Understanding Reservoir Connectivity and Tar Mat Using Gravity-Induced Asphaltene Compositional Grading Sai R. Panuganti – Rice University, Houston Advisor: Prof. Walter G. Chapman – Rice University, Houston Co-advisor: Prof. Francisco M. Vargas – The Petroleum Institute, Abu Dhabi 1 Outline • Introduction • Motivation • PC-SAFT asphaltene phase behavior modeling • Predicting asphaltene compositional gradient • Prediction of tar-mat occurrence depth • Conclusion • Future release 2 Fast Facts about Asphaltene Polydisperse mixture of the heaviest and most polarizable fraction of the oil Defined in terms of its solubility Miscible in aromatic solvents, but insoluble in light paraffin solvents Molecular structure is not completely understood Behavior depends strongly on P, T and {xi} (a) n-C5 asphaltenes (b) n-C7 asphaltenes Jill Buckley, NMT http://www.gasandoilresearch.com/asph.html 3 Compositional Grading Introduction First theoretical explanation – Morris Muskat, 1930 Used for: Used for: 1. To predict oil properties with depth 2. Find out gas-oil contact Muskat M., Physical Review, 1930; 35:1384:1393 4 Schulte, A.M., SPE Conference, 1980; September 21-25, SPE 9235 Motivation Reservoir Connectivity Understanding reservoir connectivity helps in effective sweep of oil for a given number of wells Pressure communication can be used only to understand compartmentalization Tar Mat “ The presence of a tar mat could not be inferred from the PVT behavior of the reservoir oil in the upper part of the reservoir “ – Hirschberg, A. JPT 1988; 40(1):89-94 5 Zao, J.Y., et al., Journal of Chemical & Engineering Data, 2011; 56(4):1047-1058 PC-SAFT Modeling of Asphaltene PVT Behavior 14000 STO + Precipitant 12000 Pressure (Psia) 10000 Precipitant – C1 8000 6000 Precipitant – C2 4000 Tahiti Field Black Oil, Offshore, Gulf of Mexico Precipitant – C3 2000 0 0 20 40 60 80 100 Amount of asphaltene precipitating agent added (Mole %) Live Oil 8000 exp Bu. P Pressure (Psia) exp. AOP 6000 S Field – Light Oil, Onshore, Middle East Asphaltene Onset Pressure 4000 2000 Bubble Pressure 0 50 100 150 200 Temperature (F) 250 300 350 6 Panuganti, S.R. et al., Fuel, 2012; 93:658-669 Isothermal Compositional Grading Algorithm 7 Whitson, C.H., Belery, P., SPE 28000; 1994, 443-459 Verifying the Compositional Grading Algorithm 800 Field Data GOR (scf/stb) 600 400 200 0 24000 24500 25000 25500 26000 26500 27000 27500 Depth (ft) Tahiti Field 8 Verifying the Compositional Grading Algorithm Field Data 800 PC-SAFT Prediction GOR (scf/stb) 600 400 200 0 24000 24500 25000 25500 26000 26500 27000 27500 Depth (ft) Tahiti Field PC-SAFT prediction matches the field data, verifying the successful working of the compositional grading algorithm 9 Asphaltene Grading Optical Density (@1000 nm) 0 24000 0.5 1 1.5 2 2.5 Field Data (M21B) 24500 Depth (ft) 25000 Field Data (M21A Central) 25500 26000 Field Data (M21A North) 26500 27000 27500 Tahiti field, Offshore in Gulf of Mexico Black oil, isothermal reservoir at equilibrium Optical density measured using infra red wavelength during down-hole fluid analysis 10 Freed, D.E. et al., Energy and Fuels, 2011; 24:3942-3949 Predicting Asphaltene Compositional Grading Optical Density (@1000 nm) 0 0.5 1 1.5 2 2.5 PC-SAFT (M21B) 24000 Field Data (M21B) 24500 PC-SAFT (M21A Central) Depth (ft) 25000 25500 26000 26500 Field Data (M21A Central) PC-SAFT (M21A North) Field Data (M21A North) 27000 27500 • All continuous lines are PC-SAFT predictions • All zones belong to the same reservoir as the gradient slopes are nearly the same • The curves do not overlap implying each zone belongs to different compartment 11 PC-SAFT Asphaltene Compositional Grading Asphaltene Weight % in STO Tahiti field 2 4 6 8 10 12 14 24000 26000 