+ All Categories
Home > Documents > Meeting the Thermal-Hydraulic Analysis Needs for … MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS...

Meeting the Thermal-Hydraulic Analysis Needs for … MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS...

Date post: 07-May-2018
Category:
Upload: nguyenbao
View: 216 times
Download: 4 times
Share this document with a friend
13
HTR2008-58317 MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS FOR ADVANCED GAS REACTOR SYSTEMS Richard R. Schultz Idaho National Laboratory P.O. Box 1625 2525 Fremont Idaho Falls, Idaho, USA (208) 526-9508; [email protected] ABSTRACT Simulation of some fluid phenomena associated with Generation IV reactors requires the capability of modeling mixing in two- or three-dimensional flow. At the same time, the flow condition of interest is often transient and depends upon boundary conditions dictated by the system behavior as a whole. Computational fluid dynamics (CFD) is an ideal tool for simulating mixing and three-dimensional flow in system components, whereas a system analysis tool is ideal for modeling the entire system. This paper presents the reasoning which has led to coupled CFD and systems analysis code software to analyze the behavior of advanced reactor fluid system behavior. In addition, the kinds of scenarios where this capability is important are identified. The important role of a coupled CFD/systems analysis code tool in the overall calculation scheme for a Very High Temperature Reactor is described. The manner in which coupled systems analysis and CFD codes will be used to evaluate the mixing behavior in a plenum for transient boundary conditions is described. The calculation methodology forms the basis for future coupled calculations that will examine the behavior of such systems at a spectrum of conditions, including transient accident conditions, that define the operational and accident envelope of the subject system. The methodology and analysis techniques demonstrated herein are a key technology that in part forms the backbone of the advanced techniques employed in the evaluation of advanced designs and their operational characteristics for the Generation IV advanced reactor systems. INTRODUCTION This paper is a description of the process and some of the thermal-hydraulic tools that are being readied for the evaluation of plant behavior that will be undertaken for a Generation IV Very High Temperature Gas-Cooled Reactor (VHTR). The process is similar in some respects to that followed to prepare the thermal-hydraulic tools for performing calculations for the Generation III+ advanced systems, e.g., the Westinghouse AP600 (Schultz, et al., 1997). The process, as it will be applied to the Next Generation Nuclear Plant (NGNP) variant of the VHTR, is described in detail in the NGNP Methods Technical Program Plan (Schultz, et al., 2007) However, significant differences and improvements stem from the use of single-phase fluids in the VHTR that not only allow, but also dictate, the use of computational fluid dynamics (CFD) modeling. Furthermore, an important new dimension of the tools to be used on the VHTR are coupled thermal-hydraulic software, that is, thermal-hydraulics and neutronics coupling and equally importantly, systems analysis codes 1 such as 1 In such a coupling, systems analysis software is used to perform calculations of the overall system behavior considering the interactions between all the parts, e.g., the core, the plena, the hot exit duct, the turbine, and the remainder of the plant. CFD codes are used to calculate the detailed three- dimensional fluid behavior in a region of the reactor such as a plenum. Proceedings of the 4th International Topical Meeting on High Temperature Reactor Technology HTR2008 September 28-October 1, 2008, Washington, DC USA Copyright © 2008 by ASME 1
Transcript
Page 1: Meeting the Thermal-Hydraulic Analysis Needs for … MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS FOR ADVANCED GAS REACTOR SYSTEMS Richard R. Schultz Idaho National Laboratory P.O.

HTR2008-58317

MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS FOR

ADVANCED GAS REACTOR SYSTEMS

Richard R. SchultzIdaho National Laboratory

P.O. Box 16252525 Fremont

Idaho Falls, Idaho, USA(208) 526-9508; [email protected]

Proceedings of the 4th International Topical Meeting on High Temperature Reactor Technology HTR2008

September 28-October 1, 2008, Washington, DC USA

ABSTRACT

Simulation of some fluid phenomena associated withGeneration IV reactors requires the capability of modelingmixing in two- or three-dimensional flow. At the same time, theflow condition of interest is often transient and depends uponboundary conditions dictated by the system behavior as awhole.

Computational fluid dynamics (CFD) is an ideal toolfor simulating mixing and three-dimensional flow in systemcomponents, whereas a system analysis tool is ideal formodeling the entire system. This paper presents the reasoningwhich has led to coupled CFD and systems analysis codesoftware to analyze the behavior of advanced reactor fluidsystem behavior. In addition, the kinds of scenarios where thiscapability is important are identified. The important role of acoupled CFD/systems analysis code tool in the overallcalculation scheme for a Very High Temperature Reactor isdescribed.

