Please use this identifier to cite or link to this item: http://hdl.handle.net/10125/58962

Integrating an anaerobic Bio-nest and an aerobic EMMC process as pretreatment of dairy wastewater for reuse: a pilot plant study

Item Summary

Title:Integrating an anaerobic Bio-nest and an aerobic EMMC process as pretreatment of dairy wastewater for reuse: a pilot plant study
Authors:Kongsil, Piyalerg
Irvine, Joshua Lelemia
Yang, Ping-Yi
Keywords:Anaerobi Bio-nest
Biogas
Dairy wastewater
Entrapped mixed microbial cell
Existing lagoon
Date Issued:Apr 2009
Abstract:A large dairy farm located on the island of
Oahu, Hawaii was the site for an investigation for the
potential integration of the existing facultative lagoon
system with a cost effective pretreatment unit process.
Based on the results from a laboratory study, a pilot plant
was installed with two anaerobic bioreactors (10 m3 each)
and one aerobic reactor (3.8 m3

). Two layers of media
‘‘Bio-nest,’’ providing a void volume of 98%, were placed
into each anaerobic bioreactor with 19% space-based on
the bioreactor water volume. For better performance and
reduction of shock-load, the equalization/settling tank was
employed prior to the first anaerobic Bio-nest reactor. The intermediate holding tank settled effluent suspended solids from the Bio-nest reactor and adjusted the loading rate in order to improve the performance of the aerobic EMMC (entrapped mixed microbial cell) bioreactors. Based on the start-up operation of the Bio-nest system at an organic loading rate of about 1.5 g TCOD/l/day, the production rate of biogas from the first and second Bio-nest reactors was 0.64 and 0.15 l/l/day, respectively. This indicates that the anaerobic degradation of organics occurs mainly in the first Bio-nest reactor due to the low loading rate. The removal efficiency from the Bio-nest system shows TCOD removal of about 70%. The EMMC process provided fur-
ther treatment to achieve a removal efficiency of TCOD at about 50% and a TN of about 35%. The cost for these pretreatments in order to be integrated with the existing lagoon system is US $1.1 per 1,000 gallons (3.8 m3) for dairy wastewater and $91 for each ton of TCOD removal. This integration system provides a sustainable improvement of environment and agricultural production.
URI:http://hdl.handle.net/10125/58962
Rights:An error occurred on the license name.
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Appears in Collections: Irvine, Joshua Lelemia


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