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dc.creatorJaramillo Arias, Juan Manuel
dc.date.accessioned2012-06-07T22:59:44Z
dc.date.available2012-06-07T22:59:44Z
dc.date.created2000
dc.date.issued2000
dc.identifier.urihttps://hdl.handle.net/1969.1/ETD-TAMU-2000-THESIS-J368
dc.descriptionDue to the character of the original source materials and the nature of batch digitization, quality control issues may be present in this document. Please report any quality issues you encounter to digital@library.tamu.edu, referencing the URI of the item.en
dc.descriptionIncludes bibliographical references (leaves 139-141).en
dc.descriptionIssued also on microfiche from Lange Micrographics.en
dc.description.abstractAround the world, volatile oil and retrograde gas reservoirs are considered as complex thermodynamic systems and even more when they exhibit vertical composition variations. Those systems must be characterized by an equation of state (EOS) to properly describe the thermodynamic behavior of the fluid in any compositional simulation. Thus, one can obtain accurate values of hydrocarbon fluids in place, reservoir performance and ultimate liquid recovery. Vertical compositional gradients are present in all type of reservoir fluids, from black oils to wet gases. However, the compositional gradient effect has been neglected for black oil and for wet and dry gases, but it cannot be ignored in volatile oil and gas condensate systems. This can be demonstrated by analyzing its effect upon the original gas and oil in place calculations and liquid recovery for volatile and gas condensate reservoirs. In this study we evaluated the hydrocarbon in place and liquid recovery when the compositional gradient was used or neglected during a depletion process. To accomplish this, we analyzed several z-grid sizes and well completion cases, for volatile oil, gas condensate and two-phase reservoirs. The studied reservoir fluid belongs to the Cusiana gas condensate field in Colombia. The experimental PVT tests used consisted of constant composition expansion (CCE) and constant volume depletion (CVD) and were reported by Brunal. This study was accomplished by tuning an equation of state, EOS, to the available CCE and CVD test data, generating tables of composition versus depth, and simulating a depletion process using several scenarios. The software used to calibrate the EOS and to generate the composition-depth tables is PVT-i and for the compositional simulation we used Eclipse 300. The proposed approach provided guidelines on the proper way to calculate properly the volume of oil and gas in place and liquid recovery for three types of reservoirs: a volatile oil, a gas condensate, and a two-phase reservoir. The last reservoir was considered when liquid and gas phases coexist at the initial reservoir conditions. The result of this study addressed the discrepancies that take place when the compositional gradient is not considered.en
dc.format.mediumelectronicen
dc.format.mimetypeapplication/pdf
dc.language.isoen_US
dc.publisherTexas A&M University
dc.rightsThis thesis was part of a retrospective digitization project authorized by the Texas A&M University Libraries in 2008. Copyright remains vested with the author(s). It is the user's responsibility to secure permission from the copyright holder(s) for re-use of the work beyond the provision of Fair Use.en
dc.subjectpetroleum engineering.en
dc.subjectMajor petroleum engineering.en
dc.titleVertical composition gradient effects on original hydrocarbon in place volumes and liquid recovery for volatile oil and gas condensate reservoirsen
dc.typeThesisen
thesis.degree.disciplinepetroleum engineeringen
thesis.degree.nameM.S.en
thesis.degree.levelMastersen
dc.type.genrethesisen
dc.type.materialtexten
dc.format.digitalOriginreformatted digitalen


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