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Journal of Heat Transfer | Volume 139 | Issue 4 | research-article
Research Papers: Heat Exchangers

Insights on Heat Transfer at the Top of Steam Chambers in SAGD

[+] Author and Article Information
Helen Pinto

Department of Geomatics Engineering,
Schulich School of Engineering,
University of Calgary,
2500 University Drive NW,
Calgary, AB T2N 1N4, Canada
e-mail: helen.pinto2@ucalgary.ca

Xin Wang

Associate Professor
Department of Geomatics Engineering,
Schulich School of Engineering,
University of Calgary,
2500 University Drive NW,
Calgary, AB T2N 1N4, Canada
e-mail: xcwang@ucalgary.ca

Ian D. Gates

Professor
Department of Chemical
and Petroleum Engineering,
Schulich School of Engineering,
University of Calgary,
2500 University Drive NW
Calgary, AB T2N 1N4, Canada
e-mail: ian.gates@ucalgary.ca

1Corresponding author.

Contributed by the Heat Transfer Division of ASME for publication in the JOURNAL OF HEAT TRANSFER. Manuscript received June 29, 2016; final manuscript received November 18, 2016; published online January 24, 2017. Assoc. Editor: Amy Fleischer.

J. Heat Transfer 139(4), 041801 (Jan 24, 2017) (10 pages) Paper No: HT-16-1430; doi: 10.1115/1.4035322 History: Received June 29, 2016; Revised November 18, 2016
Article
References
Figures
Tables

Steam-assisted gravity drainage (SAGD) is the method of choice for producing oil from oil sands reservoirs. In this method, steam is injected into the formation and the oil, upon heating, is mobilized and driven under gravity to a production well. The accumulation of steam within the reservoir is referred to as the steam chamber. One of the critical issues confronting SAGD operators is the thermal efficiency, measured by the steam-to-oil ratio, of their operations since it directly ties to process costs. Using thermocouple profiles from observation wells on three SAGD fields in Alberta, we use error function fits to estimate the thermal conductivity of the shale above the oil formation (found to be from 0.33 to 3.81 W/mK), heat flux at the top of the steam chamber, vertical height of the steam/gas zone above the steam chamber, and accumulated gas volume present. A gas material balance is then derived to estimate the volume of gas that might be generated through in situ chemical processes. The results of the heat transfer analysis performed on the thermocouple data reveal that the gas co-injection during SAGD operations studied did not directly affect the heat transfer rate at the top of the steam chamber since the gas volume added was small. The results also show that a sufficiently large accumulation of gas at the top of the chamber lowers the heat flux at the edge of the chamber.
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References

