J 2015

A two-stage combined trickle bed reactor/biofilter for treatment of styrene/acetone vapor mixtures

VANEK, Tomas, Martin HALECKY, Jan PÁCA, Lubos ZAPOTOCKY, Tereza GELBÍČOVÁ et. al.

Basic information

Original name

A two-stage combined trickle bed reactor/biofilter for treatment of styrene/acetone vapor mixtures

Authors

VANEK, Tomas (203 Czech Republic), Martin HALECKY (203 Czech Republic), Jan PÁCA (203 Czech Republic, guarantor), Lubos ZAPOTOCKY (203 Czech Republic), Tereza GELBÍČOVÁ (203 Czech Republic, belonging to the institution), Renata VADKERTIOVA (703 Slovakia), Evguenii KOZLIAK (840 United States of America) and Kim JONES (840 United States of America)

Edition

Journal of Environmental Science and Health Part A Toxic/Hazardous Substances & Environmental Engineering, 2015, 1093-4529

Other information

Language

English

Type of outcome

Článek v odborném periodiku

Field of Study

Biotechnology and bionics

Country of publisher

United States of America

Confidentiality degree

není předmětem státního či obchodního tajemství

Impact factor

Impact factor: 1.276

RIV identification code

RIV/00216224:14310/15:00083573

Organization unit

Faculty of Science

UT WoS

000359339900007

Keywords in English

acetone; biofiltration; biofilm identification; intermediates; styrene; two-stage reactor

Tags

Změněno: 24/3/2016 14:38, Ing. Andrea Mikešková

Abstract

V originále

Performance of a two-stage biofiltration system was investigated for removal of styrene-acetone mixtures. High steady-state acetone loadings resulted in a significant inhibition of the system’s performance in both acetone and styrene removal. This inhibition was shown to result from the acetone accumulation within the upstream trickle-bed bioreactor (TBR) circulating mineral medium, which was observed by direct chromatographic measurements. Placing a biofilter (BF) downstream to this TBR overcomes the inhibition as long as the biofilter has a sufficient bed height. A different kind of inhibition of styrene biodegradation was observed within the biofilter at very high acetone loadings. In addition to steady-state measurements, dynamic tests confirmed that the reactor overloading can be readily overcome, once the accumulated acetone in the TBR fluids is degraded. No sizable metabolite accumulation in the medium was observed for either TBR or BF. Analyses of the biodegradation activities of microbial isolates from the biofilm corroborated the trends observed for the two-stage biofiltration system, particularly the occurrence of an inhibition threshold by excess acetone.