The manner in which coupled systems analysis andCFD codes will be used to evaluate the mixing behavior in aplenum for transient boundary conditions is described. Thecalculation methodology forms the basis for future coupledcalculations that will examine the behavior of such systems at aspectrum of conditions, including transient accident conditions,that define the operational and accident envelope of the subjectsystem. The methodology and analysis techniquesdemonstrated herein are a key technology that in part forms the

1

backbone of the advanced techniques employed in theevaluation of advanced designs and their operationalcharacteristics for the Generation IV advanced reactor systems.

INTRODUCTION

This paper is a description of the process and some ofthe thermal-hydraulic tools that are being readied for theevaluation of plant behavior that will be undertaken for aGeneration IV Very High Temperature Gas-Cooled Reactor(VHTR). The process is similar in some respects to thatfollowed to prepare the thermal-hydraulic tools for performingcalculations for the Generation III+ advanced systems, e.g., theWestinghouse AP600 (Schultz, et al., 1997). The process, as itwill be applied to the Next Generation Nuclear Plant (NGNP)variant of the VHTR, is described in detail in the NGNPMethods Technical Program Plan (Schultz, et al., 2007)However, significant differences and improvements stem fromthe use of single-phase fluids in the VHTR that not only allow,but also dictate, the use of computational fluid dynamics (CFD)modeling. Furthermore, an important new dimension of thetools to be used on the VHTR are coupled thermal-hydraulicsoftware, that is, thermal-hydraulics and neutronics couplingand equally importantly, systems analysis codes1 such as

1 In such a coupling, systems analysis software is used to performcalculations of the overall system behavior considering the interactionsbetween all the parts, e.g., the core, the plena, the hot exit duct, the turbine, andthe remainder of the plant. CFD codes are used to calculate the detailed three-dimensional fluid behavior in a region of the reactor such as a plenum.

Copyright © 2008 by ASME

Page 2: Meeting the Thermal-Hydraulic Analysis Needs for … MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS FOR ADVANCED GAS REACTOR SYSTEMS Richard R. Schultz Idaho National Laboratory P.O.

RELAP5-3D©2 coupled to CFD codes such as FLUENT orSTAR-CCM+.

Evaluations of fluid behavior in the VHTR, at normaloperational conditions and during abnormal or accidentconditions, are key ingredients in the progression fromspecification of a system, to design of the system, to building ofthe system, and finally to licensing of the system. Becausenuclear reactors, by their nature, consist of nuclear fuel (whichmust be maintained within a safe operational envelope) coupledto the fluid behavior via heat transfer and neutronic interactions,the evaluations of fluid behavior are sometimes complex andhave many facets. To reduce the calculational envelope to amanageable level, various methodologies are used to identifynot only the most important scenarios for consideration, butalso the most important phenomena which must be calculatedwith high resolution and fidelity. Presently, the candidatereactor systems (pebble-bed and prismatic systems) underconsideration for the VHTR use high-temperature helium as theworking fluid. Hence the working fluid remains single-phaseduring during all scenarios of interest. The overall scenario andphenomena identification methodology for the VHTR isillustrated in Figure 1.

Activity 1, the selection of the scenarios andphenomena for analysis, define the kinds of software andanalysis tools, since the important phenomena combined withthe reactor geometry define whether a one-dimensional or amulti-dimensional analysis is required. The capability of thethermal-hydraulic tools requires models that are based on first-principles.

Once the scenarios and phenomena are identified, keyelements of the above process are Activities 2, 6, and 7 sincethese activities ensure the software are validated and shown tobe capable of calculating the important scenarios andphenomena. Activities 2 and 6 usually include comparison ofthe desired calculation to data and additional development ofthe analytical algorithms if the software are demonstrated to beincapable of calculating key phenomena/behavior. Activity 7 isthe ultimate objective of the effort. The remaining activitiesprovide input from sources that may assist in the effort byproviding expert review and collaborations to achieve thedesired objectives.

CALCULATIONAL PROCESS

Activity 7 is accomplished by a series of calculationsthat resolve into extensive calculational work in selected areas.The calculational process is shown in Figure 2 and issubdivided into seven steps as summarized in paragraphs a

2 See Schultz, et al., 2007 for references and further information onsoftware.

22

through g below. Interactions between thermal-hydraulic toolsand other tools such as reactor physics and fuel behavior toolsarise in Step c and are important for the remainder of theprocess (Steps d through g). Figure 3 identifies the softwarecurrently associated with each of the steps in Figure 2 for apebble-bed reactor system. It is noted that a systems analysiscode such as RELAP5-3D© and a CFD code such as STAR-CCM+ play a central role in the process—see Figure 3.Accommodations are made for using other tools if specificneeds arise.

a. Material cross section compilation and evaluation.Nuclear interaction probabilities (cross sections) arefundamental to calculating high-fidelity neutronicscalculations. Microscopic cross sections are available on aper atom basis; however, the actual material densities,atomic compositions, and geometry must be used to obtainmacroscopic cross sections data sets in order to calculateneutron interaction rates on a per centimeter basis for thefuel, reactor core and structural materials, as a function oftemperature.

