Hi, I'm Amogh — CFD Engineer!

I do

  • Chemical Reactor Simulations
  • Heat Transfer & Multiphase Flow
  • Computational Fluid Dynamics
  • Agentic AI Modeling & Simulation
  • Finite Element Analysis
  • Workflow Automation
Portrait of Amogh Meshram.
  • Postdoctoral Researcher National Laboratory of the Rockies
  • PhD, Chemical Engineering Arizona State University
  • BTech & MTech, Chemical Engineering Indian Institute of Technology Bombay
Let's Work Together!

Tools I use

About Me

Where I Am Now

Hello! I'm Amogh, a postdoctoral researcher in Computational Science Center at the National Laboratory of the Rockies. I build numerical models that tell engineers whether a reactor will actually work — before anyone spends millions finding out.

Where I work — the National Laboratory of the Rockies campus in Golden, Colorado
Cutaway schematic of a hydrogen direct-reduction shaft furnace. Iron oxide
                        pellets enter through a feed and lock hopper at the top and descend through a
                        pre-heating zone at about 400 °C, a reduction zone at about 900 °C, and a
                        cooling zone at about 100 °C. Hot hydrogen enters through a bustle near the
                        base and flows upward against the descending bed; the pellets change from red
                        hematite at the top to grey metallic iron at the bottom, and steam leaves with
                        the top gas. Reduced product discharges through a conical region at the base.
The reactor I model — Direct Reduction Reactor for Ironmaking using H2 and Natural Gas

Right now I make 3D CFD-DEM models of iron ore reduction in Ansys Rocky, running on HPC and resolving individual pellets, the gas moving around them, and the chemistry happening inside them. Alongside that I'm building a single-pellet model in AMReX to scale up from — and I've automated much of the modeling pipeline with AI, so more of my time goes into physics and less into plumbing.

The PhD Years

My PhD research at Arizona State University was done as a part of the GISH project under the supervision of Prof. Sridhar Seetharaman. My thesis was titled "Modeling and Simulation of iron ore reduction at lab scale, pilot scale, and industrial scale". What changes across those scales isn't the physics and chemistry — it's which simplifications you're still allowed to make.

Illustration of hydrogen iron ore reduction modelled at three scales, left to
                      right. Lab scale: a quartz-tube furnace, thermogravimetric balance, mass flow
                      controllers and hydrogen and nitrogen cylinders, beside a cutaway single pellet
                      showing shrinking-core layers — hematite core, magnetite shell, wustite shell
                      and metallic iron rim — half overlaid with a finite-element mesh and a
                      concentration contour, with hydrogen diffusing in and water vapour out. Pilot
                      scale: an insulated steel reactor on a frame with a lock hopper, gas preheater,
                      thermocouple ports and a quartz viewing window, cut away to show a packed bed
                      grading from red pellets at the top to grey at the bottom, next to monitors
                      showing a contour plot and a metallization curve. Industrial scale: a tall
                      shaft furnace with feed and lock hoppers, preheating, reduction and cooling
                      zones, a ring-shaped bustle pipe injecting hydrogen upward against the
                      descending bed, a CFD-DEM particle field coloured by metallization, metallized
                      DRI discharging onto a conveyor, and an electrolyser and wind turbines behind.
The thesis in one picture — the same reduction chemistry carried from a single pellet, to the pilot reactor, to an industrial shaft furnace

I ran the experiments that fed the models too, building a gas mixing rig and characterizing pellets with FE-SEM, TGA, and porosity analysis. The project commissioned the first pilot-scale reactor capable of reducing iron ore pellets with both hydrogen and natural gas, which is where I learned what simulation can't teach you: what fails first, and which of your assumptions were load-bearing.

Where It Started

Earlier I spent two years on gas separation membranes and electrospun fibers, building both a separation rig and an electrospinning setup from scratch. That started at IIT Bombay with dual degree work on biogas purification, where I also spent time in rural Maharashtra studying how biogas actually gets used — the clearest lesson I've had that a technology only counts once it survives the field.

