Lead Biosorption by Self-Immobilized Rhizopus nigricans Pellets in a Laboratory Scale Packed Bed Column: Mathematical Model and Experiment

被引:0
作者
Kogej, Adela [1 ]
Likozar, Blaz [1 ]
Pavko, Aleksander [1 ]
机构
[1] Univ Ljubljana, Chair Chem Biochem & Environm Engn, Fac Chem & Chem Technol, SI-1000 Ljubljana, Slovenia
关键词
biosorption; lead; packed bed column; mathematical model; Rhizopus nigricans; BATCH STIRRED-TANK; AQUEOUS-SOLUTIONS; SENSITIVITY-ANALYSIS; HEAVY-METALS; EQUILIBRIUM; BIOMASS; PB(II); ARRHIZUS; REMOVAL; IONS;
D O I
暂无
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
The biosorption of lead ions from aqueous solution on a self-immobilized Rhizopus nigricans biomass has been studied. Experiments were performed in a laboratory scale packed bed column at different liquid flow rates and biosorbent bed heights. Recorded experimental breakthrough curves were compared to those predicted by a mathematical model, which was developed to simulate a packed bed biosorption process by a soft, self-immobilized fungal biosorbent. In the range of examined experimental conditions, the biomass characteristics such as pellet porosity and biosorption capacity substantially affected the predicted response curve. General correlations for the estimation of the intra-pellet effective diffusivity, the external mass transfer coefficient, as well as axial dispersion were successfully applied in this biological system with specific mechanical properties. Under the experimental conditions, mass transfer is controlled by the external film resistance, while the intra-pellet mass transfer resistance, as well as the effect of axial dispersion, can be neglected. A new parameter a, the fraction of active biomass, with an average value of alpha=0.7, was introduced to take into account the specific biomass characteristics, and consequently the observed non-ideal liquid flow through the bed of fungal pellets.
引用
收藏
页码:344 / 351
页数:8
相关论文
共 32 条
  • [21] RIGGS JB, 1994, INTRO NUMERICAL METH, P241
  • [22] RUTHVEN DM, 1984, PRINCIPLES ADSORPTIO, P212
  • [23] Application of equilibrium and mass transfer models to dynamic removal of Cr(VI) ions by Chitin in packed column reactor
    Sag, Y
    Aktay, Y
    [J]. PROCESS BIOCHEMISTRY, 2001, 36 (12) : 1187 - 1197
  • [24] Kinetic and equilibrium studies of biosorption of Pb(II) and Cd(II) from aqueous solution by macrofungus (Amanita rubescens) biomass
    Sari, Ahmet
    Tuzen, Mustafa
    [J]. JOURNAL OF HAZARDOUS MATERIALS, 2009, 164 (2-3) : 1004 - 1011
  • [25] Biosorption of lead (II) from aqueous solution by a bacterial dead Streptomyces rimosus biomass
    Selatnia, A
    Boukazoula, A
    Kechid, N
    Bakhti, MZ
    Chergui, A
    Kerchich, Y
    [J]. BIOCHEMICAL ENGINEERING JOURNAL, 2004, 19 (02) : 127 - 135
  • [26] Tunali Y, 2009, ASIAN J CHEM, V21, P6015
  • [27] Vanysek P., 2008, CRC HDB CHEM PHYS, P5
  • [28] CADMIUM REMOVAL IN A BIOSORPTION COLUMN
    VOLESKY, B
    PRASETYO, I
    [J]. BIOTECHNOLOGY AND BIOENGINEERING, 1994, 43 (11) : 1010 - 1015
  • [29] Biosorption process simulation tools
    Volesky, B
    [J]. HYDROMETALLURGY, 2003, 71 (1-2) : 179 - 190
  • [30] YANG RT, 1997, GAS SEPARATION ADSOR, V1, P141