UNDERSATURATED OIL-GAS SIMULATION IMPES SOLUTION

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Presentation transcript:

UNDERSATURATED OIL-GAS SIMULATION IMPES SOLUTION SIG4042 Reservoir Simulation

Contents Home Flow terms Oil and Gas Flow Equations Oil storage term Gas storage term Discretized form of oil and gas equations Oil and Gas Flow Equations Black Oil Fluid Properties Introducion Constant gas injection rate Injection at constant bottom hole pressure Constant oil production rate Production at constant reservoir voidage rate Production at constant bottom hole pressure Discretization of Flow Equations » Boundary Conditions » Handouts (pdf file) Solution by IMPES Method » Assumptions IMPES oil pressure solution IMPES bubble point pressure solution Aplicability of IMPES method Questions

Oil and Gas Flow Equations If the oil is under-saturated, there is no free gas in the pores. Thus, we really have one phase flow (in absence of water). However, if the amount of gas in solution varies, such as in the case of gas injection into an under-saturated reservoir, we need to keep track of the bubble point pressure, or saturation pressure, of the oil in order to account for the gas as well as in order to be able to compute the oil properties. Again, the oil density is given by: Continue For an under-saturated oil, the oil pressure is per definition higher than the bubble point pressure: and there is no free gas in the reservoir: Po > Pbp So = Continue Thus, the formation volume factor depends on both oil pressure and bubble point pressure (or saturation pressure): The solution gas-oil ratio, on the other hand, is now a function of bubble point pressure only, and not on oil pressure: Bo = f(Po,Pbp) Rso = f(Pbp)

Oil and Gas Flow Equations Again, we will, for mass balance purposes, separate the oil density into two parts, one that remains liquid at the surface and one that becomes gas: Continue The oil mass balance is written so that its continuity equation includes the liquid part only, while the gas mass balance includes the solution gas in the reservoir, and thus all free gas at the surface: As in the case of saturated oil-gas systems, the solution gas will flow with the rest of the oil in the reservoir, at oil relative permeability, viscosity and pressure.

Oil and Gas Flow Equations The Darcy equation for the single phase in the reservoir is thus the one for oil: Continue Although we have single phase flow, we will keep the relative permeability in the equations in case it is not equal to one. Substituting Darcy's equations and the liquid oil density and the solution gas density definitions into the continuity equations, and including production/injection terms in the equations, we obtain the following two flow equations: A free gas rate term is included in the gas equation for gas injection purposes.

Black Oil Fluid Properties The Black Oil fluid properties for under-saturated oil: Bo vs. Po Rso vs. Pbp mo vs. Po Bo Rso mo Po Pbp Po In the figures, the solid lines represent saturated conditions, while the dotted lines represent under-saturated behavior, with the bubble point pressure being defined by the intersection of the dotted line and the saturated line. Thus, the bubble point pressure depends on the amount of gas present in the system. The more gas, the higher the bubble point pressure.

Discretization of Flow Equations The discretization procedure for the flow terms of the oil-gas equations is very much similar to the one for saturated oil-gas equations. Continue Flow terms The left side of the oil equation is identical to the one for a saturated system: Continue For the gas equation, we only have the solution gas terms, which may be approximated just as for the solution gas term of the saturated equation:

Discretization of Flow Equations Definitions of the terms in the equation: Where: Continue The upstream mobilities are selected as: Continue Solution gas-oil ratios:

Discretization of Flow Equations Oil storage term We expand the right hand side of the oil equation as follows, keeping in mind that the formation volume factor is a function of oil pressure as well as bubble point pressure: where Pbp now is the variable bubble point pressure, a new unknown to be solved for together with oil pressure. Continue The two first terms above are identical to the two first terms of the saturated oil equation, with the exception that the derivative of the inverse formation volume factor is now a partial derivative, and that the the gas saturation is now zero. Thus, we can write the approximation of these two terms directly: Continue For the last term, we use the standard approximation:

Discretization of Flow Equations Gas storage term We expand the right hand side of the gas equation as follows: Continue Since the first term is equal to the right hand side of the oil equation, multiplied by the solution gas-oil ratio, we can write directly: Continue The second term becomes:

Discretization of Flow Equations The oil and gas equations in discretized form may be written, including the well terms: More where, for the oil equation: and for the gas equation: The derivative terms to be computed numerically for each time step based on the input table to the model, now are: , and

Boundary Conditions Boundary conditions - introduction The boundary conditions for undersaturated oil-gas systems are somewhat simpler than those for saturated oil-gas systems since only one phase is produced in the reservoir. Normally, we inject gas in a grid block at constant surface rate or at constant bottom hole pressure, and produce oil (and solution gas) from a grid block at constant bottom hole pressure, or at constant surface oil rate. Again, we may sometimes want to specify constant reservoir voidage rate, where either the amount of injection of gas is to match a specified rate of oil production at reservoir conditions, so that average reservoir pressure remains constant, or the reservoir production rate is to match a specified gas injection rate. Continue

Boundary Conditions Constant gas injection rate Again, a gas rate term is already included in the gas equation. Thus, for a constant surface gas injection rate of Qgi (negative) in a well in grid block i: Continue It is normally assumed that the injected gas immediately goes into solution with the oil in the injection gridblock. The bottomhole pressure in the well will therefore be a function of the oil mobility around the well, since there is not any free gas present. Thus, the bottom hole presure may be determined from the same expression for the well as for saturated oil-gas flow: and since the gas mobility term is zero: The well constant is as before given by: and:

Boundary Conditions Injection at constant bottom hole pressure Using the previous well equation: The terms must be included in the appropriate coefficients in the pressure solution. At the end of the time step, the above equation may be used to compute the actual gas injection rate for the step.

Boundary Conditions Constant oil production rate For the oil equation, this condition is handled as for the saturated case. Thus, for a constant surface oil production rate of Qoi (positive) in a well in grid block i: Continue Oil production will always be accompanied by solution gas production, and this is accounted for in the gas equation by the term q’oiRsoi. At the end of a time step, after having solved the equations, the bottom hole production pressure for the production well may be calculated using the well equation for oil: Continue As for oil-water systems, production wells in oil-gas systems are normally constrained by a minimum bottom hole pressure. If this is reached, the well should be converted to a constant bottom hole pressure well. The gas-oil ratio, GOR, at the surface, is for undersaturated systems equal to the solution gas-oil ratio:

Boundary Conditions Production at constant reservoir voidage rate If the total production of fluids from a well in block i, at reservoir conditions, is to match the reservoir injection volume so that the reservoir pressure remains approximately constant, the following relationship must be obeyed: Continue Thus: Continue The bottom hole pressure of the production well may be computed at the end of the time step from:

Boundary Conditions Production at constant bottom hole pressure For a production well in grid block i with constant bottom hole pressure, Pbhi, we have an oil rate of: or Continue The solution gas rate is: The terms appearing in the rate expressions will again have to be included in the appropriate matrix coefficients when solving for pressures. At the end of each time step, actual oil rate and GOR are computed.

Solution by IMPES Method The procedure for IMPES solution is similar to the previous cases. To be correct, the method should now be labeled IMPEBPP, for Implicit pressure, Explicit Bubble Point Pressure. We make the same type of assumptions in regard the coefficients in the equations: Continue Having made these approximations, the equations become:

Solution by IMPES Method IMPES oil pressure solution The oil pressure equation for the saturated oil-gas becomes:

Solution by IMPES Method IMPES pressure solution (cont) We then rewrite the oil pressure equation as:

Solution by IMPES Method Modifications for boundary conditions As before, all rate specified well conditions are included in the rate terms qoi’, qgi’ and Rsoiqoi’ , and are already appropriately included in the di term above. For injection of gas at bottom hole pressure specified well conditions, the following expression apply: Continue In a block with a well of this type, the following matrix coefficients are modified:

Solution by IMPES Method For production at bottom hole pressure specified well conditions, we have the following expressions: and Continue In a block with a well of this type, the following matrix coefficients are modified: Again, the pressure equation may now be solved for oil pressures by using Gaussian elimination.

