Optimal Design of the Leaching Stage in the Manufacturing Process of Surimi Gel
- Autores
- Reinheimer, Maria Agustina; Scenna, Nicolas Jose; Mussati, Sergio Fabian
- Año de publicación
- 2013
- Idioma
- inglés
- Tipo de recurso
- artículo
- Estado
- versión publicada
- Descripción
- The leaching stage in the manufacturing process of surimi gel requires a large amount of wash water contributing to a high operating cost. Therefore, the minimization of the wash water demand is essential for a low cost operation. In this paper, a complete mathematical model for the simultaneous optimization of the process configuration and the operating conditions of the continuous leaching process is presented. A superstructure formulation that embeds not only known process arrangements for the leaching process but also hybrid configurations is proposed. It is modeled as a nonlinear programming mathematical model. Given the design goal (extraction rate), the aim is to obtain the best process arrangement and operating conditions at minimum wash water demand. An interesting result obtained from the superstructure optimization is that, for a given extraction yield of soluble protein and total volume of leaching tank, the same minimum fresh water requirement is obtained with different leaching arrangements and with different distributions of flow rates. In addition, a sensitivity analysis was conducted in order to study the influence of the total volume of leaching tanks, number of leaching cycles, and extraction yield of soluble protein on the minimum fresh water consumption (countercurrent arrangement). As expected, for a given percentage of extraction from soluble proteins, the fresh water consumption significantly decreases, following an exponential decay law, as the total volume increases. A sensitivity analysis reveals that the minimum theoretical water consumption is obtained for four or higher number of washing cycles.
Fil: Reinheimer, Maria Agustina. Universidad Tecnologica Nacional. Regional Rosario. Centro de Aplicaciones Informaticas y Modelado En Ingenieria; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas; Argentina
Fil: Scenna, Nicolas Jose. Universidad Tecnologica Nacional. Regional Rosario. Centro de Aplicaciones Informaticas y Modelado En Ingenieria; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas; Argentina
Fil: Mussati, Sergio Fabian. Universidad Tecnologica Nacional. Regional Rosario. Centro de Aplicaciones Informaticas y Modelado En Ingenieria; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Santa Fe. Instituto de Desarrollo y Diseño (i); Argentina - Materia
-
Optimal Design
Leaching Stage
Manufacturing Process of Surimi Gel
Mathematical Modelling - Nivel de accesibilidad
- acceso abierto
- Condiciones de uso
- https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
- Repositorio
.jpg)
- Institución
- Consejo Nacional de Investigaciones Científicas y Técnicas
- OAI Identificador
- oai:ri.conicet.gov.ar:11336/6953
Ver los metadatos del registro completo
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Optimal Design of the Leaching Stage in the Manufacturing Process of Surimi GelReinheimer, Maria AgustinaScenna, Nicolas JoseMussati, Sergio FabianOptimal DesignLeaching StageManufacturing Process of Surimi GelMathematical Modellinghttps://purl.org/becyt/ford/2.11https://purl.org/becyt/ford/2The leaching stage in the manufacturing process of surimi gel requires a large amount of wash water contributing to a high operating cost. Therefore, the minimization of the wash water demand is essential for a low cost operation. In this paper, a complete mathematical model for the simultaneous optimization of the process configuration and the operating conditions of the continuous leaching process is presented. A superstructure formulation that embeds not only known process arrangements for the leaching process but also hybrid configurations is proposed. It is modeled as a nonlinear programming mathematical model. Given the design goal (extraction rate), the aim is to obtain the best process arrangement and operating conditions at minimum wash water demand. An interesting result obtained from the superstructure optimization is that, for a given extraction yield of soluble protein and total volume of leaching tank, the same minimum fresh water requirement is obtained with different leaching arrangements and with different distributions of flow rates. In addition, a sensitivity analysis was conducted in order to study the influence of the total volume of leaching tanks, number of leaching cycles, and