Exploring the Capabilities of an LLM from CFD Simulations of Turbulent Flow in a Manifold
Abstract
1. Introduction
2. LLMs and Prompt Engineering
3. Research Context and Computational Resources
4. Methodology
4.1. Asking the LLM for Information on Turbulent Flow Manifolds
4.2. Defining the Case Study
4.3. Running CFD Simulations
4.4. Predicting Results Using the LLM
5. Results Analysis
5.1. Asking the LLM for Information on Turbulent Flow in Manifolds
5.1.1. Flow from Each Nozzle (Orifice Equation)
- where:
5.1.2. Pressure Drops Along a Lateral (Darcy–Weisbach), for Each Lateral
5.1.3. Header Pressure Drops, Same Idea for the Main Header
5.1.4. Nozzle Spacing and Count
5.1.5. Lateral Diameter Sizing
5.1.6. Header Diameter Sizing
5.1.7. Uniformity Criterion
5.2. Running CFD Simulations
5.3. Predict Results Using the LLM

5.4. Verifying the Suggestions for Mesh and Solver Improvement
6. Conclusions and Future Work
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
Abbreviations
| CFD | Computational Fluid Dynamics |
| LLMs | Large Language Models |
| CAD | Computer-Aided Design |
| QwQ-32B | Qwen with Question/thought |
| GPT | Generative Pre-trained Transformer |
| RAG | Recovery augmented generation |
| NIROMs | Non-intrusive reduced-order models |
| WGAN | Wasserstein generative adversarial network |
| BiLSTM | Bidirectional long short-term memory |
| UAV | Unmanned Aerial Vehicle |
| RANS | Reynolds-Averaged Navier–Stokes |
| UUVs | Unmanned Underwater Vehicles |
| HVAC | Heating, ventilation, and air conditioning |
| LSTM | Long Short-Term Memory |
| ANNs | Artificial Neural Networks |
| TTX2T | Twin Turbocharged Cross-Dual Tubular |
| DOF | Degrees of freedom |
| RSM | Resistive Sorting Method |
| BBD | Box–Behnken Design |
| NSGA-II | Non-Dominated Sorting Genetic Algorithm II |
| API | Application Programming Interface |
| SARD | Software Assurance Reference Dataset |
| RMSE | Root Mean Square Error |
| R2 | R-squared, the coefficient of determination |
| BLEU | Bilingual Evaluation Understudy |
| ROUGE | Recall-Oriented Understudy for Gisting Evaluation |
| Qn | Flow per nozzle |
| Cd | Discharge coefficient |
| An | Nozzle area |
| Ph | Pressure in the lateral at the nozzle |
| r | Water density |
| ∆Pheader | Header pressure drops |
| QT | Total flow |
| N | Number of nozzles |
| Uniformity error | |
| D | Tube diameter |
| ΔP | Pressure drop |
| f | Friction factor |
| L | Pipe length |
| K | Loss coefficient |
| Qmax | Maximum nozzle flow |
| Qmin | Minimum nozzle flow |
| Qavg | Average flow |
| k | Thermal conductivity |
| Qh | Header flow rate |
Appendix A
Verbatim Prompts Used with ChatGPT












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| Variable | Magnitude |
|---|---|
| Vinlet | 0.955 m/s |
| Re | 924,534.55 (turbulent flow) |
| Tempwater | 80 °C |
| Tempwalls | 20 °C |
| Poutlets | Patm |
| Constant roughness | 0.00003 m |
| Manifold Material | Steel |
| Turbulence model | k-ω SST |
