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dc.contributor.author
Mussati, Miguel Ceferino  
dc.contributor.author
Gernaey, Krist  
dc.contributor.author
Gani, Rafiqul  
dc.contributor.author
Jørgensen, Sten  
dc.date.available
2023-01-14T02:02:54Z  
dc.date.issued
2002-09  
dc.identifier.citation
Mussati, Miguel Ceferino; Gernaey, Krist; Gani, Rafiqul; Jørgensen, Sten; Computer aided model analysis and dynamic simulation of a wastewater treatment plant; Springer; Clean Technologies And Environmental Policy; 4; 2; 9-2002; 100-114  
dc.identifier.issn
1618-954X  
dc.identifier.uri
http://hdl.handle.net/11336/184764  
dc.description.abstract
A nitrogen removal benchmark was analyzed using the Activated Sludge Models No. 1 (ASM1) and No. 3 (ASM3) in order to establish a basis for designing an experimental comparison of the two model types. Differences in steady state effluent concentrations predicted by both models could to a large extent be explained by different model concepts. The steady state system performance was analyzed by evaluating the Monod factor values, and through a sensitivity analysis of the kinetic model parameters. Both methods complement each other. Analysis of the Monod factor values can lead to determination of parameters to be estimated during model calibration. The steady state system response to manipulation of the potential actuators for control was evaluated via a sensitivity analysis. The concept of relative sensitivity was introduced to compare the relative effect of each actuator in both models. The negative relative sensitivities of X S to four of the five control handles analyzed imply an opposite response of both models, which can be important for control structure design. The analysis of the process behavior to different disturbances showed different dynamics of both models. ASM3 simulation results are easier to interpret because the model structure is more transparent, mainly due to the simpler cell decay model principle considered in ASM3. An inverse response was obtained for the return sludge and nitrate recycle flow rate, indicating that multivariable control design is required.  
dc.format
application/pdf  
dc.language.iso
eng  
dc.publisher
Springer  
dc.rights
info:eu-repo/semantics/restrictedAccess  
dc.rights.uri
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/  
dc.subject
WASTEWATER TREATMENT  
dc.subject
DENITRIFICATION PROCESS  
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COMPUTER AIDED MODEL ANALYSIS  
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DYNAMIC SIMULATION  
dc.subject.classification
Otras Ingeniería Química  
dc.subject.classification
Ingeniería Química  
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INGENIERÍAS Y TECNOLOGÍAS  
dc.title
Computer aided model analysis and dynamic simulation of a wastewater treatment plant  
dc.type
info:eu-repo/semantics/article  
dc.type
info:ar-repo/semantics/artículo  
dc.type
info:eu-repo/semantics/publishedVersion  
dc.date.updated
2022-07-04T20:20:50Z  
dc.journal.volume
4  
dc.journal.number
2  
dc.journal.pagination
100-114  
dc.journal.pais
Alemania  
dc.journal.ciudad
Berlín  
dc.description.fil
Fil: Mussati, Miguel Ceferino. Technical University of Denmark; Dinamarca. Consejo Nacional de Investigaciones Científicas y Técnicas; Argentina  
dc.description.fil
Fil: Gernaey, Krist. Technical University of Denmark; Dinamarca  
dc.description.fil
Fil: Gani, Rafiqul. Technical University of Denmark; Dinamarca  
dc.description.fil
Fil: Jørgensen, Sten. Technical University of Denmark; Dinamarca  
dc.journal.title
Clean Technologies And Environmental Policy  
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.1007/s10098-002-0153-z  
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/url/https://link.springer.com/article/10.1007/s10098-002-0153-z