FEHM: A Control Volume Finite Element Code For Simulating .

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FEHM: A control volume finite element code for simulating subsurface multi-phasemulti-fluid heat and mass transferMay 18, 2007 LAUR-07-3359George ZyvoloskiTechnical Staff MemberEarth and Environmental Sciences DivisionLos Alamos National LaboratoryLos Alamos, NM 87544ABSTRACTThe Subsurface Flow and Transport Team at the Los Alamos National Laboratory(LANL) has been involved in large scale projects including performance assessment ofYucca Mountain, Environmental Remediation of the Nevada Test Site, the LANLGroundwater Protection Program and geologic CO2 sequestration. Subsurface physics hasranged from single fluid/single phase fluid flow when simulating basin scale groundwateraquifers to multi-fluid/multi-phase fluid flow when simulating the movement of air andwater (with boiling and condensing) in the unsaturated zone surrounding a potentialnuclear waste storage facility. These and other projects have motivated the developmentof software to assist in both scientific discovery and technical evaluation. LANL’s FEHM(Finite Element Heat and Mass) computer code simulates complex coupled subsurfaceprocesses as well flow in large and geologically complex basins. Its development hasspanned several decades; a time over which the art and science of subsurface flow andtransport simulation has dramatically evolved. For most early researchers, models wereused primarily as tools for understanding subsurface processes. Subsequently, in additionto addressing purely scientific questions, models were used in technical evaluation roles.Advanced model analysis requires a detailed understanding of model errors (numericaldispersion and truncation) as well as those associated with the application (conceptualand calibration) Application errors are evaluated through exploration of model andparameter sensitivities and uncertainties. The development of FEHM has been motivatedsubsurface physics of applications and also by the requirements of model calibration,uncertainty quantification, and error analysis. FEHM possesses unique features andcapabilities that are of general interest to the subsurface flow and transport communityand it is well suited to hydrology, geothermal, and petroleum reservoir applications. Asthe creator and lead developer of FEHM, I will outline the development history ofFEHM, describe its general software structure and numerical formulations, and some ofits unique features. These features range from novel representations of equations of stateto features that allow accurate representation of wellbores and other sub-grid scalephenomena. I will also compare the numerical method used in FEHM, the controlvolume finite element method (CVFE) with the finite element (FE) method, the finitedifference (FD) method, and the integrated finite difference (IFD) method. Finally Icompare FEHM with other software of which I am familiar.

OUTLINEThe BACKGROUND AND HISTORICAL DEVELOPMENT section traces thehistorical development of FEHM. This essentially mirrors the evolution of the controlvolume finite element method (CVFE) method and the simulation of coupled subsurfacephysics including, most notably, heat. The NUMERICAL FORMULATIONSUMMARY outlines the CVFE method and compares it to finite element (FE), finitedifference (FD) and integrated finite difference (IDF) methods. SUBSURFACEPHYSICIS section briefly describes the physics packages available and the associatedvariables. SOLUTION OF THE NONLINEAR EQUATIONS section describes howFEHM solves the nonlinear algebraic equations representing the coupled mass andenergy balance equations. The Newton-Raphson method (with analytical derivatives),various pre-conditioning and degree-of-freedom reduction schemes, and thepreconditioned Krylov space solver for linear equation, are explained. The TOOLS FORQUANTITATIVE ANALYSIS section outlines the issues associated with quantifyingerrors when representing hydrostatrigraphy on numerical grids, including a discussion ofthe impacts of grid generation. This section also lists external software and interfacesfrequently used with FEHM during model calibration and uncertainty/sensitivityanalyses. The section titled EXPLOITING UNSTRUCTURED GRIDS discussesseveral unique FEHM features that make use of the unstructured grid connectivity tocouple models developed with different software. It includes an account of how FEHMefficiently generates and solves double porosity models and how wellbores can be“dropped into” pre-existing numerical grids. The section titled APPLICATIONS give abrief overview of current applications. The FEHM CODE STRUCTURE AND INPUTsection outlines the basic workings of FEHM and describes features that facilitate modeltesting. Finally, the RESEARCH PRIORITIES section describes several activeresearch areas being pursued in the development of FEHM and the CONCLUSIONsection draws some general conclusions.This article does not describe the extensive transport capabilities of FEHM that includesmulti-species advection/dispersion, coupled reactive geochemistry, and particle tracking(see Viswanathan, 1996, Viswanathan et al., 1998; Hammond, 1999, and Robinson et al.,2000 for details). The fully coupled, thermal-hydrologic and mechanical (THM) moduleis also not described other than noting the extra stiffness matrix terms required over thoseneeded for the flow and transport solution and the suitability of the CVFE method forthese applications. See Kelkar and Zyvoloski (1992) and Bower and Zyvoloski (1997)for details on this capability.BACKGROUND AND HISTORICAL DEVELOPMENTThe numerical background of the FEHM computer code can be traced to the early 1970s.Before this time, finite element methods were almost exclusively used in solidmechanics, not flow problems. Applications to field problems (heat conduction) werebeing published, but nonlinear groundwater applications were rare; Neuman and