| Simulation | Inlet Vel (m/s) | Temp Walls (°C) | Temp Inlet (°C) | Outlet Vel 1 (m/s) | Outlet Vel 2 (m/s) | Outlet Vel 3 (m/s) | Outlet Vel 4 (m/s) | Outlet Vel 5 (m/s) | Outlet Vel 6 (m/s) |
| 1 | 0.955 | 20 | 80 | 1.25466 | 1.80999 | 1.22838 | 1.8053 | 1.34525 | 1.73497 |
| 2 | 1 | 19 | 80 | 1.35044 | 1.92338 | 1.32116 | 1.86866 | 1.42323 | 1.81078 |
| . | . | . | . | . | . | . | . | . | . |
| 22 | 1.75 | 17 | 83 | 2.30962 | 3.35957 | 2.29337 | 3.25306 | 2.52137 | 3.08176 |
| 23 | 1.8 | 23 | 87 | 2.37434 | 3.45639 | 2.36166 | 3.34216 | 2.59446 | 3.166 |
| Simulation | Outlet Vel 7 (m/s) | Outlet Vel 8 (m/s) | Outlet Vel 9 (m/s) | Outlet Vel 10 (m/s) | Outlet Vel 11 (m/s) | Outlet Vel 12 (m/s) | Outlet Temp 1 (°C) | Outlet Temp 2 (°C) | Outlet Temp 3 (°C) |
| 1 | 1.23728 | 1.79261 | 1.19051 | 1.88414 | 1.34173 | 1.79716 | 43.477 | 54.131 | 47.002 |
| 2 | 1.31546 | 1.86497 | 1.30703 | 1.86598 | 1.34956 | 1.91842 | 45.855 | 51.309 | 47.351 |
| . | . | . | . | . | . | . | . | . | . |
| 22 | 2.22773 | 3.29674 | 2.12367 | 3.52548 | 2.25611 | 3.44066 | 46.806 | 52.147 | 48.428 |
| 23 | 2.28121 | 3.39978 | 2.18247 | 3.61619 | 2.32226 | 3.54225 | 48.653 | 54.177 | 50.176 |
| Simulation | Outlet Temp 4 (°C) | Outlet Temp 5 (°C) | Outlet Temp 6 (°C) | Outlet Temp 7 (°C) | Outlet Temp 8 (°C) | Outlet Temp 9 (°C) | Outlet Temp 10 (°C) | Outlet Temp 11 (°C) | Outlet Temp 12 (°C) |
| 1 | 55.391 | 49.801 | 56.714 | 48.174 | 56.131 | 45.445 | 57.712 | 45.102 | 47.56 |
| 2 | 54.608 | 49.795 | 57.566 | 48.222 | 55.971 | 45.657 | 56.266 | 45.018 | 50.745 |
| . | . | . | . | . | . | . | . | . | . |
| 22 | 55.92 | 51.498 | 58.54 | 48.834 | 57.737 | 46.135 | 59.692 | 45.05 | 52.248 |
| 23 | 58.228 | 53.501 | 61.163 | 50.583 | 60.364 | 47.651 | 62.322 | 46.473 | 54.041 |
| Manifold Application | Uses |
|---|---|
| Physics | spacetime, general relativity |
| Robotics | configuration spaces |
| CFD/mechanics | curved surfaces, shells |
| Machine learning | data lies on a low-dimensional manifold |
| Differential equations | solution spaces |
| Classification | Function | Uses |
|---|---|---|
| By purpose | Hot water distribution (spray manifold) | Takes hot water from the condenser loop |
| Spreads it evenly over the fill media | ||
| Maximizes surface area for evaporation | ||
| Cold water collection manifolds | Collect cooled water from multiple outlets Feed it uniformly into the basin or the pump suction | |
| Make-up water manifolds | Add fresh water to replace evaporation + blowdown Distribute it gently to avoid disturbing the airflow or fill | |
| By function | Spray distribution manifolds | Main header + lateral pipes Nozzles or orifices along laterals |
| Collection manifolds | Combine the flow from multiple outlets Used in closed circuits or hybrid towers | |
| By geometry | Header–lateral manifold | Crossflow towers Counterflow towers |
| Ring (loop) manifold | Circular or rectangular loop Helps equalize pressure Very uniform flow | |
| Grid manifold | Network of pipes in X–Y pattern Very uniform distribution |