b. Preparation of homogenized cross-sections. The cross-section data are processed into a case-specific form usinglocal cell and assembly modeling codes. The basicphysical data are processed for case-specific resonanceshielding and then weighted with characteristic energy andspatial flux profiles generated from unit cell or super-cellmodels. This step is performed using software thatapproximates the neutron transport equation for the energyflux calculation and a one- or two-dimensional transportcode for the spatial flux. The geometric aspects of thisprocess are significantly different in the prismatic andpebble-bed concepts.

c. Whole-core analysis (diffusion or transport), detailedheating calculations, and safety parameter determination.Nodal diffusion-theory codes, such as PEBBED (PEBBEDis designed specifically for pebble-bed reactor simulation)are used to perform VHTR reactor core analysis. Steady-state eigenvalues, energy and spatial flux profiles, reactionrates, reactivity changes (burnup and control rodmovement), etc., will be calculated with the nodaldiffusion-theory codes. All of these software packages willbe verified against alternate computational models,especially models based on the well known MCNPstochastic simulation (Monte Carlo) code as shown inFigure 3, and various deterministic approaches. Spatialchanges in flux and power level as functions of time duringpostulated transients, predicted by the kinetics module, willprovide the energy source term required for the overallthermal-hydraulics systems code computations at each timestep during each transient. This process permits fullcoupling of thermal and neutronics computations,consistent with modern practice for nuclear systemsanalysis. A time-dependent implementation of thePEBBED code will be used for the pebble-bed concept.

Copyright © 2008 by ASME

Page 3: Meeting the Thermal-Hydraulic Analysis Needs for … MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS FOR ADVANCED GAS REACTOR SYSTEMS Richard R. Schultz Idaho National Laboratory P.O.

d. Thermal-hydraulic and thermal-mechanical evaluationsof system behavior. The fluid behavior, and interactionswith the neutronics, will be calculated using a systemsanalysis code, and a coupled systems analysis/computational fluid dynamics (CFD) code when necessary.Examples of a systems analysis code and a CFD code areRELAP5-3D© and FLUENT. In such a coupling, systemsanalysis software may be used to perform calculations ofthe overall system behavior considering the interactionsbetween all the parts, e.g., the core, the plenums, the hotexit duct, the turbine, and the remainder of the plant. CFDcodes, such as STAR-CCM+, are used to calculate thedetailed three-dimensional fluid behavior in a region of thereactor such as a plenum. In addition to analyzing the fluidbehavior under a spectrum of operating and accidentconditions, the thermal-hydraulic tools also will be used toinvestigate the significance of material geometric tolerancevariations due to manufacturing, thermal responses, andirradiation effects such as graphite swelling. The need toexamine factors that affect thermal-mechanical influence onfluid and heat transfer behavior will be included in the toolselection and evaluation process.

e. Models for balance of plant electrical generation systemand hydrogen production plant. The behavior of thebalance-of-plant systems will be modeled using a systemsanalysis code such as RELAP5-3D©. The balance-of-plantmodels are important to include in the analysis process toaccount for the important interactions that affect the systemefficiency during normal operational conditions, but also toaccount for the equipment interactions that may lead toundesirable conditions such as turbine over-speed, loss ofnet positive suction head for auxiliary systems, oroscillatory conditions that may lead to equipment damage.Interactions between the reactor system and its balance-of-plant components lead to boundary conditions that willdetermine whether fuel-damaging conditions are likely (seeitem f).

f. Fuel behavior and fission product release. Theperformance of fuel particles under irradiation is modeledto determine whether fuel failure will occur, with thesubsequent release of fission products, and whethersubsequent migration of fission products throughout thesystem must be considered. The INL software designed toperform this function is called PARFUME.

g. Fission product transport. If a loss-of-coolant accidenthas occurred, such that the fission products may migrate orbe impelled into the confinement/containment buildingwith perhaps subsequent release to the environment, thenthe final calculational step is the prediction of the fissionproduct movement into the environment and itsenvironmental distribution. The software tool most likelyto be used to perform these calculations is MELCOR.

The process described in items “a” through “g” is shownin the flow chart of Figure 2. The complete calculation process

33

illustrated in Figure 2 is only exercised in its entirety for a fewscenarios. Most scenarios would require the use of only afraction of the calculations represented in Stages a through e.For example, scenarios that do not include a loss of coolant,i.e., a pipe break, usually would not require calculation offission gas transport (Stage g). In addition, if the neutronicshave been thoroughly calculated for the reactor systemoperating condition (Stages a through c), then a multitude ofreactor system calculations can be performed using theevaluated reactor power state at time zero, and hence the Stagea through c calculations may only need to be performed oncefor a desired operating condition. Thereafter, for such scenariosthat assume reactor scram, a multitude of calculations can beperformed using only the software tools developed for Stages dand e. Coupled software, that is, systems analysis codes toneutronic codes and systems analysis codes to CFD codes areneeded for Stages c through g.

