Performance of Two-Stage Upflow Anaerobic Sludge Blanket Reactor Treating Wastewater from Latex-Processing Factory
Sivawan Phoolphundh, K. Hathaisamit, Somchai Wongwises
Abstract
Sivawan Phoolphundh, K. Hathaisamit, Somchai Wongwises
Abstract
In this study, a relatively high-rate treatment (hydraulic retention time ≤2.5 days) of latex-processing wastewater was achieved in a two-stage upflow anaerobic sludge blanket reactor. A maximum acid production rate of 1.8 g L−1 d−1 acetic acid was obtained when the acidogenic reactor was operated over a hydraulic retention time (HRT) of 4 hr. Total chemical oxygen demand (COD) and sulfate removal efficiencies of the system were 51.6 and 75.9%, respectively, when the methanogenic reactor was operated over an HRT of 24 h. The specific acidogenic activity of granular sludge in the acidogenic and methanogenic reactor varied between 1.33–2.02 g COD g volatile suspended solids (VSS)−1 d−1, and the specific methanogenic activity ranged from 0.0078 to 0.0138 g COD-CH4 g VSS−1 d−1. Microbial diversity monitoring using the denaturing gradient gel electrophoresis technique revealed that there was more sulfate-reducing bacteria in both reactors than archea bacteria.
OpenAlex reports 5 citations for this work. Citation counts describe recorded attention and do not establish research quality.
A contribution statement is not available in the OpenAlex record.
Method details are not available in the OpenAlex metadata.
Findings are not separately available in the OpenAlex metadata.
Limitations are not available in the OpenAlex metadata.
Application details are not available in the OpenAlex metadata.
In this study, a relatively high-rate treatment (hydraulic retention time ≤2.5 days) of latex-processing wastewater was achieved in a two-stage upflow anaerobic sludge blanket reactor. A maximum acid production rate of 1.8 g L−1 d−1 acetic acid was obtained when the acidogenic reactor was operated over a hydraulic retention time (HRT) of 4 hr. Total chemical oxygen demand (COD) and sulfate removal efficiencies of the system were 51.6 and 75.9%, respectively, when the methanogenic reactor was operated over an HRT of 24 h. The specific acidogenic activity of granular sludge in the acidogenic and methanogenic reactor varied between 1.33–2.02 g COD g volatile suspended solids (VSS)−1 d−1, and the specific methanogenic activity ranged from 0.0078 to 0.0138 g COD-CH4 g VSS−1 d−1. Microbial diversity monitoring using the denaturing gradient gel electrophoresis technique revealed that there was more sulfate-reducing bacteria in both reactors than archea bacteria.
Key concepts: Acidogenesis, Hydraulic retention time, Chemical oxygen demand, Chemistry, Wastewater, Pulp and paper industry, Sulfate, Volatile suspended solids