Since 1990, the Fluids Engineering Division of ASME has pursued activities concerning the detection, estimation and control of numerical uncertainty and/or error in computational fluid dynamics (CFD) studies. The first quality-control measures in this area were issued in 1986 (1986, “Editorial Policy Statement on Control of Numerical Accuracy,” ASME J. Fluids Eng., 108, p. 2) and revised in 1993 (1993, “Journal of Fluids Engineering Editorial Policy Statement on the Control of Numerical Accuracy,” ASME J. Fluids Eng., 115, pp. 339–340). Given the continued increase in CFD related publications, and the many significant advancements in computational techniques and computer technology, it has become necessary to revisit the issue and formulate a more detailed policy to further improve the quality of publications in this area. This brief note provides specific guidelines for prospective authors for calculation and reporting of discretization error estimates in CFD simulations where experimental data may or may not be available for comparison. The underlying perspective is that CFD-related studies will eventually aim to predict the outcome of a physical event for which experimental data is not available. It should be emphasized that the requirements outlined in this note do not preclude those already published in the previous two policy statements. It is also important to keep in mind that the procedure recommended in this note cannot possibly encompass all possible scenarios or applications.

## Preliminaries

The *computer code* used for an application must be fully referenced, and previous code *verification studies* must be briefly described or cited. The word “verification” is used in this note in its broadest sense, meaning that the computer code is capable of solving a system of coupled differential or integral equations with a properly posed set of initial and/or boundary conditions correctly, and reproduces the exact solution to these equations when sufficiently fine grid resolution (both in time and space) is employed. The *formal order of accuracy* in time and space for each equation solved should be also stated clearly, with proper references where this information is accessible to the readers. Before any discretization error estimation is calculated, it must be shown that *iterative convergence* is achieved with at least three (preferably four) orders of magnitude decrease in the normalized residuals for each equation solved. (This commonly used criterion does not always ensure adequate convergence; see Appendix) For time-dependent problems, iterative convergence at every time step should be checked, and sample convergence trends should be documented for selected, critically important, variables. A possible method for assessment of iteration errors is outlined in the Appendix.

It should also be recognized that uncertainty in inlet flow boundary conditions could be a significant contributor to the overall uncertainty. Here we recommend that the degree of sensitivity of the presented solution to small perturbations in the inlet conditions be studied and reported.

The recommended method for discretization error estimation is the Richardson extrapolation (RE) method. Since its first elegant application by its originator (1,2), this method has been studied by many authors. Its intricacies, shortcomings, and generalization have been widely investigated. A short list of references given in the bibliography (3,4,5,6,7,8,9,10,11,12,15) is selected for the direct relevance of these references to the subject and for brevity. The limitations of the RE method are well known. The local RE values of the predicted variables may not exhibit a smooth monotonic dependence on grid resolution, and in a time-dependent calculation, this nonsmooth response will also be a function of time and space. Nonetheless, it is currently the most reliable method available for the prediction of numerical uncertainty. Prospective authors can find many examples in the above references. As new and more reliable methods emerge, the present policy statement will be reassessed and modified as needed.

The Grid Convergence Method (GCI) method (and is based on RE) described herein is an acceptable and a recommended method that has been evaluated over several hundred CFD cases (19,14,2,10,7). If authors choose to use it, the method per se will not be challenged in the paper review process. If authors choose to use another method, the adequacy of their method will be judged in the review process. This policy is not meant to discourage further development of new methods. in fact, JFE encourages the development and statistically significant evaluation of alternative methods of estimation of error and uncertainty. Rather, this policy is meant to facilitate CFD publication by providing practitioners with a method that is straightforward to apply, is fairly well justified and accepted, and will avoid possible review bottlenecks, especially when the CFD paper is an application paper rather than one concerned with new CFD methodology.

## Recommended Procedure for Estimation of Discretization Error

*Step 1.*Define a representative cell, mesh, or grid size $h$. For example, for three-dimensional calculations,

*Step 2.* Select three significantly different sets of grids and run simulations to determine the values of key variables important to the objective of the simulation study, for example, a variable $\varphi $ critical to the conclusions being reported. It is desirable that the grid refinement factor $r=hcoarse\u2215hfine$ be greater than 1.3. This value of 1.3 is based on experience and not on formal derivation. The grid refinement should, however, be done systematically, that is, the refinement itself should be structured even if the grid is unstructured. Use of geometrically similar cells is preferable.

*Step 3.* Let $h1<h2<h3$ and $r21=h2\u2215h1$, $r32=h3\u2215h2$, and calculate the apparent order $p$ of the method using the expression3

*Step 4.*Calculate the extrapolated values from

*Step 5.* Calculate and report the following error estimates, along with the apparent order $p$.