Illustration following biogas from a village to a laboratory membrane, left to
                      right. Village digester: a farmhouse on dry scrubland with a rooftop solar panel
                      and a biogas stove burning inside, cattle nearby, and a cutaway fixed-dome
                      digester showing cattle dung slurry entering an inlet tank, a fermentation dome
                      and a slurry displacement chamber. A magnified inset shows the raw gas as mixed
                      methane, carbon dioxide and trace sulphur molecules. Hollow-fibre spinning: a
                      pressurised dope vessel and bore-fluid vessel driven by gear pumps into a
                      spinneret, shown cut away extruding an annulus of amber polymer around a central
                      bore fluid; the nascent fibre stretches through an air gap into a water
                      coagulation bath, over guide rollers and a godet onto a take-up drum. An inset
                      shows one fibre in cross-section — open lumen, thin outer skin holding
                      metal-organic framework crystals, and finger-like pores through the wall.
                      Permeation rig: mass flow controllers, valves, rotameter and pressure gauges on
                      an aluminium frame feeding a cutaway hollow-fibre module where carbon dioxide
                      passes out through the fibre walls and methane leaves as the purified product,
                      with a gas chromatograph alongside and the clean gas feeding a steady blue
                      cooking flame.
Where it started — village biogas, then hollow-fibre membranes built and tested to clean it up

My Stack

The software and instruments I actually work in, day to day.

COMSOL Multiphysics

Coupled flow, heat, mass transfer and kinetics

Ansys Fluent

Computational fluid dynamics

Ansys Rocky

Discrete element method, coupled CFD-DEM

AMReX

Block-structured adaptive mesh refinement

OpenFOAM

Open-source CFD toolbox

C++

Custom solvers and post-processing

Python

Scripting, data analysis and automation

Agentic Modeling

AI agents that set up, run and post-process cases

Agentic Workflow

Automated pipelines from setup to report

FE-SEM & EDAX

Microstructure and elemental mapping

TGA

Reduction kinetics from mass loss

Six Sigma Green Belt

Lean, DMAIC, OpEx, root cause analysis

Expertise

What I get hired to do.

  1. Multiphysics Modeling & Simulation

    Finite element and discrete element models that solve fluid flow, heat and mass transfer, and reaction kinetics as one coupled system. Built for equipment that has to work in the real world, not just converge.

  2. Agentic AI & Workflow Automation

    AI agents that build cases, launch them, post-process the output and draft the report — the plumbing around a simulation rather than the physics inside it. The point is to spend engineering time on judgement rather than on shepherding files.

  3. Scale-Up: Lab to Pilot to Industrial

    Carrying kinetics measured on a bench sample all the way to full-size equipment with the physics intact — and knowing which simplifications stop being safe at each step. I've validated the same model family at all three scales.

  4. Commissioning & Troubleshooting

    Working out what a plant is actually doing, as opposed to what it was designed to do. Reading modelled temperature, flow and species fields against operating data until the discrepancy explains itself — then naming the change that fixes it.

  5. Techno-Economic Assessment

    Turning simulation output into the number a decision-maker needs: cost per tonne, payback, and the operating window where a process stops paying for itself. I've written the assessment a $15 million capital decision was made on.

  6. Process & Experiment Design

    Design of experiments, protocol development, and building instrumented rigs from nothing — including gas handling for flammable and toxic streams. Designed to produce data a model can actually be held to.

Research

Agentic AI

Agentic AI for Modeling, Simulation and Automation

National Laboratory of the Rockies · 2024–present

At the National Laboratory of the Rockies I build simulations of an experimental furnace that makes iron out of ore using hydrogen. The most detailed of them is three-dimensional and follows the pellets of ore as individual objects, with the gas flowing around them, built in Ansys Rocky and Ansys Fluent and run on the laboratory's supercomputer. One thing stood in the way: Rocky can move particles about but it has no way of making them react, so the chemistry had to be written from scratch as a custom module. I developed that module with Ansys's own engineers.

Writing it is skilled, slow work. So I trained an AI agent on the software's developer documentation, along with example code and tutorials. It now writes and compiles a working module on its own.

Three-panel diagram of the agent workflow. Module development: manuals of documentation, example code and tutorials feed an AI agent cabinet, which sends a machined module through a compile stage into a socket in the reacting-particle solver. Simulation automation: an agent beside an HPC cluster drives a loop of five stations — submit, run, save, adjust, restart — with fainter rings behind for parallel cases. Post-processing: raw simulation output passes through the agent to screens showing contour field profiles and trend curves.
Where the agents do the work: writing the module, running the cases, and turning the output into results.

The second job was duller and cost more time. A simulation could only run about an hour before it had to be stopped and saved, adjusted by hand in the interface, written out as a restart file and started again — then the same thing an hour later, for every case, each covering a full day of reactor time. Days of my week went on that. An agent now runs the whole loop in Python: it submits the jobs, handles the restarts and keeps going without me.

