Synthesis and Design of Combined Biological Nitrogen and Phosphorus Removal WWT Plants

Alasino, Noelia; Mussati, Miguel C.; Scenna, Nicolás J.; Aguirre, Pío A.

doi:10.1016/s1570-7946(09)70409-2

Cited by 1 publication

(2 citation statements)

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“…• As in previous works, , it was observed that treatment performance benefits from operational features such as the use of different aeration and stream distributions patterns, mainly in cases where the reaction volumes are constrained.…”

Section: Resultsmentioning

confidence: 57%

“…Mussati et al presented a mixed-integer nonlinear programming (MINLP) model for the simultaneous optimization of the process configuration and the operation conditions of WWTPs for nitrogen removal, introducing a superstructure that embeds the three most used ASP configurations, i.e., predenitrification (PreDN), postdenitrification (PostDN), and pre-postdenitrification (PrePostDN) systems, but without allowing streamflow distribution patterns. In the studies by Alasino et al, , that model was extended to account for flow distribution of the main process streams (nitrate and sludge recycle streams and fresh feed stream) along the reaction zone. However, reactor volumes were fixed and investment costs were not included in the model.…”

Section: Introductionmentioning

confidence: 99%

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Wastewater Treatment Plant Synthesis and Design

Alasino

Mussati

Scenna

2007

Ind. Eng. Chem. Res.

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The most used process for biological nitrogen removal from municipal and industrial wastewaters is the activated sludge process. Because of the importance of this process, as well as the large number of existing facilities, a lot of research effort has been focused on optimizing the operation strategies or improving the individual plant design. However, the systematic optimization of the process structure (process synthesis) and operation conditions based on rigorous process models has not been presented in the literature. The objective of this work is to address the simultaneous optimization of the process configuration and equipment dimensionsi.e., process synthesis and designand the operation conditions of activated sludge wastewater treatment plants for nitrogen removal based on a superstructure model. The model embeds up to five reactors and a secondary settler, and allows flow distribution of the main process streams, i.e., nitrate and sludge recycle streams and fresh feed, along the reaction zone. The objective function is to minimize the net present value formed by investment and operating costs, while verifying compliance with the effluent permitted limits. The investment cost computes the reaction tanks, aeration systems, secondary settler, influent pumping station, and sludge pump costs. The operation cost computes the cost for pumping, aeration, dosage of an external carbon source, excess sludge treatment for disposal, and fines according to pollution units discharged. Influent wastewater flowrate and composition are assumed to be known. The activated sludge model no. 3 and the Takács model are selected to describe the biochemical processes and the secondary settler, respectively. This results in a highly nonlinear system with nonsmooth functions. Because of the problem complexity, in this first approach, a nonlinear programming (NLP) problem (specifically a nonlinear programming with discontinuous derivatives (DNLP) problem) is proposed and solved to obtain some insights for future models. It was implemented and solved using general algebraic modeling system (GAMS). Results for case studies are presented and discussed.

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Section: Resultsmentioning

confidence: 57%

Section: Introductionmentioning

confidence: 99%