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Record W4233789682 · doi:10.2523/84198-ms

A Stochastic Approach to Extract Vapex Related Dispersion Coefficients from Magnetic Resonance Images

2003· article· en· W4233789682 on OpenAlexaffabout
Karmaker Kulada, Brij Maini

Bibliographic record

VenueProceedings of SPE Annual Technical Conference and Exhibition · 2003
Typearticle
Languageen
FieldChemistry
TopicPetroleum Processing and Analysis
Canadian institutionsUniversity of Calgary
Fundersnot available
KeywordsCitationExhibitionComputer scienceInformation retrievalWorld Wide WebArt historyArt

Abstract

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A Stochastic Approach to Extract Vapex Related Dispersion Coefficients from Magnetic Resonance Images Kulada Karmaker; Kulada Karmaker University of Calgary Search for other works by this author on: This Site Google Scholar Brij B. Maini Brij B. Maini University of Calgary Search for other works by this author on: This Site Google Scholar Paper presented at the SPE Annual Technical Conference and Exhibition, Denver, Colorado, October 2003. Paper Number: SPE-84198-MS https://doi.org/10.2118/84198-MS Published: October 05 2003 Cite View This Citation Add to Citation Manager Share Icon Share Twitter LinkedIn Get Permissions Search Site Citation Karmaker, Kulada, and Brij B. Maini. "A Stochastic Approach to Extract Vapex Related Dispersion Coefficients from Magnetic Resonance Images." Paper presented at the SPE Annual Technical Conference and Exhibition, Denver, Colorado, October 2003. doi: https://doi.org/10.2118/84198-MS Download citation file: Ris (Zotero) Reference Manager EasyBib Bookends Mendeley Papers EndNote RefWorks BibTex Search Dropdown Menu toolbar search search input Search input auto suggest filter your search All ContentAll ProceedingsSociety of Petroleum Engineers (SPE)SPE Annual Technical Conference and Exhibition Search Advanced Search SummaryIn vapor extraction (Vapex) process, the dispersional mixing between injected solvent vapor (propane) and in-situ bitumen occurs along the oil-solvent interface during the oil drainage process. The solvent dispersion coefficient is a key parameter that governs the oil dilution efficiency as well as the rate of production. To predict the field performance of the Vapex process it is vital to accurately estimate the value of the dispersion coefficient at the field conditions of interest. Currently, there are no factual data available in the literature and there is no proven empirical methodology for estimating the dispersion coefficients that would be pertinent to the Vapex process.Recently, the Magnetic Resonance Imaging (MRI) tools have been used to gain insights into the Vapex process. The MRI technique can generate 2-dimensional (2-D) images during the progress of a laboratory-scale Vapex experiment. Both the original bitumen and the solvent vapor are virtually invisible in these MRI generated 2-D images. However, the propane saturated bitumen is clearly visible and in the diluted oil zone, the signal intensity is a function of the dissolved solvent concentration.This paper describes a new technique to extract the net dispersion coefficients pertinent to the Vapex process from 2-D MRI images captured during a test. A new mathematical model has been developed for analyzing such 2-D images. The model portrays the unique context of mass transfer mechanisms and the interface propagation in the Vapex process. The technique has been used on a previously published MRI image and found to be very effective and straightforward.IntroductionThe Vapex process can be described as a solvent analogue of the steam assisted gravity drainage (SAGD) process1, which involves a drastic reduction of oil viscosity by diluting the in-situ bitumen with vaporized hydrocarbon solvents (HCS). The process uses a horizontal well pair with the production well located near the bottom of the pay zone and the injection well completed right above the production well as schematically shown in Figure-1. The injected solvent vapor, such as propane, dissolves into the bitumen and reduces its viscosity to a low value so that the diluted bitumen can drain down, under the gravity force, into the production well. The pore space around the injection well in the swept zone remains filled with solvent vapor and is called "vapor chamber". The diluted oil flow occurs in a thin film (drainage edge) adjoining the interface as illustrated in Figure-1. In the progress of oil drainage, the vapor chamber grows and the vapor-bitumen interface moves laterally at a certain velocity depending on the rate of interfacial mass transfer of solvent into bitumen.There are several mechanisms that enhance the interfacial mass transfer process in porous media, as explained by Das and Butler2. However, the mixing of solvent and bitumen occurs mainly by a combined mechanism of molecular diffusion and convective dispersion that takes place mostly within the drainage edge. While history matching the results of Vapex experiments using reservoir simulation software, Nghiem3 has shown that the convective dispersion is more important than the molecular diffusion in the mixing process. For a satisfactory history match, he needed transverse dispersion coefficients that were at least an order of magnitude larger than the molecular diffusion coefficient. Keywords: experiment, equation, enhanced recovery, dispersion coefficient, successive image, concentration, signal strength profile, propane, interface velocity, upstream oil & gas Subjects: Improved and Enhanced Recovery This content is only available via PDF. 2003. Society of Petroleum Engineers You can access this article if you purchase or spend a download.

Fetched live from OpenAlex and de-inverted. Abstracts are not stored in this database: the inverted indexes are 8.6 GB of the frame’s 9.3 GB of text, and the host has 13 GB free.

How this classification was reachedexpand

Full frame distilled prediction

Teacher imitation

Not calibrated prevalence, not ground truth. Human validation pending. Learned from the 10,348 direct Codex labels and 10,348 direct Gemma labels. Candidate is the union of thresholded teacher heads; consensus is their intersection. These outputs are machine_predicted_unvalidated and are not human labels or direct frontier model labels.

metaresearch head score (Codex)0.000
metaresearch head score (Gemma)0.000
Version: codex-gemma-dda1882f352aValidation status: machine_predicted_unvalidated
Candidate categoriesnone
Consensus categoriesnone
DomainCandidate signal: none · Consensus signal: none
Study designCandidate signal: Bench or experimental · Consensus signal: Bench or experimental
GenreCandidate signal: Empirical · Consensus signal: Empirical
Teacher disagreement score0.121
Threshold uncertainty score0.774

Codex and Gemma teacher scores by category

CategoryCodexGemma
Metaresearch0.0000.000
Meta-epidemiology (narrow)0.0000.000
Meta-epidemiology (broad)0.0000.000
Bibliometrics0.0000.000
Science and technology studies0.0000.000
Scholarly communication0.0000.000
Open science0.0000.000
Research integrity0.0000.000
Insufficient payload (model declined to judge)0.0000.000

Machine scores (provisional)

The two teacher heads of the student model, read on this work. A score orders the frame for review; it never asserts a category, and the validation status ships verbatim with every row.

Baseline scores from an immature model (maturity gate not passed, 7 training rounds). Scores rank; they never assert a category.

Opus teacher head0.012
GPT teacher head0.234
Teacher spread0.222 · how far apart the two teachers sit on this one work
Validation statusscore_only:v0-immature-baseline · verbatim from the scoring run: score_only means the number may rank works, and no category label ships from it

Classification

machine, unvalidated

Machine predicted; a candidate call from one teacher head, not a consensus.

The models applied no category: nothing in the taxonomy fit this work.
Study designBench or experimental
Domainnot available
GenreEmpirical

How this classification was reached, model by model and score by score, is at the end of the page under "How this classification was reached".

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Citations0
Published2003
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