Abstract:
In some embodiments, a method for locally lumped equation of state fluid characterization can include determining a set of components for the material balance calculations for a plurality of grid blocks of a reservoir. The plurality of grid blocks can experience different recovery methods between them. Lumping schemes can be determined for the plurality of grid blocks. Phase behavior calculations can be performed on the plurality of grid blocks, wherein different lumping schemes can be used across the plurality of grid blocks.

Description:
BACKGROUND 
       [0001]    Equation of State (EOS) fluid characterization can be used to model the behavior of hydrocarbon reservoir fluids when variation in the fluid composition has a significant influence on the recovery of the hydrocarbons. The EOS fluid characterizations can be used as the parameters of PVT equations that relate the pressure, volume and temperature (PVT) of a system. These equations of state can be used to predict equilibrium conditions such as the number of phases that are present in the fluid (e.g., single phase or multiple phases). The equations can also be used to describe the properties of the phases, such as the density of the phase, and the composition of each phase. 
         [0002]    Hydrocarbon fluids may contain thousands of components. It is impractical to determine the properties of all of these components and to use this number of components in simulation calculations, so EOS characterizations reduce the number of components by grouping together all the components in a range of molecular weights. Each group of components is referred to as a pseudo-component. The properties of these pseudo-components are adjusted so that the fluid properties give acceptable agreement with laboratory data over the range of pressures, temperatures and fluid composition likely to be encountered in the reservoir and the production/injection facilities. For example, for each pseudo-component of a fluid, the molecular weight, the critical temperature, and the critical pressure may all need to be adjusted. Additionally, properties that are used to relate any two pseudo-components (e.g., binary interaction coefficients) may also be adjusted. The cost of calculating fluid properties using an EOS characterization increases greatly as the number of lumped components increases, so it is advantageous to use the fewest number of lumped components that can give an acceptable match to the laboratory data. 
     
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         [0003]      FIG. 1  illustrates a reservoir with a different recovery method used in each of two regions. 
           [0004]      FIG. 2  illustrates a table of one embodiment of component lumping. 
           [0005]      FIG. 3  illustrates a flowchart of an embodiment of a method for EOS fluid characterization using component lumping. 
           [0006]      FIG. 4  illustrates a diagram of an embodiment of a wireline logging operation in accordance with various embodiments. 
       
    
    
     DETAILED DESCRIPTION 
       [0007]    During production operations, simulations can be used to model the properties of fluid reservoirs that may be subjected to different recovery mechanisms (e.g. gravity drainage, fluid expansion, displacement by water, gas) A reservoir can be subjected to multiple different recovery mechanisms in different geographical locations (e.g. water displacement near an aquifer, gas expansion in a gas cap), and/or for different periods of time. (e.g., because of the commencement or termination of gas, water, steam, solvent injection). Each recovery mechanism has a different sensitivity to the composition of the reservoir and injected fluids, and the simulations should take this into account. 
         [0008]    The embodiments herein encompass a method that locally lumps a plurality of components, of the thousands of components that can typically make up a hydrocarbon fluid, to be represented by usually a smaller number of pseudo-components (i.e., EOS characterization). Components are lumped together to be represented by a pseudo-component having similar properties as the components being replaced. Unlike the typical methods of EOS characterization, the embodiments herein provide locally lumped EOS characterization such that the characterization can vary from point-to-point across the reservoir as the recovery mechanisms vary across the reservoir. 
         [0009]      FIG. 1  illustrates a reservoir with a different recovery method used in each of two regions, and a corresponding different recovery mechanism in each of these regions. This reservoir is for purposes of illustration only as the present embodiments are not limited to any certain quantity of regions nor to any certain recovery mechanism. In other words, the locally lumped EOS characterization method can adapt to any number and type of recovery mechanisms across a reservoir, generating a different group of pseudo-components for each different recovery mechanism region. 
         [0010]      FIG. 1  shows a gas injection region  101  and a water injection region  102  within the same reservoir  100 . In other words, in order to recover the hydrocarbon fluid in the reservoir, the water injection region uses a water injection recovery mechanism and the gas injection region uses a gas injection recovery mechanism. 