extraction yield of soluble protein on the minimum fresh water consumption (countercurrent arrangement). As expected, for a given percentage of extraction from soluble proteins, the fresh water consumption significantly decreases, following an exponential decay law, as the total volume increases. A sensitivity analysis reveals that the minimum theoretical water consumption is obtained for four or higher number of washing cycles.Fil: Reinheimer, Maria Agustina. Universidad Tecnologica Nacional. Regional Rosario. Centro de Aplicaciones Informaticas y Modelado En Ingenieria; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas; ArgentinaFil: Scenna, Nicolas Jose. Universidad Tecnologica Nacional. Regional Rosario. Centro de Aplicaciones Informaticas y Modelado En Ingenieria; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas; ArgentinaFil: Mussati, Sergio Fabian. Universidad Tecnologica Nacional. Regional Rosario. Centro de Aplicaciones Informaticas y Modelado En Ingenieria; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Santa Fe. Instituto de Desarrollo y Diseño (i); ArgentinaAmerican Chemical Society2013-08info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/6953Reinheimer, Maria Agustina; Scenna, Nicolas Jose; Mussati, Sergio Fabian; Optimal Design of the Leaching Stage in the Manufacturing Process of Surimi Gel; American Chemical Society; Industrial & Engineering Chemical Research; 52; 36; 8-2013; 13034-130450888-5885enginfo:eu-repo/semantics/altIdentifier/doi/info:eu-repo/semantics/altIdentifier/doi/10.1021/ie400675tinfo:eu-repo/semantics/altIdentifier/url/10.1021/ie400675tinfo:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-11-05T09:44:15Zoai:ri.conicet.gov.ar:11336/6953instacron:CONICETInstitucionalhttp://ri.conicet.gov.ar/Organismo científico-tecnológicoNo correspondehttp://ri.conicet.gov.ar/oai/requestdasensio@conicet.gov.ar; lcarlino@conicet.gov.arArgentinaNo correspondeNo correspondeNo correspondeopendoar:34982025-11-05 09:44:15.362CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse |
| dc.title.none.fl_str_mv |
Optimal Design of the Leaching Stage in the Manufacturing Process of Surimi Gel |
| title |
Optimal Design of the Leaching Stage in the Manufacturing Process of Surimi Gel |
| spellingShingle |
Optimal Design of the Leaching Stage in the Manufacturing Process of Surimi Gel Reinheimer, Maria Agustina Optimal Design Leaching Stage Manufacturing Process of Surimi Gel Mathematical Modelling |
| title_short |
Optimal Design of the Leaching Stage in the Manufacturing Process of Surimi Gel |
| title_full |
Optimal Design of the Leaching Stage in the Manufacturing Process of Surimi Gel |
| title_fullStr |
Optimal Design of the Leaching Stage in the Manufacturing Process of Surimi Gel |
| title_full_unstemmed |
Optimal Design of the Leaching Stage in the Manufacturing Process of Surimi Gel |
| title_sort |
Optimal Design of the Leaching Stage in the Manufacturing Process of Surimi Gel |
| dc.creator.none.fl_str_mv |
Reinheimer, Maria Agustina Scenna, Nicolas Jose Mussati, Sergio Fabian |
| author |
Reinheimer, Maria Agustina |
| author_facet |
Reinheimer, Maria Agustina Scenna, Nicolas Jose Mussati, Sergio Fabian |
| author_role |
author |
| author2 |
Scenna, Nicolas Jose Mussati, Sergio Fabian |
| author2_role |
author author |
| dc.subject.none.fl_str_mv |
Optimal Design Leaching Stage Manufacturing Process of Surimi Gel Mathematical Modelling |
| topic |
Optimal Design Leaching Stage Manufacturing Process of Surimi Gel Mathematical Modelling |
| purl_subject.fl_str_mv |
https://purl.org/becyt/ford/2.11 https://purl.org/becyt/ford/2 |
| dc.description.none.fl_txt_mv |
The leaching stage in the manufacturing process of surimi gel requires a large amount of wash water contributing to a high operating cost. Therefore, the minimization of the wash water demand is essential for a low cost operation. In this paper, a complete mathematical model for the simultaneous optimization of the process configuration and the operating conditions of the continuous leaching process is presented. A superstructure formulation that embeds not only known process arrangements for the leaching process but also hybrid configurations is proposed. It is modeled as a nonlinear programming mathematical model. Given the design goal (extraction rate), the aim is to obtain the best process arrangement and operating conditions at minimum wash water demand. An interesting result obtained from the superstructure optimization is that, for a given extraction yield of soluble protein and total volume of leaching