• Je něco špatně v tomto záznamu ?

Effect of loading types on performance characteristics of a trickle-bed bioreactor and biofilter during styrene/acetone vapor biofiltration

M. Halecky, J. Paca, E. Kozliak, K. Jones,

. 2016 ; 51 (8) : 669-78. [pub] 20160418

Jazyk angličtina Země Anglie, Velká Británie

Typ dokumentu časopisecké články

Perzistentní odkaz   https://www.medvik.cz/link/bmc17013940

A 2:1 (w/w) mixture of styrene (STY) and acetone (AC) was subjected to lab-scale biofiltration under varied loading in both a trickle bed reactor (TBR) and biofilter (BF) to investigate substrate interactions and determine the limits of biofiltration efficiency of typical binary air pollutant mixtures containing both hydrophobic and polar components. A comparison of the STY/AC mixture degradation in the TBR and BF revealed higher pollutant removal efficiencies and degradation rates in the TBR, with the pollutant concentrations increasing up to the overloading limit. The maximum styrene degradation rates were 12 and 8 gc m(-3) h(-1) for the TBR and BF, respectively. However, the order of performance switched in favor of the BF when the loading was conducted by increasing air flow rate while keeping the inlet styrene concentration (Cin) constant in contrast to loading by increasing Cin. This switch may be due to a drastic difference in the effective surface area between these two reactors, so the biofilter becomes the reactor of choice when the rate-limiting step switches from biochemical processes to mass transfer by changing the loading mode. The presence of acetone in the mixture decreased the efficiency of styrene degradation and its degradation rate at high loadings. When the overloading was lifted by lowering the pollutant inlet concentrations, short-term back-stripping of both substrates in both reactors into the outlet air was observed, with a subsequent gradual recovery taking several hours and days in the BF and TBR, respectively. Removal of excess biomass from the TBR significantly improved the reactor performance. Identification of the cultivable strains, which was performed on Day 763 of continuous operation, showed the presence of 7 G(-) bacteria, 2 G(+) bacteria and 4 fungi. Flies and larvae of Lycoriella nigripes survived half a year of the biofilter operation by feeding on the biofilm resulting in the maintenance of a nearly constant pressure drop.

Citace poskytuje Crossref.org

000      
00000naa a2200000 a 4500
001      
bmc17013940
003      
CZ-PrNML
005      
20170428113320.0
007      
ta
008      
170413s2016 enk f 000 0|eng||
009      
AR
024    7_
$a 10.1080/10934529.2016.1159882 $2 doi
035    __
$a (PubMed)27089477
040    __
$a ABA008 $b cze $d ABA008 $e AACR2
041    0_
$a eng
044    __
$a enk
100    1_
$a Halecky, Martin $u a The University of Chemistry and Technology, Department of Biotechnology , Prague , Czech Republic.
245    10
$a Effect of loading types on performance characteristics of a trickle-bed bioreactor and biofilter during styrene/acetone vapor biofiltration / $c M. Halecky, J. Paca, E. Kozliak, K. Jones,
520    9_
$a A 2:1 (w/w) mixture of styrene (STY) and acetone (AC) was subjected to lab-scale biofiltration under varied loading in both a trickle bed reactor (TBR) and biofilter (BF) to investigate substrate interactions and determine the limits of biofiltration efficiency of typical binary air pollutant mixtures containing both hydrophobic and polar components. A comparison of the STY/AC mixture degradation in the TBR and BF revealed higher pollutant removal efficiencies and degradation rates in the TBR, with the pollutant concentrations increasing up to the overloading limit. The maximum styrene degradation rates were 12 and 8 gc m(-3) h(-1) for the TBR and BF, respectively. However, the order of performance switched in favor of the BF when the loading was conducted by increasing air flow rate while keeping the inlet styrene concentration (Cin) constant in contrast to loading by increasing Cin. This switch may be due to a drastic difference in the effective surface area between these two reactors, so the biofilter becomes the reactor of choice when the rate-limiting step switches from biochemical processes to mass transfer by changing the loading mode. The presence of acetone in the mixture decreased the efficiency of styrene degradation and its degradation rate at high loadings. When the overloading was lifted by lowering the pollutant inlet concentrations, short-term back-stripping of both substrates in both reactors into the outlet air was observed, with a subsequent gradual recovery taking several hours and days in the BF and TBR, respectively. Removal of excess biomass from the TBR significantly improved the reactor performance. Identification of the cultivable strains, which was performed on Day 763 of continuous operation, showed the presence of 7 G(-) bacteria, 2 G(+) bacteria and 4 fungi. Flies and larvae of Lycoriella nigripes survived half a year of the biofilter operation by feeding on the biofilm resulting in the maintenance of a nearly constant pressure drop.
650    _2
$a aceton $x chemie $7 D000096
650    _2
$a látky znečišťující vzduch $x chemie $7 D000393
650    _2
$a znečištění ovzduší $x prevence a kontrola $7 D000397
650    12
$a bioreaktory $7 D019149
650    _2
$a filtrace $x metody $7 D005374
650    _2
$a lidé $7 D006801
650    _2
$a styren $x chemie $7 D020058
655    _2
$a časopisecké články $7 D016428
700    1_
$a Paca, Jan $u a The University of Chemistry and Technology, Department of Biotechnology , Prague , Czech Republic.
700    1_
$a Kozliak, Evguenii $u b Department of Chemistry , University of North Dakota , Grand Forks , North Dakota , USA.
700    1_
$a Jones, Kim $u c South Texas Environmental Institute, Texas A&M University-Kingsville , Kingsville , Texas , USA.
773    0_
$w MED00007280 $t Journal of environmental science and health. Part A, Toxic/hazardous substances & environmental engineering $x 1532-4117 $g Roč. 51, č. 8 (2016), s. 669-78
856    41
$u https://pubmed.ncbi.nlm.nih.gov/27089477 $y Pubmed
910    __
$a ABA008 $b sig $c sign $y a $z 0
990    __
$a 20170413 $b ABA008
991    __
$a 20170428113641 $b ABA008
999    __
$a ok $b bmc $g 1200405 $s 974718
BAS    __
$a 3
BAS    __
$a PreBMC
BMC    __
$a 2016 $b 51 $c 8 $d 669-78 $e 20160418 $i 1532-4117 $m Journal of environmental science and health. Part A, Toxic/hazardous substances and environmental engineering $n J Environ Sci Health Part A Tox Hazard Subst Environ Eng $x MED00007280
LZP    __
$a Pubmed-20170413

Najít záznam

Citační ukazatele

Nahrávání dat ...

Možnosti archivace

Nahrávání dat ...