Witherspoon (1970), Neuman (1973), and Dalen (1979) were notable exceptions.Neuman (1973) solved the unsaturated-saturated zone flow equations with a free watertable using a traditional finite element code. Table 1 summarizes the historicaldevelopment of FEHM. Zyvoloski et al. (1976) published a finite element solution tounsaturated zone equations with application to shallow infiltration. The formulationZyvoloski et al. (1976) used was different from previous finite element formulations inthat the equations were developed by node rather than by element. They also expandedthe nonlinear hydraulic conductivity in low–order, finite element basis functions insteadof the usual method of evaluating these nonlinearities at integration (quadrature) points oras element averages. The element stiffness coefficients were then formed analytically.These procedures effectively separated the fluid and geometric parts of the approximatingalgebraic equations in a manner similar to what later became know as the CVFE method.The details of this formulation are given by Zyvoloski (1975). The nodal construction ofthe equations also facilitated storage of neighboring nodes in modified compressed sparserow format (CSR) (George and Liu, 1981; Zyvoloski, 1983) where only the nonzeroneighbors of the solution matrices are stored and the starting positions of each row areidentified at the beginning of the connectivity array. While Zyvoloski et al. (1976)described the predecessor of the CVFE discretization currently used in FEHM, theformulation for fully coupled subsurface heat and mass transfer equations was developedwhile the author was a post-doctoral fellow at the University of Auckland, New Zealand.Here, motivated by the need to solve the two–phase coupled subsurface heat and fluidflow equations for geothermal applications, Zyvoloski et al. (1979) formulated the heatand mass balance equations in primitive (mass conservative) form rather than with theusual linearized equations (Mercer and Pinder, 1973). The equations were solved fullyimplicitly rather than using the Implicit Pressure Explicit Saturation (IMPES) formulationthat was common at the time in petroleum industry software (Thomas, 1979). Zyvoloskiet al. (1979) also used a FD formulation to discretize the fully coupled mass and energybalance equations because finite-element-based solutions to multiphase flow problemslack numerical stability (Mercer and Faust 1975; Faust and Mercer, 1976). Zyvoloski etal (1979) used Newton-Raphson (NR) iteration and introduced a method for solving thecoupled system with an algebraic reduction in the effective degrees of freedom from twounknowns per node to one unknown per node to effectively “pre-condition” the linearsystem of equations, the solution of which provides the NR variable updates. The detailsare described in the section entitled SOLUTION OF THE NONLINEAREQUATIONS. After the solution of this reduced algebraic system of equations, the prefactored variable is recovered through back-substitution. This method of solving the fullycoupled heat and mass balance equations in geothermal reservoirs was extended to water,water vapor, heat, and non-condensable CO2 gas by Zyvoloski and O’Sullivan (1980).The three independent variables in this application were again solved with an algebraicreduction of variables. These techniques, which solve the coupled heat and mass transferequations, were combined with the early CVFE discretization work to form an earlyversion of the current FEHM computer code. This combination of techniques was firstdescribed by Zyvoloski (1983). Similar to Zyvoloski et al. (1976), the finite elementequations developed by Zyvoloski (1983) were constructed with the row and geometricpart of the finite element stiffness matrix separated from the fluid part and stored inmodified CSR format. This required that the equation parameters to be defined on nodes