KEY PHENOMENA REQUIRING ANALYSIS AND NEEDFOR COUPLED SOFTWARE

To begin the process of defining the fluid behaviorscenarios that will require analysis and also to identify thesoftware that require validation, a preliminary evaluation of thephenomena requiring evaluation has been compiled and is listedin Table 1. The listed phenomena, identified during aphenomena identification and ranking table exercise sponsoredby the U.S. Nuclear Regulatory Commission (Ball, et al., 2007)stem from both normal operational conditions as well as theclassic depressurized conduction cooldown (DCC) andpressurized conduction cooldown (PCC) scenarios. Thefollowing phenomena have been determined to be important:neutronics behavior, core hot channel characterization, bypassanalysis, mixing, laminar-turbulent transition flow and forced-natural mixed convection flow, convective and radiation heattransfer in the reactor cavity cooling system (RCCS), air-wateringress, and fission product transport. The thermal- hydraulicphenomena of interest are described below:

i. Core hot channel characterization. The characteristics ofthe hottest cooling channels at operational conditions areconsidered a key calculational need since the hot channeltemperature distribution defines the hottest initial condition forthe fuel and surrounding materials. Hence preliminarycomputational fluid dynamics (CFD) studies have been initiatedand validation data are sought.

ii. Bypass. The bypass flow passes through the reflectorregions in both pebble-bed and block reactors and, in a block-type reactor, between the blocks. Because the quantity ofbypass flow is a direct function of the bypass area, which in turnis a function of the temperature distribution, fluence, andgraphite properties, the influence of the bypass on the coretemperature distribution may be significant. The influence of

Copyright © 2008 by ASME

Page 4: Meeting the Thermal-Hydraulic Analysis Needs for … MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS FOR ADVANCED GAS REACTOR SYSTEMS Richard R. Schultz Idaho National Laboratory P.O.

bypass may be assessed in part by performing a series ofparametric calculations that differ in the geometric boundaryconditions—as defined by the various factors that influence thebypass flow passages such as manufacturing tolerances,misalignments, and geometric distortions.

iii. Mixing. Mixing refers to the degree to which coolant ofdiffering temperatures entering a region mixes to produce auniform temperature. Mixing is a three-dimensionalphenomenon in the inlet and outlet plenums and a function of anumber of variables. Thus, for example, for a prismatic designin the inlet plenum, where it is identified as important in thePCC scenario, mixing occurs during natural convection ashelium moves upward through the hottest portion of the corewhile cooler helium moves downward through the bypass andthe cooler regions of the core. In the outlet plenum, mixingoccurs between the bottom of the core and the turbine orimmediate heat exchanger inlet during normal operation. Apreliminary calculation of the temperature variation in the lowerplenum indicates that gas temperature variations could exceed300 C. Although the specification for temperature variation atthe immediate heat exchanger or turbine inlet has not been set,it is thought that the helium temperature variation must be lessthan 20 C. Also, it has been seen that helium has a surprisingresistance to thorough mixing [Ball 2004, based on experienceof Kunitoni, et al., 1986] and that the temperature in the coreoutlet jet can vary over a considerable range, particularly sincethe bypass flow may vary between 10% and 25%. Therefore, itis likely that special design features will be required to ensuregood mixing and minimal thermal streaking from the lowerplenum to the turbine inlet.

iv. Laminar-Turbulent Transition Flow and. Forced-NaturalMixed Convection Flow. During the PCC scenario in the coreregion and during both the PCC and DCC scenarios in thereactor cavity cooling system (RCCS), there is the potential forhaving convective cooling in the transition region. Because theconvective cooling contribution is an important ingredient indescribing the total heat transfer from the core and thus theultimate peak core and vessel temperatures, these heat transferphenomena are potentially important.

v. Air and Water Ingress. For loss-of-coolant scenarios, suchas the DCC, there is the potential for air and water ingress intothe core in perhaps harmful quantities—depending on thescenario assumptions. Air may be present in the reactor cavity(some designs have a cavity filled with inert gas) and may enterthe core by diffusion in a DCC accident. Water is normallypresent in the air in the form of humidity, but it may enter thecore in much greater quantities, with much greater potentialeffect on reactivity, if the shutdown cooling system suffers apipe leak or break. Oxidation of graphite in the prismatic coredesign is also a potential safety issue.

vi. RCCS. Analyses of the natural circulation and radiationheat transfer that will occur in the reactor cavity are crucial to

44

determine the peak temperatures of the structural members andthe fuel in particular. It is envisioned that the mixing in thecavity will be done using a CFD code such as FLUENT whilethe boundary conditions to the CFD code will be provided by asystems analysis code such as RELAP5-3D.