Depth (ft) 28000 Reference Depth 30000 32000 34000 36000 • PC-SAFT asphaltene compositional grading extended to further depths • Field observations did not report any tar mat 12 Predicting Asphaltene Compositional Grading Dimensionless Optical Density (OD/ODo) 0.5 0.7 0.9 1.1 1.3 1.5 7500 Zone A1 S field Well Z Zone B1 Depth (ft) 7700 Field Data Well X 7900 Well Y 8100 • All continuous lines are PC-SAFT predictions • All zones belong to the same reservoir as the gradient slopes are nearly the same • The curves do not overlap implying each zone belongs to different compartment •Wells X and Y are connected because they lie on the same asphaltene grading curve 13 Tar-mat Onshore S field Tar-mat formation mechanism of S field • Asphaltene compositional grading Other tar-mat formation mechanisms • • • • • • Settling of precipitated asphaltene Asphaltene can adsorption onto mineral surfaces Oil-water contact Biodegradation Maturity between the oil leg and tar-mat Oil cracking Carpentier, B. et al. Abu Dhabi International Petroleum Exhibition and Conference 1998; November 11-14 14 Predicting Tar-mat Occurrence Asphaltene weight percentage in STO 0 10 20 30 40 50 60 7800 S field Depth (ft) 8100 Zone 1 8400 8700 Crude-Tar Transition 9000 Zone 2 Zone 3 • Matches field observations and tar-mat’s asphaltene content in SARA • Zone 1 – Liquid 1 (Asphaltene lean phase) Zone 2 – Liquid 1 + Liquid 2 Zone 3 – Liquid 2 (Asphaltene rich phase) • Such a prediction is possible only with an equation of state • Predicted tar-mat formation depth matching the field data, from PVT behavior in the upper parts of the reservoir Panuganti, S.R. et al., Energy and Fuels, 2011; dx.doi.org/10.1021/ef201280d 15 Tar-mat Analysis Asphaltene Weight % in STO 2 7 Asphaltene Weight % in STO 12 0 24000 10 20 30 40 50 60 7800 26000 8100 Depth (ft) Depth (ft) 28000 30000 32000 34000 8400 8700 9000 36000 Tahiti field S field Can the T field have an S field situation and vice versa ? 16 Asphaltene Compositional Gradient Isotherms Asphaltene weight % in STO 0 10 20 30 40 50 60 70 80 90 7800 S field Liquid 1 + Liquid 2 8800 P = 3500 Psia P = 4000 Psia Depth (ft) 9800 P = 5500 Psia P = 7500 Psia P = 10000 Psia 10800 P = 15000 Psia Phase Boundary 11800 12800 Thus any field can show large or low asphaltene gradients without a need of asphaltene precipitation 17 Panuganti, S.R. et al., Energy and Fuels, 2012; The 1st International Conference on Upstream Engineering and Flow Assurance Conclusion • Successful capture of asphaltene PVT behavior in the upper parts of the reservoir • Evaluated reservoir connectivity through asphaltene compositional grading • Predicted tar-mat occurrence depth because of asphaltene compositional grading 18 Future Release Input Parameters Property Density Mol. Weight Boiling Point Function of Temperature Mixtures Critical Temperature Y Y Y N/A Y Critical Pressure Y Y Y N/A Y Surface Tension Y Y Y Y N Molecular Polarizability N Y N N/A N/A Dielectric Constant Y N N Y Y Basis : Quantum and Statistical Mechanics 19 Predicted vs Experiment 1100 Critical Temperature (K) for 77 Nonolar Hydrocarbons 700 X=Y 50 500 40 X=Y 300 300 500 700 Experiment 900 1100 Predicted Predicted 900 30 20 10 Mean Polarizability of 53 Nonpolar Hydrocarbons (cc, 10^-24) 0 0 10 20 30 Experiment 40 50 20 Predicted vs Experiment 1100 Critical Temperature (K) for 77 Nonolar Hydrocarbons 700 n-Alkanes 50 Cyclo-Alkanes 500 Branched-Alkanes 40 Aromatics Polynuclear Aromatics 300 300 500 700 Experiment 900 1100 Predicted Predicted 900 Alkenes 30 Alkynes X=Y 20 10 Mean Polarizability of 53 Nonpolar Hydrocarbons (cc, 10^-24) 0 0 10 20 30 Experiment 40 50 21 Acknowledgement ADNOC OPCO’s R&D DeepStar Chevron ETC Schlumberger New Mexico Tech Infochem VLXE 22