| Order | Recommendation | Suggested Action | Main Objective |
|---|---|---|---|
| 1 | Refine the overall mesh size. | Reduce the size of the base element compared to the current size (0.404 m) to increase the number of cells in the header, sides, and nozzles. | Capture velocity, pressure, and temperature gradients more accurately. |
| 2 | Apply local refinement to critical areas. | Incorporate body sizing or face sizing at the inlet, header-side junctions, and nozzle roots. | Improve the resolution of recirculation, minor losses, and sudden accelerations. |
| 3 | Increase the inflation layers. | Increase from 5 to 10–15 layers with a growth rate of approximately 1.2 | Adequately address the boundary layer and wall shear stresses. |
| 4 | Verify the y+ parameter. | Check that the values near the wall are suitable for the k-ω SST model (ideally y+ ≈ 1). | Ensure a more accurate prediction of friction and heat transfer. |
| 5 | Increase the number of iterations. | Running between 800 and 1500 iterations or until stable convergence is observed. | Reduce residuals and improve mass balance. |
| 6 | Monitor residuals and output variables. | Monitor continuity, momentum, energy, flow rates, and temperatures during the run. | Confirm actual numerical convergence of the solution. |
| 7 | Evaluate the mass balance error. | Compare the inlet flow with the sum of the 12 outlet flows | Verify overall consistency and mass conservation. |
| 8 | Perform a mesh independence study | Compare results between the current, medium, and fine meshes. | (e.g., final mesh size, number of elements, final mass balance error, and residual values after refinement). |
| Structure | Description |
|---|---|
| File Size | Total Rows: 24 |
| Total Columns: 28 | |
| Total Rows: 24 | |
| Row Structure | Row 1: Units of the variables. Rows 2–24: Experimental data or simulations (23 records named Data 1, Data 2, …). |
| Summary of input/control variables | Inlet velocity (m/s) Temp_walls (°C) Temp_Inlet (°C) |
| Summary of output variables | 12 outlet velocities 12 outlet temperatures |
| Total variables: | 3 input variables 24 output variables |
| Inlet velocity ranges | 0.955–2.0 m/s |
| Outlet temperature ranges | 47.6–54.6 °C |
| High-flow outlets | Outlets 2, 4, 8, 10, and 12 Velocity ≈ 2.7–2.9 m/s |
| Low-flow outlets | Outlets 1, 3, 7, 9, and 11 Velocity ≈ 1.8–1.9 m/s |
| Predicted Values | CFD Simulation Values | |||
|---|---|---|---|---|
| Outlet | Vel (m/s) | Temp (°C) | Vel (m/s) | Temp (°C) |
| 1 | 2.332 | 47.12 | 2.30962 | 46.806 |
| 2 | 3.326 | 52.31 | 3.35957 | 52.147 |
| 3 | 2.305 | 48.77 | 2.29337 | 48.428 |
| 4 | 3.238 | 56.08 | 3.25306 | 55.92 |
| 5 | 2.5 | 51.36 | 2.52137 | 51.498 |
| 6 | 3.07 | 58.46 | 3.08176 | 58.54 |
| 7 | 2.213 | 49.05 | 2.22773 | 48.834 |
| 8 | 3.281 | 57.71 | 3.29674 | 57.737 |
| 9 | 2.108 | 46.42 | 2.12367 | 46.135 |
| 10 | 3.46 | 59.88 | 3.52548 | 59.692 |
| 11 | 2.281 | 45.92 | 2.25611 | 45.05 |
