Modelling of Non-Equilibrium Heavy Oil-Solvent Behaviour

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dc.contributor.advisorGates, Ian
dc.contributor.authorTai, Nan
dc.contributor.committeememberHejazi, Hossein
dc.contributor.committeememberChen, Shengnan (Nancy)
dc.date.accessioned2021-12-23T21:29:15Z
dc.date.available2021-12-23T21:29:15Z
dc.date.issued2021-12-17
dc.description.abstractA multi-component kinetic model is proposed to simulate non-equilibrium solvent ex-solution and back dissolution processes in the heavy oil bulk environment. The model consists of micro bubbles, which inherit physical properties from the solution gas and is treated as a gas-like liquid, to simulate foamy oil behavior during volume expansion processes. Free gas is considered as being able to transfer directly to solution gas to simulate the hysteresis which happens in the dissolution process when volume pressure increases. The kinetic model comprises three pseudo-chemical reactions with seven parameters which were calibrated against experimental data. The model was validated by using a thermal reservoir simulator and the results were capable of predicting the oil-gas system volume changes for two different solvent-heavy oil systems accurately under various pressure variation rates at both 15 and 75°C. Four reaction orders and three reaction frequency factors were tuned and it indicated that in a solvent-heavy oil system with solvent CH4 or C2H6: (1) stronger foamy oil behavior exists with solvent of C2H6 instead of CH4 during pressure depletion processes for heavy oil with the similar solvent concentration; (2) for both solvents, micro bubble release rates are larger at higher temperature and the rates tend to increase with pressure decline regardless of temperature; and (3) in the solvent dissolution process, for both CH4 and C2H6, relatively high pressure and temperature are both significant elements for promoting solvent dissolution back into heavy oil.en_US
dc.identifier.citationTai, N. (2021). Modelling of Non-Equilibrium Heavy Oil-Solvent Behaviour (Master's thesis, University of Calgary, Calgary, Canada). Retrieved from https://prism.ucalgary.ca.en_US
dc.identifier.doihttp://dx.doi.org/10.11575/PRISM/39473
dc.identifier.urihttp://hdl.handle.net/1880/114232
dc.language.isoengen_US
dc.publisher.facultySchulich School of Engineeringen_US
dc.publisher.institutionUniversity of Calgaryen
dc.rightsUniversity of Calgary graduate students retain copyright ownership and moral rights for their thesis. You may use this material in any way that is permitted by the Copyright Act or through licensing that has been assigned to the document. For uses that are not allowable under copyright legislation or licensing, you are required to seek permission.en_US
dc.subject.classificationEngineering--Petroleumen_US
dc.titleModelling of Non-Equilibrium Heavy Oil-Solvent Behaviouren_US
dc.typemaster thesisen_US
thesis.degree.disciplineEngineering – Chemical & Petroleumen_US
thesis.degree.grantorUniversity of Calgaryen_US
thesis.degree.nameMaster of Science (MSc)en_US
ucalgary.item.requestcopytrueen_US
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