A common thread that connects items i through vi is theneed to couple one-dimensional analyses that provide boundaryconditions to multi-dimensional calculations for scenarios thatrequire evaluation as a function of time. Hence results ofanalyses performed for items i and ii lead to boundaryconditions for item iii. Also, a mixture of one-dimensional andmulti-dimensional analysis requirements are needed to satisfythe calculational needs for items iv through vi.

CFD VERSUS SYSTEMS ANALYSIS CODES

Computational Fluid Dynamics (CFD) codes, such asSTAR-CCM+, are commonly used to analyze the flow behaviorin regions of a system where complex flow patterns areexpected or present. Therefore, the CFD codes are usually usedto analyze either two-dimensional or three-dimensional flowbehavior. The great appeal of the CFD codes is their relianceon first principles to describe the fluid behavior and theircapability to calculate the behavior of many complex flowpatterns. On the other hand, the CFD codes also rely on a finemesh discretization to model the region of interest;consequently, even with modern fast computers, the region of asystem that can be modeled is generally limited as defined bypractical computing times. Thus, CFD codes are rarely used tomodel the behavior of an entire system and instead are focusedon the behavior of a region of a system or component.Although today’s CFD codes are well suited to analyze a wide range of single-phase problems that do not undergo phasechanges, their range of applicability to two-phase or multi-phaseproblems is limited.

Although CFD software is rarely used to calculatedsystem-wide behavior, there are experts who advocate thedevelopment of coarse-grain CFD meshes designed to capturethe key phenomena (Class, et al., 2008). The advantages of thisapproach rest with the ability to perform system-widecalculations using a consistent set of field equations throughoutthe calculation. However, the approach for defining and usingcoarse-grain CFD (Hierarchical multi-scale CFD) is a leadingRandD area and a working methodology has not been defined todate.

Systems analysis codes, such as RELAP5-3D©, aregenerally aimed at modeling the behavior of an entire systemsuch as a high temperature gas-cooled reactor—including thebalance-of-plant. While such codes generally have thecapability to model multi-dimensional effects, their capacity toproduce widely accepted analyses of multi-dimensionalbehavior is limited by the assumptions and capabilities that stem

Copyright © 2008 by ASME

Page 5: Meeting the Thermal-Hydraulic Analysis Needs for … MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS FOR ADVANCED GAS REACTOR SYSTEMS Richard R. Schultz Idaho National Laboratory P.O.

from their field equation formulations, for example, the viscousstress terms are missing from their field equation formulations.Historically RELAP5-3D© was developed first to analyze thebehavior of two-phase systems that could be modeled in one-dimension. Because of the need to analyze two-phase flow, theassumptions used to define the field equations resulted in asimplification of the viscous stress terms and the use of manyempirical relationships that cannot be traced to first-principles,e.g., flow regime transitions and the models describing theinteractions between phases. The RELAP5-3D© field equationset was later extended to analyze two- and three-dimensions.However, the assumptions inherent to the one-dimensionalequation set were retained.

The starting point and the needs that led to thedevelopment of codes such as STAR-CCM+ and RELAP5-3D©,not surprisingly, led to different products with differentcapabilities, limitations, strengths, and weaknesses. Thissubject was addressed in Schultz 2001. The recent coupling ofFLUENT and RELAP5-3D© was executed to take advantage ofthe strengths of each. For example, the systems analysis codecan be used to model the balance of a system while the CFDcode can be used to model a portion of the same system in greatdetail. When the two codes are coupled, then the systemsanalysis code will provide the boundary conditions to the CFDcode so that a transient can be modeled with some confidence.Thus interactions between the balance-of-system and thedetailed CFD model of a portion of the system can besimulated. In summary, the fundamental strengths andweaknesses of the FLUENT and RELAP5-3D© codes, from ananalysis perspective, are given in Table 2. The CFD codes arewithout peer when analyzing the complex flow behavior ofsingle-phase systems in two- or three-dimensions, for eithersteady-state or transient behavior. The systems analysis codes,such as RELAP5-3D©, are without peer for analysis of two-phase systems in one-, two-, or three-dimensions. However, asusual, there are exceptions to these statements, e.g., systemsanalysis codes cannot analyze the behavior of stratified flowsystems such as warm water over cold water with a gas abovethe free surface. While CFD codes can analyze this behavior,commercial CFD codes cannot analyze the behavior of a vaporthat can condense on the free surface, such as steam over water.Indeed, commercial CFD codes do not even have the steamtables included in their source coding.

Thus, today’s CFD codes are tools capable ofanalyzing selected two-phase applications. For example,FLUENT has been demonstrated to model applicationsinvolving film boiling, aerosol deposition in a condenser,nucleate boiling and subcooled nucleate boiling. Systemsanalysis codes, such as RELAP5 on the other hand, are toolsthat can be used to analyze the two-phase phenomena andconditions that will be encountered by the equipment they weredesigned to analyze.

