JM
Beltran, FJ
Ramiro, A
Gonzalez, JF
机构
[1] Depto. de Ing. Química, Universidad de Extremadura
关键词
D O I
10.1021/ie960795b
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Catalyzed pyrolysis of grape and olive bagasse under different experimental conditions has been studied. Variables investigated were temperature and type and concentration of catalysts. Experiments were carried out in an isothermal manner. Products of pyrolysis are gases (Hz, CO, CO2, and CH4), liquids (methanol, acetone, furfurylic alcohol, phenol, furfural, naphthalene, and o-cresol), and solids (chars). Temperature is a significant variable, yielding increases of fixed carbon content, gases, and to a lesser extent, ash percentage. Catalyst presence also yields increases of solid phase content, but the amount of Liquid components decrease. Among catalysts applied those of Fe and Zn are the most advisable to obtain gases. Chemical treatment of bagasses with sulfuric or phosphoric acid washing leads to lower char yields, although fixed carbon content is higher and ash presence diminishes with respect to catalyst pyrolysis without chemical pretreatment. A pyrolysis kinetic study based on gas generation from thermal decomposition of residues has been carried out. From the model proposed, rate constants for the formation of each gas, reaction order of the catalyst, and activation energies were determined.
引用
收藏
页码:4176 / 4183
页数:8
相关论文
共 29 条
  • [1] ALDEN H, 1988, RESEARCH IN THERMOCHEMICAL BIOMASS CONVERSION, P987
  • [2] [Anonymous], ORGANIC CHEM BIOMASS
  • [3] EFFECTS OF REACTOR SEVERITY ON THE GAS-PHASE PYROLYSIS OF CELULOSE-DERIVED AND KRAFT LIGNIN-DERIVED VOLATILE MATTER
    ANTAL, MJ
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1983, 22 (02): : 366 - 375
  • [4] INFLUENCE OF PHYSICAL AND CHEMICAL-PARAMETERS ON WOOD PYROLYSIS
    BEAUMONT, O
    SCHWOB, Y
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1984, 23 (04): : 637 - 641
  • [5] BEVIA FR, 1984, IND ENG CHEM PROD RD, V23, P269
  • [6] BIOMASS PYROLYSIS WITH AN ENTRAINED FLOW REACTOR
    BOHN, MS
    BENHAM, CB
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1984, 23 (02): : 355 - 363
  • [7] PRODUCT YIELDS AND KINETICS FROM THE VAPOR-PHASE CRACKING OF WOOD PYROLYSIS TARS
    BOROSON, ML
    HOWARD, JB
    LONGWELL, JP
    PETERS, WA
    [J]. AICHE JOURNAL, 1989, 35 (01) : 120 - 128
  • [8] Bridgwater AV, 1993, Advances in thermochemical biomass conversion, V1st
  • [9] CHEMBUKULAM KS, 1981, IND ENG CHEM PROC DD, V20, P7
  • [10] CHENG KT, 1979, ATOM DATA NUCL DATA, V24, P11