rather than on elements. It was noted in the paper that using node point quadrature (alsoknown as Lobatto quadrature) instead of the usual Gauss quadrature points resulted adiagonal capacitance matrix and the usual five point FD stencil for two-dimensionalproblems when applied to numerical grids constructed of orthogonal quadrilateralelements. The paper also studied the relative performance of the node point quadrature(equivalent to CVFE) and the Gauss quadrature (equivalent to the FE). It was concludedthat the node point quadrature CVFE-like) option performed better than the Gaussquadrature (FEM) option for the nonlinear convection-dominated problems studied.The next breakthrough came in the iterative solution of linear equations, often known asthe “inner” iteration when used with a NR “outer” iteration. In the early 1980s,pre-conditioned conjugate-gradient methods and their non-symmetric variants began toappear in petroleum industry software literature for multi-phase subsurface fluid flowapplications (Behie and Vinsome, 1982). These applications were for structured FD gridsand were not available for FE or CVFE codes. Zyvoloski (1986) developed a variablypre-conditioned Krylov acceleration method using ORTHOMIN acceleration with amodified CSR format. The pre-conditioning part of the algorithm consists of incompletelower-upper (ILU) factorization, which starts with the nodal connectivity and addsconnections during each factorization step. This was the first time that a preconditioner,based on incomplete factorization, was reported for an unstructured grid application.Instead of completing the LU process, only one or two factorization steps are performed.Thus the label ILU(n), where ILU stands for incomplete LU factorization, and nrepresents the number of factorization steps. With n 1, only those operations are donethat affect matrix positions of the original connectivity. With n 2, addition nodalconnections occur and for a typical FD application, the connectivity for the ILUpreconditioner is about 50% greater than the nodal connectivity for the FD grid stencil.With the structured connectivity of FD methods, additional connections for thefactorization steps can be determined rather easily for a given node. FE and CVFEmethods use an unstructured connectivity and a symbolic factorization must be done todetermine the positions of additional terms that occur during the factorization steps.Zyvoloski (1986) obtained an order of magnitude decrease in computer runtime inaddition to significantly less computer memory usage with this linear solver whencompared with the direct solvers previously used in FEHM. This has been the ‘core’linear equation solver in FEHM ever since. Conversations with Manteuffel (1980) helpedguide this programming effort. The ORTHOMIN acceleration was replaced with themore efficient GMRES and BCGSTAB (van der Vorst, 1992) acceleration methods andthere have also been improvements in the symbolic factorization. Addition details areprovided in the SOLUTION OF THE NONLINEAR EQUATIONS section.FEHM is a large computer code comprising roughly 450 subroutines and approximately200,000 lines of code with development and usage guided by funding trends of ourresearch group at LANL and major collaborators. Several hundred no-cost FEHMlicenses to individuals and institutions have been distributed world wide. This papersummarizes FEHM in sufficient detail to inform the reader of most of FEHM’scapabilities. With the advent of FORTRAN 90, FEHM common bocks were replaced

with use modules and dynamic memory allocation. Continued releases of new versionsgenerally represent additional capabilities.NUMERICAL FORMULATION SUMMARYIn the author’s opinion CVFE evolved from researchers need to solve nonlinear problemswith finite elements. Besides the author’s work the reader is referred to Forsyth (1990)and Fung (1992) for more detail. A detailed numerical development of the CVFE methodused in FEHM is provided by Zyvoloski (2007). In the rest of this section a numericaldefinition of the CVFE method will be provided and the method will be compared to thefinite element method (FEM), the finite difference method (FDM), and the integratedfinite difference method (IFDM). Later in the paper, FEHM will be compared withseveral well known software packages.As noted in the background section above, the finite element method can be madeequivalent to the finite difference method by choosing quadrature points for theevaluation of the stiffness matrix integral that are positioned at the nodes. The nodalquadrature points make the inputting of parameters at nodes, like FD methods, veryconvenient. If these procedures are applied to orthogonal four node quadrilateral andhexahedral elements, the standard five point (2D) and seven point (3D) FD stencils result.If these procedures are applied to triangular or tetrahedral elements the result is a methodequivalent to the IFD method (described later). The geometric terms associated with theCVFE method are defined in Figure 1. The internodal area divided by distance (Aij/Δdij)term, also called the area factor, is defined for both orthogonal (Fig. 1a) and nonorthogonal grids (Fig. 1b). The area factors are formed by the intersection ofperpendicular bisectors (PEBI) of the edges of the elements. This ensures that the areafactors are perpendicular to the control volume boundary. In particular, note the areafactor A35 for the connection between nodes 3 and 5 is zero for the orthogonal grid andnon zero for the non orthogonal grid. The resulting connectivity for the orthogonal case isthe standard five-point FD stencil. The CVFE, block centered FD, and IFD methodswould be equivalent on such (orthogonal) grids. In fact, the grid generation softwaretypically used for large-scale FEHM applications, the Los Alamos Grid Toolkit (LaGriT,2007) generates nodal volumes and area factors (Aij/Δdij) from a finite element definitionof triangles (with unit depth) , tetrahedrals, quadrilaterals (with unit depth), andhexahedrals. In this author’s opinion the only difference between IFD and CVFEmethods is the underlying finite element grid which accompanies the CVFE method.Comparison with the FE method. CVFE methods have several advantages compared tothe traditional FE method when used to simulate unsaturated groundwater flow. Considerthe equation for the conservation of water in the unsaturated zone:

(θρ wφ ) t kρ w k '(θ ) ( pw ρ w gz ) μw .(1)where θ is saturation, ρw is the water density, φ is the porosity, t is the time, z iselevation, g is the gravitational constant, μ w is viscosity, pw is pressure, k is intrinsicpermeability and k ‘(θ) is relative permeability. Equation 1 can be highly nonlinear andis equivalent to Richards’ Equation (Richards, 1931) with the specification of a capillaryrelationship between θ and pw . For unconditional stability, the nonlinear relativepermeability, k‘(θ), must be upwinded in any numerical method. For FE methods, this iseither not done or it is computationally inefficient because of the necessity to recomputethe stiffness matrix. For the CVFE method, it is easy. Because of the nodal input ofparameters, the separation of the geometric and the nodal nonlinear terms, and the nodeby node assembly of the numerical analog of Eq. 1, the CVFE method naturally identifiesnode pairs and can apply any internodal evaluation technique, including harmonicaveraging or upwinding, at the control volume boundary. While FEHM users have theability to chose the internodal evaluation method, they are always recommended to usefull upwinding for nonlinear or advective terms The nodal connectivity is contained incompressed sparse row (CSR) format as opposed to the element connectivity array that istypical of FE methods. The nodal connectivity greatly facilitates the formulation ofnonlinear equations (requiring upwinding) in a Newton Raphson (NR) iteration ratherthan the Picard iteration commonly found in FE software. This in turn results in theCVFE method having greater computational efficiency than FE method.It should be noted here that all control volume discretization methods (FD, IFD, CVFE)have an advantage over typical FE methods in mass conservation. These methods arelocally conservative and the standard FE method is not. Mixed FE methods do conservemass locally, but at a considerable cost in efficiency. The lack of local mass conservationhas the potential to cause significant errors in nonlinear problems with large grid changes.This author sees no disadvantages in the CVFE method compared to the FE method forhighly nonlinear subsurface flow applications (e. g. Richards’ Equation). For the solutionof large scale confined aquifer applications, a linear problem requiring no iteration, theremight be little difference between the two methods.Comparison with the FD method. It was noted previously that the CVFE methodapplied on a grid with orthogonal quadrilaterals (2D) or hexahedrals (3D) produced thestandard five point and seven point finite difference stencils. The two methods bothreadily implement upwinding and NR iteration in the solution of nonlinear equations. TheCFVE method has significant advantage in that it can also build control volumes fromtriangles and tetrahedrals. This allows spatially variable hydrostratigraphy and otherinternal boundaries to be represented accurately. Figures 2 and 3 give examples of CVFEgrids with grid resolution that varies in accordance with stratigraphic constraints.Additional discussion will occur when quality grids are presented.