55

COUPLED CFD AND SYSTEMS ANALYSIS CODES

FLUENT and RELAP5-3D© were linked using anExecutive Program (Weaver, et al., 2002) that (a) monitors thecalculational progression in each code, (b) determines wheneach code has converged, (c) governs the informationinterchanges between the codes, and (d) issues permission toallow each code to progress to the next time step. TheExecutive Program was interfaced with FLUENT and RELAP5-3D© using user-defined functions. User-defined functions werealso used to ensure the fluid properties used by FLUENT andRELAP5-3D© are equivalent.

The Executive Program uses the Oak Ridge NationalLaboratory Parallel Virtual Machine (PVM) computer softwareprogram to control the interactions, data and message passingbetween the Fluent and RELAP5-3D© codes which are runningindependently. The PVM program execution serves as a "trafficcop" between the codes and gets data from one code at thecurrent time step and passes it to the other code so that theNGNP analysis can be done consistently in parallel.

The FLUENT/RELAP5-3D coupled software hasbeen validated and verified by modeling a portion of a simplesystem using FLUENT while the balance of the system wasmodeled using RELAP5-3D. The system is shown in Figure4—and a blowup of the portion modeled using FLUENT isshown in Figure 5.

The integrity of the coupling was validated byinspecting the boundary conditions for both the RELAP5-3Dmodel and the FLUENT at the boundaries (labeled zones 2 and3 in Figures 4 and 5) to establish that the pressures and fluidflow conditions were correct.

ONGOING ANALYSES AND OBSERVATIONS

Since the validation work described in the paragraphsabove, the practices and procedures for using the coupled toolshave been studied and expanded. In a recent paper theFLUENT calculational envelope was studied to determine therange of applicability of the FLUENT segregated solver3

(Schowalter, et al., 2004). And for the first time the coupledFLUENT/RELAP5-3D© software are being used to analyze thebehavior of the flow in the lower plenum of an advanced gas-cooled reactor in conjunction with changing boundaryconditions in the remainder of the system.

3 FLUENT may be used with coupled or segregated solvers. The coupledsolver is used with higher Mach number flow problems where changes in thefluid properties are important to integrate with the velocity field calculation.The segregated solver is used for lower Mach number flows, and especially forincompressible flows.

Copyright © 2008 by ASME

Page 6: Meeting the Thermal-Hydraulic Analysis Needs for … MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS FOR ADVANCED GAS REACTOR SYSTEMS Richard R. Schultz Idaho National Laboratory P.O.

The RELAP5-3D model of the reactor vessel itself isillustrated in Figures 6 and 7 (INL model—figures courtesy ofKorea Atomic Energy Research Institute). The FLUENTmodel (courtesy of FLUENT), shown in Figure 8, replacesComponents 160 and 170 of the RELAP5-3D© model.

A clear need to have a coupled CFD and systems analysistool has been identified. The tool exists and development iscontinuing to accommodate the needs specific to the VHTR.Presently the calculational envelope of the coupledCFD/systems analysis tool is being defined and documented.

REFERENCES

A. G. Class, et al.,“Hierarchical Multi-Scale ThermalHydraulics in Nuclear Applications,” Proceedings of theInternational Workshop on Thermal-Hydraulics of InnovativeReactor and Transmutation Systems - THIRSApril 14-16, 2008, Forschungszentrum Karlsruhe, Germany

S. J. Ball, M.. Corradini, S. E. Fisher, R. Gauntt, G.Geffraye, J. C. Gehin, Y. Hassan, D. L.. Moses, J. P. Renier, R.R. Schultz, and T. Wei, Next-Generation Nuclear Plant (NGNP)Phenomena Identification and Ranking Table (PIRT) forAccident and Thermal Fluids Analysis, NUREG/CR-6944,September, 2007

Schowalter, D.G., N. Basu, A. Walavalkar, and R. R.Schultz, “Discussion on the Calculational Envelope of the FLUENT Computational Fluid Dynamics Code and theRELAP5 Systems Analysis Code when Using Segreagated

66

Solvers,” Proceedings of the American Nuclear Society WinterMeeting, November, 2004.

Schultz, R. R., C. M. Kullberg, G. E. McCReery, R. A.Shaw, B. Hanson, N. Newman, C. P. Liou, J. L. Westacott,RELAP5/MOD3 Code Assessment Analyses Based on theROSA-AP600 Program: Small Break LOCAs and the StationBlackout Transient, March, 1997.

Schultz, R. R., R. A. Riemke, C. B. Davis, and G.Nurnburg, “Comparison: RELAP5-3D© Systems Analysis Codeand FLUENT CFD Code Momentum Equation Formulations,” Proceedings of the ICONE-11, Tokyo, Japan, April, 2003.