1
Canadian Association of Petroleum Producers, 2013, “  The Facts on Oil Sands,” Canadian Association of Petroleum Producers, Calgary, Canada, accessed June 3, 2016, http://issuu.com/capp/docs/oilsands-fact-book
2
Canadian Heavy Oil Association, 2013, “  Heavy Oil 101,” Canadian Heavy Oil Association, Calgary, Canada, accessed June 3, 2016, http://www.albertacanada.com/mexico/documents/P2.HeavyOil.pdf.
3
Gates, I. D. , Larter, S. R. , Wang, J. , Huang, H. , Bao, Y. , and Guo, T. , 2012, “ Rapid Routes to Carbon-Efficient Recovery of Bitumen and Heavy Oil,” Management Canada (CMC-NCE), Report No. A03 http://www.cmcghg.org/wp-content/uploads/2013/10/Ian-Gates-v1-final.pdf.
4
Chopra, S. , Lines, L. , Schmitt, D. R. , and Batzle, M. , 2010, “ Heavy Oils: Reservoir Characterization and Production Monitoring,” SEG Geophysical Developments, Series No. 13, Society of Exploration Geophysicists, Tulsa, OK, pp. 1–69. http://library.seg.org/doi/pdf/10.1190/1.9781560802235.fm
5
Butler, R. M. , 1994, “ Steam-Assisted Gravity Drainage: Concept, Development, Performance And Future,” J. Can. Pet. Technol., 33(2) pp.44–50. [CrossRef]
6
Gates, I. D. , and Larter, S. R. , 2014, “ Energy Efficiency and Emissions Intensity of SAGD,” Fuel, 115, pp. 706–713. [CrossRef]
7
Grant, J. , Angen, E. , and Dyer, S. , 2013, “ Forecasting the Impacts of Oilsands Expansion,” Pembina Institute, Calgary, AB, Canada, accessed June 3, 2016, www.pembina.org/reports/oilsands-metrics.pdf
8
Phenix, T. , 2015, “ Enhancing SAGD,” Oilsands Rev. 10(10) pp.16–19, accessed June 3, 2016, http://media.oilsandsreview.com.s3.amazonaws.com/pdf/2015/OSR_151001TS.pdf
9
Thimm, H. F. , 2005, “ Solvent Co-Injection in SAGD: Prediction of Some Operational Issues,” J. Can. Pet. Technol., 44(9), pp. 7–10.
10
Butler, R. , 1999, “ The Steam And Gas Push (SAGP),” J. Can. Pet. Technol., 38(3), pp. 54–61. [CrossRef]
11
Butler, R. M. , Jiang, Q. , and Yee, C. T. , 2001, “ Steam and Gas Push (SAGP)-4: Recent Theoretical Developments and Laboratory Results Using Layered Models,” J. Can. Pet. Technol., 40(1), pp. 54–61.
12
Edmunds, N. , 2006, “ Analysis of the Solution Gas Effect on SAGD Slope Drainage Rate,” World Heavy Oil Conference, Beijing, Paper No. 406.
13
Edmunds, N. , 2007, “ Effect of Solution Gas on 1D Steam Rise in Oil Sands,” J. Can. Pet. Technol., 46(1), pp. 56–62. [CrossRef]
14
Canbolat, S. , Akin, S. , and Kovscek, A. , 2004, “ Noncondensable Gas Steam-Assisted Gravity Drainage,” J. Pet. Sci. Eng., 45(1), pp. 83–96. [CrossRef]
15
Gillis, K. A. , Palmgren, C. , and Thimm, H. F. , 2000, “ Simulation of Gas Production in SAGD,” SPE/CIM International Conference on Horizontal Well Technology, Society of Petroleum Engineers, Calgary, AB, Canada, Paper No. 65500-MS.
16
Sharma, J. , Moore, R. G. , and Mehta, S. A. , 2012, “ Effect of Methane Co-Injection in SAGD—Analytical and Simulation Study,” SPE J., 17(3), pp. 687–704. [CrossRef]
17
Yuan, J.-Y. , Chen, J. , Pierce, G. , Wiwchar, B. , Golbeck, H. , Wang, X. , and Cameron, S. , 2011, “ Noncondensable Gas Distribution in SAGD Chambers,” J. Can. Pet. Technol., 50(3), pp. 11–30. [CrossRef]
18
Ito, Y. , Ichikawa, M. , and Hirata, T. , 1999, “ The Effect of Gas Injection on Oil Recovery During SAGD Projects,” Annual Technical Meeting of the Petroleum Society of Canada, Calgary, AB, Canada.
19
Butron, J. , Bryan, J. , Yu, X. , and Kantzas, A. , 2015, “ Production of Gases During Thermal Displacement Tests,” SPE Canada Heavy Oil Technical Conference, Society of Petroleum Engineers, Calgary, AB, Canada.
20
Kisman, K. E. , and Yeung, K. C. , 1995, “ Numerical Study of the SAGD Process in the Burnt Lake Oil Sands Lease,” SPE International Heavy Oil Symposium, Society of Petroleum Engineers, Calgary, AB, Canada.
21
Yee, C. T. , and Stroich, A. , 2004, “ Flue Gas Injection Into a Mature SAGD Steam Chamber at the Dover Project (Formerly UTF),” J. Can. Pet. Technol., 43(1), pp. 54–61. [CrossRef]
22
Gittins, S. , Gupta, S. C. , and Zaman, M. , 2013, “ Simulation of Noncondensable Gases in SAGD-Steam Chambers,” J. Can. Pet. Technol., 52(1), pp. 20–29. [CrossRef]
23
Canas, C. , Kantzas, A. , and Edmunds, N. , 2009, “ Investigation of Gas Flow in SAGD,” Canadian International Petroleum Conference, Petroleum Society of Canada, Calgary, AB, Canada.
24
AER, 2016, “Alberta Energy Regulator (AER) In-Situ Performance Presentations,” Alberta Energy Regulator, Calgary, Canada, accessed June 3, 2016, https://www.aer.ca/data-and-publications/activity-and-data/in-situ-performance-presentations
25
Divestco , 2016, “ EnerGISite,” Divestco, Calgary, Canada, accessed June 3, 2016, https://energisite.divestco.com/idcWellLogs2010/Home.aspx
26
Carslaw, H. , and Jaeger, J. , 1959, Conduction of Heat in Solids, Oxford University Press, Oxford, UK.
27
Irani, M. , and Gates, I. D. , 2014, “ On the Stability of the Edge of a Steam-Assisted-Gravity-Drainage Steam Chamber,” SPE J., 19(2), pp. 280–288. [CrossRef]
28
ConocoPhillips , 2009, “ Innovative Energy Technologies Program—Project Annual Report 2008,” accessed June 3, 2016, http://www.energy.alberta.ca/xdata/IETP/IETP%202008/01-013%20Surmount%20SAGD%20Pilot/01-013_Annual_Report_2008.pdf
29
Satter, A. , Ghulam, I. , and Buchwalter, J. , 2007, Practical Enhanced Reservoir Engineering: Assisted with Simulation Software, Penwell Books, Tulsa, OK.
30
Belgrave, J. D. M. , Moore, R. G. , and Ursenbach, M. G. , 1997, “ Comprehensive Kinetic Models for the Aquathermolysis of Heavy Oils,” J. Can. Pet. Technol., 36(4), pp. 38–44. [CrossRef]
31
Gates, I. D. , 2011, Basic Reservoir Engineering, Kendall Hunt Publishing, Dubuque, IA.
32
Statistics Solutions, 2016, “ Correlation (Pearson, Kendall, Spearman),” Statistics Solutions, accessed June 3, 2016, http://www.statisticssolutions.com/correlation-pearson-kendall-spearman/
33
Robertson, E. C. , 1988, “ Thermal Properties of Rocks,” U.S. Department of Interior Geological Survey, Report No. 88-441, p. 25 https://pubs.er.usgs.gov/publication/ofr88441.
34
Gilliam, T. M. , and Morgan, I. L. , 1987, “ Shale: Measurement of Thermal Properties,” Oak Ridge National Laboratory, Paper No. ORNL/TM-10499, p. 53 http://www.osti.gov/scitech/biblio/6163318.
35
Cohen, J. , 1988, Statistical Power Analysis for the Behavioral Sciences, 2nd ed., Erlbaum, Hillsdale, NJ.
36
Yang, X. , and Gates, I. D. , 2009, “ Design of Hybrid Steam-In Situ Combustion Bitumen Recovery Processes,” Nat. Resour. Res., 18(3), pp. 213–233. [CrossRef]
37
WIKA, 2016, “WIKA Downhole Temperature Measurement,” WIKA Instruments, Ltd., Edmonton, AB, Canada, accessed on Sept. 22, 2016, www.wika.ca/upload/BR_DownHole_en_ca_21863.pdf

