| Literature DB >> 23994962 |
Xijun Xu1, Chuan Chen1, Duu-Jong Lee2, Aijie Wang1, Wanqian Guo1, Xu Zhou1, Hongliang Guo1, Ye Yuan1, Nanqi Ren3, Jo-Shu Chang4.
Abstract
This study describes the sulfate-reducing (SR) and sulfide-oxidizing (SO) process using Monod-type model with best-fit model parameters both being reported and estimated. The molar ratio of oxygen to sulfide (ROS) significantly affects the kinetics of the SR+SO process. The S(0) is produced by SO step but is later consumed by sulfur-reducing bacteria to lead to "rebound" in sulfide concentration. The model correlated well all experimental data in the present SR+SO tests and the validity of this approach was confirmed by independent sulfur bioreduction tests in four denitrifying sulfide removal (DSR) systems. Modeling results confirm that the ratio of oxygen to sulfide is a key factor for controlling S(0) formation and its bioreduction. Overlooking S(0) bioreduction step would overestimate the yield of S(0).Entities:
Keywords: Data fitting; Kinetic model; Microaeration; Sulfur bioreduction
Mesh:
Substances:
Year: 2013 PMID: 23994962 DOI: 10.1016/j.biortech.2013.07.113
Source DB: PubMed Journal: Bioresour Technol ISSN: 0960-8524 Impact factor: 9.642