Please use this identifier to cite or link to this item: http://irepo.futminna.edu.ng:8080/jspui/handle/123456789/990
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dc.contributor.authorAdeniyi, O.D.-
dc.date.accessioned2021-06-03T11:51:32Z-
dc.date.available2021-06-03T11:51:32Z-
dc.date.issued2004-
dc.identifier.issn1583-0233-
dc.identifier.urihttp://repository.futminna.edu.ng:8080/jspui/handle/123456789/990-
dc.description.abstractIn recent years, the performance requirements for petroleum process plants have become increasingly difficult to satisfy. In order to understand, design and operate the complex systems in the petroleum industries at relatively low cost and with minimum risk, mathematical modelling becomes very useful. Thus, this paper proposes some developed mathematical models for a two-phase gas-liquid horizontal separator, which is valid with an accuracy of about 1.641% based on the liquid temperature values. Simulated temperature values were 300.24 K, 299.69 K and 299.14 K with the corresponding industrial values as 300.22 K, 299.67 K and 299.11 K respectively. Within the boundaries of the limitations stated, the model could be used to predict the operation of the separator at different operating conditions, to optimize the separator products and as a tool for further expansion amongst other uses.en_US
dc.language.isoenen_US
dc.publisherLeonardo Journal of Sciences (LJS), Romaniaen_US
dc.relation.ispartofseriesIssue 5, pp. 34-45;Issue 5, pp. 34-45-
dc.subjectGas-liquid, two phase horizontal separator, process control, model, simulationen_US
dc.titleDevelopment of Model and Simulation of a Two-Phase, Gas-Liquid Horizontal Separatoren_US
dc.typeArticleen_US
Appears in Collections:Chemical Engineering

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