tank, the same minimum fresh water requirement is obtained with different leaching arrangements and with different distributions of flow rates. In addition, a sensitivity analysis was conducted in order to study the influence of the total volume of leaching tanks, number of leaching cycles, and extraction yield of soluble protein on the minimum fresh water consumption (countercurrent arrangement). As expected, for a given percentage of extraction from soluble proteins, the fresh water consumption significantly decreases, following an exponential decay law, as the total volume increases. A sensitivity analysis reveals that the minimum theoretical water consumption is obtained for four or higher number of washing cycles. Fil: Reinheimer, Maria Agustina. Universidad Tecnologica Nacional. Regional Rosario. Centro de Aplicaciones Informaticas y Modelado En Ingenieria; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas; Argentina Fil: Scenna, Nicolas Jose. Universidad Tecnologica Nacional. Regional Rosario. Centro de Aplicaciones Informaticas y Modelado En Ingenieria; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas; Argentina Fil: Mussati, Sergio Fabian. Universidad Tecnologica Nacional. Regional Rosario. Centro de Aplicaciones Informaticas y Modelado En Ingenieria; Argentina. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Santa Fe. Instituto de Desarrollo y Diseño (i); Argentina |
| description |
The leaching stage in the manufacturing process of surimi gel requires a large amount of wash water contributing to a high operating cost. Therefore, the minimization of the wash water demand is essential for a low cost operation. In this paper, a complete mathematical model for the simultaneous optimization of the process configuration and the operating conditions of the continuous leaching process is presented. A superstructure formulation that embeds not only known process arrangements for the leaching process but also hybrid configurations is proposed. It is modeled as a nonlinear programming mathematical model. Given the design goal (extraction rate), the aim is to obtain the best process arrangement and operating conditions at minimum wash water demand. An interesting result obtained from the superstructure optimization is that, for a given extraction yield of soluble protein and total volume of leaching tank, the same minimum fresh water requirement is obtained with different leaching arrangements and with different distributions of flow rates. In addition, a sensitivity analysis was conducted in order to study the influence of the total volume of leaching tanks, number of leaching cycles, and extraction yield of soluble protein on the minimum fresh water consumption (countercurrent arrangement). As expected, for a given percentage of extraction from soluble proteins, the fresh water consumption significantly decreases, following an exponential decay law, as the total volume increases. A sensitivity analysis reveals that the minimum theoretical water consumption is obtained for four or higher number of washing cycles. |
| publishDate |
2013 |
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2013-08 |
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info:eu-repo/semantics/article info:eu-repo/semantics/publishedVersion http://purl.org/coar/resource_type/c_6501 info:ar-repo/semantics/articulo |
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article |
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publishedVersion |
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http://hdl.handle.net/11336/6953 Reinheimer, Maria Agustina; Scenna, Nicolas Jose; Mussati, Sergio Fabian; Optimal Design of the Leaching Stage in the Manufacturing Process of Surimi Gel; American Chemical Society; Industrial & Engineering Chemical Research; 52; 36; 8-2013; 13034-13045 0888-5885 |
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http://hdl.handle.net/11336/6953 |
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Reinheimer, Maria Agustina; Scenna, Nicolas Jose; Mussati, Sergio Fabian; Optimal Design of the Leaching Stage in the Manufacturing Process of Surimi Gel; American Chemical Society; Industrial & Engineering Chemical Research; 52; 36; 8-2013; 13034-13045 0888-5885 |
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eng |
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eng |
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American Chemical Society |
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American Chemical Society |
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