Fungal biofiltration of toluene on ceramic rings

被引:59
作者
Aizpuru, A
Dunat, B
Christen, P
Auria, R
García-Peña, I
Revah, S
机构
[1] Univ Autonoma Metropolitana Iztapalapa, Proc Engn Dept, Mexico City 09340, DF, Mexico
[2] Univ Pau & Pays Adour, F-65000 Tarbes, France
[3] Univ Autonoma Metropolitana Iztapalapa, Inst Rech Dev France, Mexico City 09340, DF, Mexico
[4] Univ Aix Marseille 1, CESB, ESIL, Inst Rech Dev,Lab IRD Microbiol, F-13288 Marseille 9, France
[5] Univ Autonoma Metropolitana Iztapalapa, Dept Chem Engn, Mexico City 09340, DF, Mexico
关键词
D O I
10.1061/(ASCE)0733-9372(2005)131:3(396)
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Fungal biofilters attain higher toluene elimination. rates compared to bacterial systems. However, strong mycelia growth can cause clogging. In the present work, toluene biofiltration with the fungus Paecilomyces variotii CBS 115145 was tested with two rigid packing materials that allow high mycelia growth. The reactor had two 4.25 L sections, each packed with ceramic Raschig rings differing in water retention capacity and internal porosity. After optimizing nutrient solution delivery, an overall maximum elimination capacity of 245 g/m(3)/h was obtained. Higher elimination capacity (290 g/m(3)/h) was measured in the ceramic ring with lower water content, indicating the interest of such packing material for treating hydrophobic pollutants in fungal biofilters. Additional experiments with this support in a 2 L biofilter showed bacterial contamination, but the fungal activity was responsible for about 70% of the total removal. The support with less humidity showed greater aerial growth, which possibly improves removal efficiency by favoring the direct transfer of pollutants from the gas phase to the microorganism.
引用
收藏
页码:396 / 402
页数:7
相关论文
共 35 条
[1]  
Acuña ME, 1999, BIOTECHNOL BIOENG, V63, P175, DOI 10.1002/(SICI)1097-0290(19990420)63:2<175::AID-BIT6>3.0.CO
[2]  
2-G
[3]   The effect of nutrient concentration on biofilm formation on peat and gas phase toluene biodegradation under biofiltration conditions [J].
Acuña, ME ;
Villanueva, C ;
Cárdenas, B ;
Christen, P ;
Revah, S .
PROCESS BIOCHEMISTRY, 2002, 38 (01) :7-13
[4]   Quantitative structure-activity relationship modeling of biofiltration removal [J].
Aizpuru, A ;
Malhautier, L ;
Fanlo, JL .
JOURNAL OF ENVIRONMENTAL ENGINEERING-ASCE, 2002, 128 (10) :953-959
[5]   Biofiltration of a mixture of volatile organic emissions [J].
Aizpuru, A ;
Malhautier, L ;
Roux, JC ;
Fanlo, JL .
JOURNAL OF THE AIR & WASTE MANAGEMENT ASSOCIATION, 2001, 51 (12) :1662-1670
[6]   DESIGN OF GAS-TREATMENT BIOREACTORS [J].
ANDREWS, GF ;
NOAH, KS .
BIOTECHNOLOGY PROGRESS, 1995, 11 (05) :498-509
[7]   INFLUENCE OF MOLD GROWTH ON THE PRESSURE-DROP IN AERATED SOLID-STATE FERMENTERS [J].
AURIA, R ;
MORALES, M ;
VILLEGAS, E ;
REVAH, S .
BIOTECHNOLOGY AND BIOENGINEERING, 1993, 41 (11) :1007-1013
[8]  
Auria R, 2000, BIOTECHNOL BIOENG, V68, P448, DOI 10.1002/(SICI)1097-0290(20000520)68:4<448::AID-BIT10>3.0.CO
[9]  
2-2
[10]   Biological purification of exhaust air containing toluene vapor in a filter-bed reactor [J].
Bibeau, L ;
Kiared, K ;
Leroux, A ;
Brzezinski, R ;
Viel, G ;
Heitz, M .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1997, 75 (05) :921-929