         [0011]    Since the water injection recovery mechanism introduces fewer new components than the gas injection recovery mechanism, the water injection recovery mechanism can achieve an acceptable accuracy for phase behavior calculations with a fewer number of pseudo-components (NC 1  components) than the gas injection recovery mechanism pseudo-components (NC 2  components). For component mass balance calculations, the components used in the gas injection recovery mechanism can be used throughout the reservoir  100 . However, in the water injection region  102 , these components are first lumped into the NC 1  components for the water injection region  102  and the phase behavior calculations can then be performed using the EOS characterization for the water injection recovery mechanism. The resulting phase compositions can then be de-lumped and the derivatives of the fluid properties (e.g., phase densities, saturations, phase compositions) with respect to the NC 1  components can also be de-lumped in order to be expressed with respect to the original NC 2  components. 
         [0012]    The phase behavior calculations with the lumped components can take less processing time than the delumped EOS calculations. This can reduce the processing time used for the reservoir simulation. This may be particularly true if the simulation is run using an Implicit Pressure Explicit Saturation (IMPES) formulation, where the component masses are solved explicitly, rather than an implicit formulation, where the component masses are solved implicitly. The implicit formulation results in a much larger system of equations and uses a relatively large amount of processing time to solve the linear system of equations, so the phase behavior calculations can use a smaller proportion of the total processing time. 
         [0013]    The locally lumped EOS characterization method can be used with any lumping scheme. However, the lumped components of  FIG. 2  can more closely reproduce the solution that would be obtained if the mass balance was performed using the lumped components. The lumped components can be chosen so that each of the delumped components makes up a part (or the whole) of only one of the lumped components. 
         [0014]      FIG. 2  illustrates a table of one embodiment of component lumping. The number of lumped components and/or their associated delumped components are for purposes of illustration only. The quantity of delumped components represented by each lumped component can vary with each embodiment. Additionally, the particular delumped components to be lumped with a particular lumped component can also vary with each embodiment. 
         [0015]    In this figure, the lumped fluid characterization for the water injection recovery mechanism uses six pseudo-components represented by C1 through C6. The lumped fluid characterization used for the gas injection recovery mechanism uses eleven pseudo-components represented as G1 through G11. For the water injection recovery mechanism, pseudo-component C1 is the same as G1 for the gas injection recovery mechanism, C2 is the sum of G2 and G3, C3 is the sum of G4 and G5, C4 is the sum of G6 and G7, C5 is the sum of G8 and G9, and C6 is the sum of G10 and G11. The illustrated choice of lumping has the property that the mass balance, using the mass of the components of the second characterization as the primary variables, can give the same result as if the components of the first characterization had been used as the primary variables. 
         [0016]    If the recovery mechanism changes during the simulation, the choice of lumping can be changed to be appropriate for the new recovery mechanism. For example, if part of the reservoir  100  is switched from water injection to gas injection, the EOS calculations could be performed with a different set of lumped components and corresponding characterization. 
         [0017]    The choice of lumping could also be dynamically chosen based on changes in composition in a grid block. These changes might be a different recovery method being used or elements from a recovery method for one portion of the reservoir invading another portion of the reservoir. For example, if the injected gas of  FIG. 1  invades the water injection region  102 , the components in the water injection region  102  will change. Thus, the choice of lumped components could be switched dynamically to take into account the additional components in the water injection region  102 . 
         [0018]    However, a change in the lumping and EOS characterization will result in slightly different phase densities and saturations, thus introducing a volume balance error (i.e., the fluid volume no longer exactly equals the pore volume in the grid block). This volume balance error will result in a spurious pressure change in the grid block on the next iteration of the solution. To avoid this, a onetime adjustment can be made to the pore volume when the characterization is switched. 