Figures

Grahic Jump Location
Fig. 1

Cross section of a SAGD well pair. The injection and production wells are horizontal wells that go into the page.

+Cross section of a SAGD well pair. The injection and production wells are horizontal wells that go into the page.
View Large  |  Save Figure  |  Download Slide (.ppt)
Cross section of a SAGD well pair. The injection and production wells are horizontal wells that go into the page.
Grahic Jump Location
Fig. 2

Temperature profiles from one observation well at Christina Lake SAGD field (data sourced from Ref. [24]). Depth is relative to the Kelly Bushing (KB) on the drill rig.

+Temperature profiles from one observation well at Christina Lake SAGD field (data sourced from Ref. [24]). Depth is relative to the Kelly Bushing (KB) on the drill rig.
View Large  |  Save Figure  |  Download Slide (.ppt)
Temperature profiles from one observation well at Christina Lake SAGD field (data sourced from Ref. [24]). Depth is relative to the Kelly Bushing (KB) on the drill rig.
Grahic Jump Location
Fig. 3

Error function fit without and with gas accumulation at top of SAGD depletion chamber

+Error function fit without and with gas accumulation at top of SAGD depletion chamber
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Error function fit without and with gas accumulation at top of SAGD depletion chamber
Grahic Jump Location
Fig. 5

Flowchart of analysis tasks

+Flowchart of analysis tasks
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Flowchart of analysis tasks
Grahic Jump Location
Fig. 6

Example of profiles of temperature, gas fraction, and heat flux derived from sequenced thermocouple profiles with superposed error function fits

+Example of profiles of temperature, gas fraction, and heat flux derived from sequenced thermocouple profiles with superposed error function fits
View Large  |  Save Figure  |  Download Slide (.ppt)
Example of profiles of temperature, gas fraction, and heat flux derived from sequenced thermocouple profiles with superposed error function fits
Grahic Jump Location
Fig. 9

Graphical depiction of significant correlations

+Graphical depiction of significant correlations
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Graphical depiction of significant correlations

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