Schultz, R. R., A. M. Ougouag, D. W. Nigg, H. D. Gougar,R. W. Johnson, W. K. Terry, C. H. Oh, D. M. McEligot, G. W.Johnsen, G. E. McCreery, W. Y. Yoon, J. W. Sterbentz, J. S.Herring, T. A. Taiwo, T. Y. C. Wei, W. D. Pointer, W. S. Yang,M. T. Farmer, H. S. Khalil, M. A. Feltus, Next GenerationNuclear Plant Methods Technical Program Plan, INL/EXT-06-11804, January, 2007.

Schultz, R. R., A. M. Ougouag, D. W. Nigg, H. D. Gougar,R. W. Johnson, W. K. Terry, C. H. Oh, D. M. McEligot, G. W.Johnsen, G. E. McCreery, W. Y. Yoon, J. W. Sterbentz, J. S.Herring, T. A. Taiwo, T. Y. C. Wei, W. D. Pointer, W. S. Yang,M. T. Farmer, H. S. Khalil, M. A. Feltus, Next GenerationNuclear Plant Methods Technical Program Plan, INL/EXT-06-11804, Revision 1, August, 2008 (to be published).

Weaver, W.L., E. T. Tomlinson, and D. L. Aumiller, 2002,“A Generic Semi-Implicit Coupling methodology for Use inRELAP5-3D©,” Nuclear Engineering and Design, 211, pages13 to 26.

Copyright © 2008 by ASME

Page 7: Meeting the Thermal-Hydraulic Analysis Needs for … MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS FOR ADVANCED GAS REACTOR SYSTEMS Richard R. Schultz Idaho National Laboratory P.O.

1. VHTR Project Scenario Selection & Phenomena Identification: PhenomenaIdentification & Ranking Table (PIRT) process used to select the scenarios and to identifythe phenomena of importance.

2. VHTR ProjectSoftwareValidation:Analysis tools areevaluated todetermine whetherimportantphenomena can becalculated.

3. Validation &Development byComm unity:Validationperformed byanalysis communityvia internationalstandard problems.

4. Collaborations with GIF -Partners:Use I -NERIs as medium for internationalrelationships and collaboration projects tovalidate & develop software.

5. Collaborations with UniversitiesUse NERIs as vehicle for R&Drelationships with universities to focus onpertinent VHTR R&D issues (validation &development).

6. Developm ent coordinated by VHTR Project: Ifimportant phenomena cannot be calculated by analysistools, then further development is undertaken.

7. Analysis: The operational and accident scenarios that require study are analyzed.

8.P

eer

revi

ew:

Nuc

lear

com

mun

itype

erre

view

ofm

etho

dsR

&D

proc

ess

Figure 1. Methods RandD process—(see Schultz, et al., 2007)

7 Copyright © 2008 by ASME7

Page 8: Meeting the Thermal-Hydraulic Analysis Needs for … MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS FOR ADVANCED GAS REACTOR SYSTEMS Richard R. Schultz Idaho National Laboratory P.O.

a. Material CrossSectionCompilation andEvaluation

b. Preparation ofHomogenized CrossSections

c. Whole-Core Analysis(Diffusion orTransport), DetailedHeating Calculation,and Safety ParameterDetermination

d. Thermal-Hydraulic andThermal-MechanicalEvaluation of SystemBehavior

f. Fuel Behavior: FissionGas Release Evaluation

g. Fission Gas Transport

e. Models for Balance ofPlant ElectricalGeneration System andHydrogen ProductionPlant

a. Material CrossSectionCompilation andEvaluation

b. Preparation ofHomogenized CrossSections

c. Whole-Core Analysis(Diffusion orTransport), DetailedHeating Calculation,and Safety ParameterDetermination

d. Thermal-Hydraulic andThermal-MechanicalEvaluation of SystemBehavior

f. Fuel Behavior: FissionGas Release Evaluation

g. Fission Gas Transport

e. Models for Balance ofPlant ElectricalGeneration System andHydrogen ProductionPlant

a. Material CrossSectionCompilation andEvaluation

b. Preparation ofHomogenized CrossSections

c. Whole-Core Analysis(Diffusion orTransport), DetailedHeating Calculation,and Safety ParameterDetermination

d. Thermal-Hydraulic andThermal-MechanicalEvaluation of SystemBehavior

f. Fuel Behavior: FissionGas Release Evaluation

g. Fission Gas Transport

e. Models for Balance ofPlant ElectricalGeneration System andHydrogen ProductionPlant

a. Material CrossSectionCompilation andEvaluation

b. Preparation ofHomogenized CrossSections

c. Whole-Core Analysis(Diffusion orTransport), DetailedHeating Calculation,and Safety ParameterDetermination

d. Thermal-Hydraulic andThermal-MechanicalEvaluation of SystemBehavior

f. Fuel Behavior and FissionProduct Release

g. Fission Product Transport

e. Models for Balance ofPlant ElectricalGeneration System andHydrogen ProductionPlant

Figure 2. Calculation process (see Schultz, et al., 2007)

8 Copyright © 2008 by ASME8

Page 9: Meeting the Thermal-Hydraulic Analysis Needs for … MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS FOR ADVANCED GAS REACTOR SYSTEMS Richard R. Schultz Idaho National Laboratory P.O.

