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dc.creatorJenny Díaz-Ramírez
dc.creatorJosé Ignacio Huertas
dc.date2018
dc.date.accessioned2019-10-08T20:36:22Z
dc.date.available2019-10-08T20:36:22Z
dc.identifierhttp://www.redalyc.org/articulo.oa?id=64358093012
dc.identifier.urihttp://hdl.handle.net/11285/635283
dc.descriptionIn the chemical industry, it is common to find production systems characterized by having a single stage or a previously identified bottleneck stage, with multiple non-identical parallel stations and with setup costs that depend on the production sequence. This paper proposes a mixed integer production-scheduling model that identifies lot size and product sequence that maximize profit. It considers multiple typical industry conditions, such as penalties for noncompliance or out of service periods of the productive units (or stations) for preventive maintenance activities. The model was validated with real data from an oil chemical company. Aiming to analyze its performance, we applied the model to 155 instances of production, which were obtained using Monte Carlo technique on the historical production data of the same company. We obtained an average 12 % reduction in the total cost of production and a 19 % increase in the estimated profit.
dc.formatapplication/pdf
dc.languageen
dc.publisherUniversidad Nacional de Colombia
dc.relationhttp://www.redalyc.org/revista.oa?id=643
dc.rightsIngeniería e Investigación
dc.sourceIngeniería e Investigación (Colombia) Num.1 Vol.38
dc.subjectIngeniería
dc.subjectMIP modeling
dc.subjectgoal programming
dc.subjectbatch process scheduling
dc.subjectshort-term scheduling
dc.subjectmathematical formulation
dc.subjectMonte Carlo simulation
dc.titleA continuous time model for a short-term multiproduct batch process scheduling
dc.typeArtículo científico


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    Red de Revistas Científicas de América Latina y el Caribe, España y Portugal

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