Environmental Biotechnology

Electronic Journal of Biotechnology ISSN: 0717-3458 Vol. 8 No. 3, Issue of December 15, 2005
© 2005 by Pontificia Universidad Católica de Valparaíso -- Chile Received November 3, 2004 / Accepted June 22, 2005
DOI: 10.2225/vol8-issue3-fulltext-5  
RESEARCH ARTICLE

Resistance of diethylenetriaminepentaacetic acid to anaerobic biodegradation

Evelyn Alarcón
Environmental Science Center EULA-Chile
Universidad de Concepción
P.O. Box 160-C
Concepción, Chile

Jacqueline Decap
Environmental Science Center EULA-Chile
Universidad de Concepción
P.O. Box 160-C
Concepción, Chile

Gladys Vidal*
Environmental Science Center EULA-Chile
Universidad de Concepción
P.O. Box 160-C
Concepción, Chile
Fax: 56 41 204067
E-mail: glvidal@udec.cl

*Corresponding author


Financial support: FONDECYT Grants 1010644 and 1040987.

Keywords: anaerobic biodegradation, DTPA, kraft mill effluent.

Abbreviations:  

AF: Anaerobic filter
BOD5: Biological Oxygen Demand
COD: Chemical Oxygen Demand
DPTA: diethylenetriaminepentaacetic acid
HRT: Hidraulic Retention Time
IA: Intermediate Alkalinity
LRDPTA: DPTA Load Rate
EDTA: ethylenediaminetetraacetic acid
OLR: Organic Load Rate
TA: Total Alkalinity
TCF: Total Chlorine Free
VFA: Volatile Fatty Acids
VSS: Volatile Suspended Solid


Abstract
Full Text

Kraft mills are responsible for the massive discharge of highly polluted effluents, and new bleaching processes (i.e. Total Chlorine Free (TCF)) is presented as a feasible option to reduce this environmental impact. However, increased TCF pulp production is accompanied by an increase in chelate use. The most commonly used chelates, ethylenediaminetetraacetic acid (EDTA) and diethylenetriaminepentaacetic acid (DPTA), are considered to be relatively persistent substances in water treatment plants, and consequently environmentally critical compounds.

The purpose of this work is to investigate DPTA behaviour in an anaerobic system. An Anaerobic filter (AF) was operated with three different DPTA load rates (LRDPTA = 0.07 - 0.28 gDPTA/L×d), and the operating strategy was to maintain the anaerobic system stable during the entire operation (alkalinity ratio below 0.3). The AF's maximum Chemical Oxygen Demand (COD) removal was 59%, whereas the Biological Oxygen Demand (BOD5) was around 95%. However, only 5% of DPTA removal was observed under anaerobic conditions during the first operating period. Scanning electronic microscopy indicates that the operating system reduced microorganism biodiversity.

 
Supported by UNESCO / MIRCEN network