Energy and economic optimization of a fishmeal plant using exergy analysis and experimental determination of mixture flows specific heat.

Authors

  • Salome Gonzales Chávez Facultad de Ingeniería Mecánica, Universidad Nacional de Ingeniería. Lima, Perú.
  • Ferdinan Estrada Almanza Industria Pesquera Diamante, Perú

DOI:

https://doi.org/10.21754/tecnia.v25i1.21

Keywords:

optimization, mixed flow, fishmeal, specific heat, exergy, balance, irreversibilities

Abstract

In this paper we formulate and apply the Exergy Analysis the set heat energy consumption elements of a typical plant of fishmeal, estimating experimentally the specific heat of the solid- liquid-vapor mixtures that form the raw material and steam, in order to optimize energy consumption by changes in the original installation and thus achieving the reduction in operating costs. Usually in these plants conventional energy balance and the premise that the specific heats are physical single phase flows is used; however, when solid-fat-water-steam mixture flows are presented, as is the case, these simple energy balances in each heating element become weak and lead to a high error margin in energy system assessment. In the methodology, the specific heats of mixture flows fat-water-vapor-solid is estimated by measurement of indicators in the industrial plant, contrasted with laboratory standards and empirical mathematical models. Then proceed to formulation and exergy calculation for each process and together, being elaborated a structured Excel program that calculates balances linked mass, energy and exergy. From this diagnosis suggestions for improvement are made to select the best alternative. As a result the best energy conformation of a typical fishmeal plant is obtained, this mean compared to the traditional system: excess fuel is removed, steam overproduction is removed and heat loss is reduced in each element. This represents an annual savings of ten million dollars plus additional benefits are presented as reduction of greenhouse gas emissions, effluents and improved industrial safety .

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References

[1] Göran Wall, Exergy a useful concept, “Physical Resource Theory Group”, Göteborg 1986, 3rdedition.

[2] .Ibrahim Dincer, Marc A. Rosen., “Exergy, Energy, Environmet and Sustainable Development”, first edition2007.

[3] .Lozano Serrano, M. A., -Valero Capilla., “Análisis exergético y energético de calderas de vapor”, Dpto. de Termodinámica y Físico Química, Escuela Superior de Ingenieros Industriales Universidad de Zaragoza,2000.

[4] .Choi, Y., Okos, M. R., “Effects of temperature and composition on the thermal properties of foods”, Engineering and Process Applications (M. A. Rao and S. S. H. Rizvi, Editors). Elsevier Applied Science Publishers. Great Britain, London.1986.

[5] .Orrego Alate C., “Procesamiento de alimentos”, Publicado por Unibiblos -U. Nal. Colombia,2001.

[6] .Alton E. Bayley. “Aceites y Grasas Industriales”. USA,1984.

[7] .Charm, S. E., “Fundamental of Food Engineering”. Vna Nostrand Reinhold/ AVI, New Cork. 164 pp.1971.

[8] .Dickerson, R. W. Jr., “Thermal properties of food”, Chapter 2 in The freezing preservation of food,1968.

[9] .Donald Q. Kern, “Procesos de transferencia de calor, Ed McGraw –Hill Book Company INC New York,1986.

[10] .Kenneth Wark Jr, Donald E, Richards“Termodinámica”, NY, 2001.

Published

2015-06-01

How to Cite

[1]
S. Gonzales Chávez and F. Estrada Almanza, “Energy and economic optimization of a fishmeal plant using exergy analysis and experimental determination of mixture flows specific heat”., TEC, vol. 25, no. 1, p. 41, Jun. 2015.

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Articles