Traditional FD methods embodied in the popular MODFLOW (Harbaugh et al., 2000)software package have a structured connectivity that allows the neighboring nodes to beidentified without the use of either an element or nodal connectivity array. Efficientsoftware is readily available for structured connectivity that solves the linear equationsthat result from the finite difference equations. This gives a computational advantage inboth speed and computer memory requirements over the FE, IFD, and CVFE methodsthat use unstructured connectivity. Zyvoloski and Vessilinov (2006) estimated that thepenalty for unstructured connectivity was 20 -50 % extra CPU time to solve an identicalproblem. Because the FE method must recalculate the stiffness matrix at each iteration,this penalty is greater, for problems requiring iteration, for the FE method than the CVFEmethod which separates the nonlinear and geometric parts on the internodal flux terms.There is considerable extra storage required for the unstructured connectivity methods.This will be discusses later when FEHM is compared to the FD code MODFLOW. Thesedisadvantages disappear when a fine resolution region is required in a large numericalgrid. Here, the fine resolution will propagate to the boundary in the FD method, oftenreferred to as streaking, where as the unstructured methods have the ability to localizethe refinement. Localization can only be achieved with a FD method through iteration,with additional model runs, of the solutions on the fine grid and coarse grid parts of theproblem (Mehl and Hill, 2002).Comparison with the IFD method. In many applications the IFD and CVFE methodsare identical. One of the most well known IFD based computer codes, TOUGH2 (Pruess,1991), needs a connectivity matrix, nodal coordinates, nodal volumes, and controlvolume face areas to be provided to the code as input data. For relatively complicatedproblems, this is accomplished by external grid generation software. Internally, FD, IFDand CVFE solve the same numerical equations. For Eq. 1 this would be: (θρwφ) n 1 (θρwφ) n k '(θ)kρw Aij ii Vi pw pwi ( ρwg)ij ( z j zi ) 0 Δtμw ij Δdij jneighbor ()(2)cellsThe summation refers to neighboring nodes, j, connected to node i. Here the ( )ijrepresents some inter-nodal averaging. The term Vi is the volume of the gridblocksurrounding node i. The area factor (Aij/Δdij) has been described earlier. Harmonic,arithmetic, and upwinded internodal evaluation can all be used with the IFD method. Theupwinding of the two point fluxes (depending only on i and j nodes) facilitates stable andmonotonic numerical simulation of multiphase flow.Differences between the IFD and CVFE methods are largely based on where and whenthe gridblock volume and area factors are calculated. IFD methods do not have anunderlying FE grid. In CVFE software (e. g. FEHM or LaGRit) the traditional FEelement definitions and nodal coordinates are inputs and they are used to calculate boththe nodal connectivity and the area factors. If the elements used are orthogonal (or righttriangles and right tetrahedrals) both methods will produce identical connectivities andarea factors. This is shown in Figure 1a. Note that the areas are constructed by the PEBI

method described earlier and this leads naturally to zero diagonal area (i.e., A35 0) inFigure 1a and the elimination of the diagonal connection. This results in the standard FDstencil. If the elements are non orthogonal as is shown in Figure 1b, then the CVFEsoftware will automatically add connections during the course of creating the area factorsas required to produce a quality grid (discussed later). The IFD software requires thatnodal connectivities (not element definitions) be provided as input. Thus, the additionalconnections required for non orthogonal grids are not easy to obtain As a practicalapproach, IFD methods often ignore the requirement of additional terms and use a simpleFD stencil (Haukwa et al., 2003) even on non orthogonal grids. The CVFE methodnaturally conserves computer memory by only adding additional connections whererequired by grid geometry.The second difference is that the stiffness matrix calculations available with the CVFEmethod as part of its FE legacy are invaluable when coupling the thermal, hydrologic,and mechanical behavior (THM).In a CVFE code, the variables and equationparameters for both the flow and stress equations are co-located at gridblock centers andthe non isotropic terms (e. g. the xy, xz, yz terms) needed for the stress equations areeasily calculated. This functionality is not available in IFD software; the fully coupledTHM simulations are difficult if not impossible in IFD software. This functionality isavailable in FE software and coupling would be possible for mildly nonlinear problemswith the caveats listed previously in the discussion on the comparison between the FEand CVFE methods.SUBSURFACE PHYSICISFEHM contains a large suite of subsurface physics modules that are used for a variety ofapplications. Table 2 lists the physics modules that are tested and in common use. Thetable also includes the primary variable set and selected references. The oldest module isthe water, water vapor, and energy flow that has been used for geothermal applications.Of particular interest to geothermal applications is the inclusion (in the usual suite of rockcompressibility of a nonlinear fracture opening relationship, the “Gangi model” (Gangi,1978) that relates the permeability and aperture of fractures to fracture roughness andearth stresses. This relationship made it possible to accurately model a very complicatedgeothermal reservoir that was created through hydraulic fracturing (Tenma et. al., 2007).The newest physics module is the non isothermal CO2-water module that is used in CO2sequestration studies. The module includes a novel tabular equation of state (EOS) thatallows for efficient calculation of CO2 properties and phase transitions even in the supercritical range. This EOS formulation will be detailed shortly. In addition, feedback fromthe transport module (Robinson et. al, 2000) in FEHM is available in a timestep-laggedmanner to the flow solution. For example, if the reactive transport solution in FEHMpredicts that silica will precipitate in a fracture, then the porosity and permeability can bechanged accordingly. Of course, any explicit update will put limitations on the time stepsize.While FEHM uses several different functional representations for the EOS of fluids androck parameters, two that are unique to FEHM are worth mentioning. The first is the use