Solution by IMPES Method IMPES bubble point pressure solution Having obtained the oil pressures above, we need to solve for bubble point pressures using either the oil equation or the gas equation. In the following we will use the oil equation for this purpose: Continue Since bubble point pressure only appears as an unknown in the last term on the right side of the oil equation, we may solve for it explicitly: Continue For grid blocks having pressure specified oil production wells, we make appropriate modifications, as discussed previously:

Solution by IMPES Method IMPES bubble point pressure solution (cont) Having obtained oil pressures and water saturations for a given time step, well rates or bottom hole pressures may be computed, if needed, from, from the following expression for an injection well: Continue For a production well: and Continue The surface gas-oil ratio is of course equal to the solution gas-oil ratio: Required adjustments in well rates and well pressures, if constrained by upper or lower limits, are made at the end of each time step, before all coefficients are updated before proceeding to the next time step.

Solution by IMPES Method Applicability of IMPES method Applicability of the IMPES method for undersaturated oil-gas systems is fairly much as for the previously discussed systems. However, due to the fact that changes in bubble point pressure may be rapid, relatively small time step sizes may be required.

All questions are taken from former exams in Reservoir Simulation What are the criteria for undersaturated flow? What are the functional dependencies of Rso and Bo? Next What are the primary unknowns when solving the undersaturated equations? Write the equations for undersatrated flow. Make sketches of Black Oil fluid properties for undersaturated system. Write the two flow equations for oil and gas on discretized forms for a undersaturated system in terms ot transmissibilities, storage coefficients and pressure differences. All questions are taken from former exams in Reservoir Simulation

Nomenclature Back to presentation B - formation volume factor C - storage coefficient c - compressibility, 1/Pa GOR - gas-oil ratio k - permeability, m2 kr - relative permeability, m2 L - lenght, m N - number of grid blocks P - pressure, Pa Pbh - bottom hole pressure, Pa Pbp - bubble point pressure, Pa Pc - capillary pressure, Pa Q, q - flow rate, Sm3/d Rso - solution gas-oil ratio r - radius, m S - saturation T - transmissibility, Sm3/Pa·s t - time, s u - Darcy velocity, m/s WC - well constant x - distance, m x, y, z - spatial coordinate Dx - lenght of grid block, m Dt - time step, s f - porosity l - mobility, m2/Pa·s m - viscosity, Pa·s r - density, kg/m3 Subscripts: d - drainage e - end of reservoir f - fluid G, g - gas i - block number inj - injection ir - irreducible L, l - liquid o - oil S - surface (standard) conditions r - residual r - rock t - total w - water w - well Back to presentation

General information About the author Title: Undersaturated Oil-Gas Simulation - IMPES Solution Teacher(s): Jon Kleppe Assistant(s): Szczepan Polak Abstract: Criteria for undersaturated oil conditions. Black Oil fluid properties for undersaturated oil. IMPES solution for undersaturated system. Keywords: undersaturated oil-gas simulation, black oil fluid properties, IMPES, bubble point pressure Topic discipline: Reservoir Engineering -> Reservoir Simulation Level: 4 Prerequisites: Good knowledge of reservoir engineering Learning goals: Learn basic principles of Reservoir Simulation Size in megabytes: 1.0 Software requirements: - Estimated time to complete: 45 minutes Copyright information: The author has copyright to the module About the author

FAQ

References Aziz, K. and Settari, A.: Petroleum Reservoir Simulation, Applied Science Publishers LTD, London (1979) Mattax, C.C. and Kyte, R.L.: Reservoir Simulation, Monograph Series, SPE, Richardson, TX (1990) Skjæveland, S.M. and Kleppe J.: Recent Advances in Improved Oil Recovery Methods for North Sea Sandstone Reservoirs, SPOR Monograph, Norvegian Petroleum Directoriate, Stavanger 1992

Summary

About the Author kleppe@ipt.ntnu.no +47 73 59 49 33 Name Jon Kleppe Position Professor at Department of Petroleum Engineering and Applied Geophysics at NTNU Address: NTNU S.P. Andersensvei 15A 7491 Trondheim E-mail: kleppe@ipt.ntnu.no Phone: +47 73 59 49 33 Web: http://iptibm3.ipt.ntnu.no/~kleppe/