Development of a model for PHA-based denitrification in a packed bed reactor
Document Type
Article
Publication Date
1-1-2014
Abstract
A model of the denitrification on a polyhydroxyalkanoate (PHA) based reactor for recirculating aquaculture was developed. PHA is a family of non-water soluble bioplastics produced by bacteria. The PHA formulation used in this work was polyhydroxybutyrate (PHB). The model considered nitrate concentration, dissolved oxygen, organic carbon and biomass concentration as the most significant variables. The developed model represents adequately the nitrate reduction with the medium used, for nitrate under 100ppm NO3--N. In the conditions tested, an average ratio of 2.92g PHA to 1gNO3--N reduced was found. The model results showed a denitrification rate of 2.97kgm-3d-1 for ranges from 10 to 50mgNO3--NL-1. Using this model as a management tool, the required size of denitrification units and PHA recharging time can be predicted based on the expected nitrate loading and the time between PHA recharges desired. The unit sizing should be done for the maximum load expected. The slow rate and the energy required for PHA hydrolysis, make it unavailable as electron donor after the nitrate is consumed, so it will not promote the formation of sulfides. The model can be modified for other biodegradable non-water soluble medium by changing the hydrolysis constant, which must be determined experimentally. © 2014 Elsevier B.V.
Publication Source (Journal or Book title)
Aquacultural Engineering
First Page
41
Last Page
47
Recommended Citation
Gutierrez-Wing, M., Malone, R., & Rusch, K. (2014). Development of a model for PHA-based denitrification in a packed bed reactor. Aquacultural Engineering, 60, 41-47. https://doi.org/10.1016/j.aquaeng.2014.04.005