of rational polynomials is the EOS for water and water vapor. Rational functionapproximations and innovative tabular equations of state facilitate the evaluationanalytical derivatives in FEHM’s NR iteration. Rational function approximations (ratiosof polynomials) accurately represent water properties (less than a few tenths of percenterror over the ranges given above) while providing derivatives, because of thepolynomial functions, at virtually no additional CPU cost. Complete third-orderpolynomials in pressure and temperature are used in both the numerator and denominator.For example, the density is approximated as:ρ ( P, T ) Y ( P, T ),Z ( P, T )(3)whereY ( P, T ) Y0 Y1 P Y2 P 2 Y3 P 3 Y4T Y5T 2 Y6T 3 Y7 PT Y8 P 2T Y9 PT 2 ,(4)andZ ( P, T ) Z 0 Z1 P Z 2 P 2 Z 3 P 3 Z 4T Z 5T 2 Z 6T 3 Z 7 PT Z8 P 2T Z 9 PT 2 . (5)This type of relationship provides an accurate method for determining parameter valuesover a wide range of pressures and temperatures, as well as allowing derivatives withrespect to pressure and temperature to be computed easily (Zyvoloski et al., 1992).Polynomial coefficients were obtained using a Levenberg-Marquardt-based minimizationmethod with a differential correction algorithm (Blackett, 1996) to fit data from theNational Bureau of Standards OSRD Database 10, the database used for the NBS/NRCSteam Tables (Harr et al., 1984). The properties of the liquid (water) and water vaporphases are represented over wide range of pressures (0.001 to 110 MPa) and temperatures(0.5 to 360oC).The other unique EOS uses a variably-spaced tabular lookup tables for representing theproperties of CO2 in all phase states including “supercritical fluid”. The details aredescribed in Doherty (2006). The method may be outlined with the aid of Figure 4 andFigure 5. Figure 4 depicts how a phase transition line (ie. the saturation line) isrepresented in a variably-spaced grid. This arrangement allows very fine grid spacing inareas where properties change rapidly, while not using massive amount of computermemory. In the tables of CO2 properties in FEHM, temperature increments as low as0.01oC are used near the critical point (7.38 Mpa, 31.1oC) and up to 1oC elsewhere. Thisallows the use of tables that have thousands to millions of points rather than billions ofpoints. The data for both liquid and vapor and also stored in a single table in an intuitiveand natural way. Figure 5 shows a close-up of an element of the lookup table that has aphase transition line. There is a property discontinuity at the liquid vapor interface andtriangular interpolation is used on each side of the phase transition line. In a cell withoutthe phase transition line, bilinear interpolation is used. With two phase calculations, the

temperature becomes a function of pressure and the above method smoothly representsthis behavior because the phase transition line is an integral part of the table.SOLUTION OF THE NONLINEAR EQUATIONSThe efficient solution of coupled nonlinear problems is critical to the simulation of largescale applications. FEHM uses a Newton-Raphson (NR) iteration (the “outer loop”) tosolve the nonlinear material and energy balance equations. FEHM differs from similiarmulti-physics computer codes (e.g. TOUGH2, see Pruess (1991), and NUFT, seeNitao(1998)) in that the NR derivatives are formed analytically, as opposed tonumerically, because this generally leads to faster convergence of the very stiff nonlinearsystem of equations that often arise when investigating widely varying parameter sets asmight be encountered during model calibration . However, it also can lead to slowerdevelopment of new physics modules (i.e., tracking down programming errors). A porousflow simulator that solves energy and mass balance equations requires the functionaldependence of the phase densities, the phase enthalpies, and the phase viscosities on Tand P for all fluids in a system. For the NR iteration, FEHM requires t

volume finite element method (CVFE) method and the simulation of coupled subsurface physics including, most notably, heat. The NUMERICAL FORMULATION SUMMARY outlines the CVFE method and compares it to finite element (FE), finite difference (FD) and integrated finite difference (IDF) methods. SUBSURFACE

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