         [0019]      FIG. 3  illustrates a flowchart of an embodiment for locally lumped EOS fluid characterization in reservoir simulations. Prior to the simulation, PVT analysis is performed to develop EOS characterizations for each recovery mechanism  301  that will be encountered in the reservoir. Each characterization can have a different number of pseudo-components, and different properties for any pseudo-components that are in common. The number of components for each characterization should be the fewest that are capable of accurately representing the phase behavior for each recovery mechanism. The material balance components used for the material balance calculations are determined by the characterization with the largest number of components. The reservoir is divided up into grid blocks, and for each grid block the mass of the material balance components is conserved. The material balance components for the plurality of grid blocks of the reservoir is determined wherein different recovery mechanism are experienced for local groupings of grid blocks. 
         [0020]    Each grid block is assigned one of the EOS characterizations  303  (e.g., lumping scheme), depending on the recovery mechanism that is present at the location of the grid block. If the characterization assigned to a grid block is not the characterization associated with the material balance components, then the PVT properties of the fluid in the grid block (e.g. phase compositions, phase volume, phase density and phase viscosity) are calculated by first lumping the components into the components associated with the characterization, calculating the properties using the lumped components, then delumping the phase compositions and the derivatives of phase volumes, densities and viscosities to get these quantities in terms of the material balance components. The process can be referred to as locally lumped EOS fluid characterizations. 
         [0021]    In an embodiment, the components from a first recovery mechanism having a greater number of components can be lumped into the components for a second recovery mechanism having the least number of components (different from the first recovery mechanism). The reduced number of components can be referred to as the pseudo-components representing the greater number of components since they can represent the greater number of components in phase behavior calculations, thus, reducing the processor time used for the reservoir simulation. As seen in  FIG. 2  and discussed previously, each pseudo-component can represent one or more of the material balance components. 
         [0022]    Based on the recovery mechanism and/or fluid properties in a particular grid block or group of grid blocks, phase behavior calculations can be performed across the reservoir on a grid block or group of grid blocks using different lumping schemes based on a composition and/or recovery method for the grid block or group of grid blocks  305 . The resulting phase compositions are delumped  307  and the fluid properties (e.g., phase densities and saturations, phase compositions) with respect to the lumped components are delumped and expressed with respect to the original delumped components  309 . Using this locally lumped EOS fluid characterization method, different lumping schemes can be applied to different grid blocks and/or at different times (e.g., when the recovery mechanism of a grid block changes). 
         [0023]    Data obtained during a wireline sampling operation can be used in the compositional reservoir simulations. For example, after a recovery operation has started on a reservoir, a wireline sampling operation can be used to obtain a fluid sample that can be used to determine the fluid properties at a particular location of the reservoir due to components being added to the reservoir by a particular recovery mechanism. If necessary, the data for the reservoir simulation model can be adjusted to improve the match between the measured fluid properties measured on the sample, and the fluid properties predicted by using the original characterization at the corresponding grid block in the reservoir simulation. Adjustments of this kind improve the accuracy of the reservoir simulation, and make it more reliable for predicting hydrocarbon recovery in response to changes in how the reservoir is operated. 
         [0024]      FIG. 4  illustrates generally an example of a wireline sampling system. A hoist  406  may be included as a portion of a platform  402 , such as coupled to a derrick  404 , and used to raise or lower equipment such as a wireline sonde  410  into or out of a borehole. In this wireline example, a cable  442  may provide a communicative coupling between a logging facility  444  (e.g., including a processor circuit  445  including memory or other storage or control circuitry) and the sonde  410 . In this manner, information about the reservoir  418  may be obtained. The processor circuit  445  may be configured to execute any methods for characterizing fluids, locally lumping a plurality of components, and/or reservoir simulations. 
         [0025]    In the foregoing Detailed Description, it can be seen that various features are grouped together in a single embodiment for the purpose of streamlining the disclosure. This method of disclosure is not to be interpreted as reflecting an intention that the claimed embodiments require more features than are expressly recited in each claim. Rather, as the following claims reflect, inventive subject matter lies in less than all features of a single disclosed embodiment. Thus the following claims are hereby incorporated into the Detailed Description, with each claim standing on its own as a separate embodiment.