| 12 | 3.397 | 52.55 | 3.44066 | 52.248 |
| Predicted Values | CFD Simulation Values | |||
|---|---|---|---|---|
| Outlet | Vel (m/s) | Temp (°C) | Vel (m/s) | Temp (°C) |
| 1 | 2.395 | 48.21 | 2.37434 | 48.653 |
| 2 | 3.42 | 53.64 | 3.45639 | 54.177 |
| 3 | 2.366 | 49.88 | 2.36166 | 50.176 |
| 4 | 3.329 | 57.32 | 3.34216 | 58.228 |
| 5 | 2.571 | 52.63 | 2.59446 | 53.501 |
| 6 | 3.161 | 59.84 | 3.166 | 61.163 |
| 7 | 2.267 | 50.11 | 2.28121 | 50.583 |
| 8 | 3.365 | 59.02 | 3.39978 | 60.364 |
| 9 | 2.154 | 47.51 | 2.18247 | 47.651 |
| 10 | 3.548 | 61.24 | 3.61619 | 62.322 |
| 11 | 2.338 | 46.92 | 2.32226 | 46.473 |
| 12 | 3.486 | 53.88 | 3.54225 | 54.041 |
| Prediction | Values Obtained |
|---|---|
| First prediction | RMSE_velocity = 0.0290 m/s |
| RMSE_temperature = 0.330 °C R2 velocity = 0.999 | |
| R2 temperature = 0.998 | |
| Second prediction | RMSE_velocity = 0.033 m/s RMSE_temperature = 0.783 °C R2 velocity = 0.999 R2 temperature = 0.997 |
| Output Variable | CV RMSE | CV MAPE (%) | CV R2 |
|---|---|---|---|
| Outlet Velocity | 0.022801 m/s | 0.7636% | 0.998958 |
| Outlet Temperature | 0.485121 °C | 0.5602% | 0.990976 |
| Parameter | Magnitude |
|---|---|
| Gravity | On |
| Skewness | 0.6 |
| Element size | 0.03 m |
| Maximum layers | 10 |
| Growth rate | 1.2 |
| First layer thickness | 0.00005 m |
| Number of iterations | 1500 |
| Iteration | Continuity | x-Velocity | y-Velocity | z-Velocity | Energy | k | ω |
|---|---|---|---|---|---|---|---|
| 100 | 1.8644 × 10−2 | 1.2700 × 10−4 | 1.0564 × 10−4 | 1.5115 × 10−4 | 1.0113 × 10−5 | 1.3708 × 10−4 | 4.9381 × 10−4 |
| 250 | 1.1326 × 10−3 | 3.4901 × 10−6 | 4.2624 × 10−6 | 5.5010 × 10−6 | 2.0184 × 10−6 | 8.6126 × 10−6 | 3.6627 × 10−5 |
| 500 | 4.6523 × 10−4 | 1.0243 × 10−6 | 1.4387 × 10−6 | 1.4879 × 10−6 | 1.0048 × 10−6 | 7.7172 × 10−6 | 1.7077 × 10−4 |
| 698 | 5.1756 × 10−4 | 1.1313 × 10−6 | 1.6195 × 10−6 | 1.8689 × 10−6 | 9.9845 × 10−7 | 3.6295 × 10−6 | 1.7640 × 10−5 |
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Share and Cite
Morano-Okuno, H.R.; San Vicente-Cisneros, A.R.; Sandoval-Benitez, G. Exploring the Capabilities of an LLM from CFD Simulations of Turbulent Flow in a Manifold. Appl. Sci. 2026, 16, 5300. https://doi.org/10.3390/app16115300
Morano-Okuno HR, San Vicente-Cisneros AR, Sandoval-Benitez G. Exploring the Capabilities of an LLM from CFD Simulations of Turbulent Flow in a Manifold. Applied Sciences. 2026; 16(11):5300. https://doi.org/10.3390/app16115300
Chicago/Turabian StyleMorano-Okuno, Hector Rafael, Armando Rafael San Vicente-Cisneros, and Guillermo Sandoval-Benitez. 2026. "Exploring the Capabilities of an LLM from CFD Simulations of Turbulent Flow in a Manifold" Applied Sciences 16, no. 11: 5300. https://doi.org/10.3390/app16115300
APA StyleMorano-Okuno, H. R., San Vicente-Cisneros, A. R., & Sandoval-Benitez, G. (2026). Exploring the Capabilities of an LLM from CFD Simulations of Turbulent Flow in a Manifold. Applied Sciences, 16(11), 5300. https://doi.org/10.3390/app16115300