Figure 3. Application of process to pebble-bed candidate designs forVHTR—with applicable software—see Schultz, et al., 2008

9 Copyright © 2008 by ASME9

Page 10: Meeting the Thermal-Hydraulic Analysis Needs for … MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS FOR ADVANCED GAS REACTOR SYSTEMS Richard R. Schultz Idaho National Laboratory P.O.

Table 1. Phenomena identified for analysis during for normal operation, PCC and DCCscenarios.

Scenario InletPlenum

Core RCCS OutletPlenum

Normaloperation

i. Neutronic behaviorii. Bypass flow

iii. Hot channel characteristics

Mixing

DCC i. Thermal radiation and conduction of heatacross the coreii. Axial heat conduction and radiationiii. Natural circulation in the reactorpressure vesseliv. Air and water ingressv. Potential fission product transport

i. Laminar-turbulenttransition flowii. Forced-natural mixedconvection flow

PCC Mixing i. Neutronic behaviorii. Bypassiii. Laminar-turbulent transition flowiv. Forced-natural mixed convection flowv. Hot channel characteristics at operationalconditions

i. Laminar-turbulenttransition flowii. Forced-natural mixedconvection flow

Mixing

Table 2 Comparison of FLUENT and RELAP5-3D© Capabilities

Single-Phase Two-Phase1-D 2- or 3-D 1-D 2- or 3-D

FLUENT Not used Preferred tool Not used Superior for specialized applications—but generallyunable to model phenomena behavior over widethermodynamic ranges and through phase transitions.Fluid properties must be input; FLUENT does not havesteam tables.

RELAP5-3D© Preferredtool

Inputassumptions are

required.

Preferredtool

Preferred tool for analyses of integral system behavior andapplications that require analyses over wide fluidthermodynamic state ranges and through phase transitions.

10 Copyright © 2008 by ASME10

Page 11: Meeting the Thermal-Hydraulic Analysis Needs for … MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS FOR ADVANCED GAS REACTOR SYSTEMS Richard R. Schultz Idaho National Laboratory P.O.

PIPE Component 1: lrcore

TMDPVOL Component 15: coretop

FLUENTmodel

Zone 2 ofFLUENT model

SNGLJUN Component 105:lcrout

TMDPVOL Component 6:corebtm

PIPE Component 16: upcore

Zone 3 ofFLUENTmodelSNGLJUN

Component 115:upcrin

TMDPVOL Component 210: contain

SNGLJUN Component 200: outlet

SNGLJUN Component 180:cortoup

SNGLJUNComponent 115:upcrin

SNGLVOLCompt 190:upperp

SNGLJUNComponent 910:bytoup

PIPE Component2: bypass

TMDPVOL Component 110:contain

SNGLVOLCompt 120:upperp

SNGLJUNCompt 100:inlet

SNGLJUN Component 130:cortolp

Figure 4. System model with FLUENT 3-D component

1111

FLUENTmodel

Zone 2 of FLUENTmodel

Zone 3 of FLUENTmodel

Figure 5. Blow-up of FLUENTcomponent in system model

Copyright © 2008 by ASME

Page 12: Meeting the Thermal-Hydraulic Analysis Needs for … MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS FOR ADVANCED GAS REACTOR SYSTEMS Richard R. Schultz Idaho National Laboratory P.O.

130(Riser

&Head)

140 (Upper plenum)

160 (Lower plenum)110(Inletann.)

120 (SCS & Lower head)

100(Inlet)

170(Outlet)

145

OuterReflecor

156

OuterCore

154

MiddleCore

152

InnerCore

142

InnerReflecor

Figure 6. RELAP5-3D© nodalization of a VHTR

InnerReflector

InnerBypass

3 Core

OuterBypass

OuterReflector

CoolantRiser

ReactorVessel

InnerReflector

InnerBypass

3 Core

OuterBypass

OuterReflector

CoolantRiser

ReactorVessel

Figure 7. Plan view of RELAP5-3D© VHTR nodalization showing heat transfer paths

12 Copyright © 2008 by ASME12

Page 13: Meeting the Thermal-Hydraulic Analysis Needs for … MEETING THE THERMAL-HYDRAULIC ANALYSIS NEEDS FOR ADVANCED GAS REACTOR SYSTEMS Richard R. Schultz Idaho National Laboratory P.O.

Figure 8. FLUENT model of lower plenum: illustrating turbulence intensity;FLUENT model represents Components 160 and 170 of RELAP5-3D© VHTRmodel—see Figure 6

13 Copyright © 2008 by ASME13


Recommended