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dc.contributor.authorZaboon, Sami Mohammed Zaboon
dc.contributor.supervisorAhmed Barifcanien_US
dc.contributor.supervisorRolf Gubneren_US
dc.date.accessioned2020-03-19T04:17:26Z
dc.date.available2020-03-19T04:17:26Z
dc.date.issued2019en_US
dc.identifier.urihttp://hdl.handle.net/20.500.11937/78308
dc.description.abstract

The sponsored bench-top scale Monoethylene glycol distillation unit located at Curtin University was designed and operated to use realistic production fluids, such as condensate mixtures and formation water/brines to simulate conditions representative industrial MEG systems. Many parameters such as MEG inlet concentration, temperature, rebiler temperature, inlet mass flowrate and reflux ratio have been experimentally examined to achieve the optimum conditions for the distillation process. These results were then compared with the results from HYSYS simulation.

en_US
dc.publisherCurtin Universityen_US
dc.titleMonoethylene Glycol Distillation System Design Validation, Operation and Effluent Treatmenten_US
dc.typeThesisen_US
dcterms.educationLevelPhDen_US
curtin.departmentWASM: Minerals, Energy and Chemical Engineeringen_US
curtin.accessStatusFulltext not availableen_US
curtin.facultyScience and Engineeringen_US
dc.date.embargoEnd2022-03-18


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