Table 1 illustrates this calculation procedure for three selected grids. The data used are taken from Ref. 4, where the turbulent two-dimensional flow over a backward facing step was simulated on nonuniform structured grids with total number of cells $N1$, $N2$, and $N3$. Hence, according to Table 1, the numerical uncertainty in the fine-grid solution for the reattachment length should be reported as 2.2%. Note that this does not account for modeling errors.

$\varphi =dimensionless$reattachment length(with monotonicconvergence) | $\varphi =axial$ velocity at$x\u2215H=8$, $y=0.0526$$(p<1)$ | $\varphi =axial$ velocity at$x\u2215H=8$, $y=0.0526$(with oscillatoryconvergence) | |

$N1$, $N2$, $N3$ | 18,000, 8000, 4500 | 18,000, 4500, 980 | 18,000, 4500, 980 |

$r21$ | 1.5 | 2.0 | 2.0 |

$r32$ | 1.333 | 2.143 | 2.143 |

$\varphi 1$ | 6.063 | 10.7880 | 6.0042 |

$\varphi 2$ | 5.972 | 10.7250 | 5.9624 |

$\varphi 3$ | 5.863 | 10.6050 | 6.0909 |

$p$ | 1.53 | 0.75 | 1.51 |

$\varphi ext21$ | 6.1685 | 10.8801 | 6.0269 |

$ea21$ | 1.5% | 0.6% | 0.7% |

$eext21$ | 1.7% | 0.9% | 0.4% |

$GCIfine21$ | 2.2% | 1.1% | 0.5% |

$\varphi =dimensionless$reattachment length(with monotonicconvergence) | $\varphi =axial$ velocity at$x\u2215H=8$, $y=0.0526$$(p<1)$ | $\varphi =axial$ velocity at$x\u2215H=8$, $y=0.0526$(with oscillatoryconvergence) | |

$N1$, $N2$, $N3$ | 18,000, 8000, 4500 | 18,000, 4500, 980 | 18,000, 4500, 980 |

$r21$ | 1.5 | 2.0 | 2.0 |

$r32$ | 1.333 | 2.143 | 2.143 |

$\varphi 1$ | 6.063 | 10.7880 | 6.0042 |

$\varphi 2$ | 5.972 | 10.7250 | 5.9624 |

$\varphi 3$ | 5.863 | 10.6050 | 6.0909 |

$p$ | 1.53 | 0.75 | 1.51 |

$\varphi ext21$ | 6.1685 | 10.8801 | 6.0269 |

$ea21$ | 1.5% | 0.6% | 0.7% |

$eext21$ | 1.7% | 0.9% | 0.4% |

$GCIfine21$ | 2.2% | 1.1% | 0.5% |

## Discretization Error Bars

When computed profiles of a certain variable are presented, it is recommended that numerical uncertainty be indicated by error bars on the profile, analogous to the experimental uncertainty. It is further recommended that this be done using the GCI in conjunction with an average value of $p=pave$ as a measure of the global order of accuracy. This is illustrated in Figs.1,2.

Figure 1 (data taken from Ref. 4) presents an axial velocity profile along the $y$-axis at an axial location of $x\u2215H=8.0$ for a *turbulent* two-dimensional backward-facing-step flow. The three sets of grids had 980, 4500, and 18000 cells, respectively. The local order of accuracy $p$ calculated from Eq. 3 ranges from 0.012 to 8.47, with a global average $pave$ of 1.49, which is a good indication of the hybrid method applied for that calculation. Oscillatory convergence occurs at 20% of the 22 points. This averaged apparent order of accuracy is used to assess the GCI index values in Eq. 7 for individual grids, which is plotted in the form of error bars, as shown in Fig. 1b. The maximum discretization uncertainty is 10%, which corresponds to $\xb10.35m\u2215s$.

Figure 2 (data taken from Ref. 16) presents an axial velocity profile along the $y$-axis at the station $x\u2215H=8.0$ for a *laminar* two-dimensional backward-facing-step flow. The Reynolds number based on step height is 230. The sets of grids used were $20\xd720$, $40\xd740$, and $80\xd780$, respectively. The local order of accuracy $p$ ranges from 0.1 to 3.7, with an average value of $pave=1.38$. In this figure, 80% out of 22 points exhibited oscillatory convergence. Discretization error bars are shown in Fig. 2b, along with the fine-grid solution. The maximum percentage discretization error was about 100%. This high value is relative to a velocity near zero and corresponds to a maximum uncertainty in velocity of about $\xb10.012m\u2215s$.

### Appendix: A Possible Method for Estimating Iteration Error

It is recommended that the iteration convergence error calculated as suggested above (or in some other rational way) should be at least one order of magnitude smaller than the discretization error estimates for each calculation (for alternative methods see, e.g., Refs. 20,21).

**Ismail B. Celik**

**Urmila Ghia**

**Patrick J. Roache**

**Christopher J. Freitas**

**Hugh Coleman**

**Peter E. Raad**