The third piece is AMReX, an open-source simulation framework the laboratory's SAMS group has already built codes on. I trained an agent on those codes and set it to work on iron ore reduction. It can reproduce a model of one ore pellet turning into iron, which I had built in COMSOL during my PhD.

Reactor Modeling

Modeling Ironmaking on Pilot and Industrial Scale

Arizona State University · National Laboratory of the Rockies · 2020–present

  • 95 %+ of the ore turned into metal, guided by the model
  • $15M pilot plant investment informed by the cost analysis
  • 1st reactor in the USA to make iron with hydrogen, modelled and checked

Iron is made in a shaft furnace: pellets of ore go in at the top, hot reducing gas comes up from below, and reduced iron leaves at the bottom. That gas has normally been made from reformed natural gas.

In 2021 the United States Department of Energy started the Grid-Interactive Steelmaking with Hydrogen project, or GISH, to lower the risk of investing in the equipment needed to make iron with hydrogen instead and turn it into steel in an electric arc furnace. A pilot reactor was built as part of that project. It was small, but built to the same design as a full plant so its results would carry over. One of the things we wanted to know was how it would behave when the feed was changed from pure hydrogen to a mixture of hydrogen and reformed natural gas.

Interior of the pilot plant: a steel structure under an arched corrugated roof, with yellow handrails and stairs, ladders, an insulated vertical vessel and pipework running between platforms.
Inside the pilot plant.
A tanker trailer carrying long cylindrical tubes labelled hydrogen, compressed, parked outside a corrugated metal building, with a worker in a high-visibility vest beside it and small storage vessels behind orange barriers.
Hydrogen arriving at the site by tube trailer.

I built a FEA multiphysics model of that reactor. What it predicted for the quality of metal produced was close to what the plant actually made, and so were the temperatures it gave for the inside of the furnace. That agreement is what made it usable on the plant rather than only on paper. When the pilot clogged during commissioning, the model was used to work out how to bring it back into operation, and to say in advance how a startup would go. The work is described in this paper. The pictures below show the simulation results at a steady state, showing how the soild species and gaseous species vary inside the pilot reactor geometry.

Modelled mass fraction of iron ore through a vertical slice of the pilot reactor, highest at the top where the pellets enter and falling away down the shaft.
Iron ore, Fe2O3
Modelled mass fraction of the part-reduced oxide through the pilot reactor, forming in the middle of the shaft between the ore above and the iron below.
Part-reduced, FeO
Modelled mass fraction of metallic iron through the pilot reactor, reaching its highest values in the lower part of the shaft and the cone below it.
Iron, Fe
Modelled hydrogen concentration through the pilot reactor, entering low in the shaft and thinning out as it rises and is consumed.
Hydrogen, H2
Modelled water vapour concentration through the pilot reactor, building up where the hydrogen has been used and rising towards the gas outlet.
Water vapour, H2O

The same model was then scaled up to industrial size, to a shaft of the proportions a commercial plant would actually use. No plant of that kind existed to compare it against, so the scaled version rests on the agreement already established at pilot scale. One result stands out on its own: the reactor needs appreciably more hydrogen than the chemistry alone would require, and the surplus leaves unused. The pictures below are the same set of profiles for that larger reactor, with the temperature of the pellets added.

Modelled mass fraction of iron ore through a vertical slice of the industrial-scale reactor, concentrated in the upper part of the reduction zone.
Iron ore, Fe2O3
Modelled mass fraction of the part-reduced oxide through the industrial-scale reactor, spread through the upper, middle and lower reduction zone.
Part-reduced, FeO
Modelled mass fraction of metallic iron through the industrial-scale reactor, filling the lower reduction zone and the cooling cone beneath it.
Iron, Fe
Modelled hydrogen concentration through the industrial-scale reactor, highest at the gas inlet and falling as it works its way up and inwards.
Hydrogen, H2
Modelled water vapour concentration through the industrial-scale reactor, rising exactly where the hydrogen has been consumed.
Water vapour, H2O
Modelled pellet temperature through the industrial-scale reactor, hot through the reduction zone with cooler bands where the reaction draws heat in and a sharp drop in the cooling cone.
Pellet temperature
Chemical Kinetics

Simulating Iron Ore Reduction on Lab Scale

Arizona State University · 2020–2024

  • 22 citations on the resulting paper
  • 3 temperatures, from 800 to 900 °C
  • 3 gas flow rates measured at each one

For as long as anyone has made steel, the job has been the same one: get the oxygen out of the iron ore. What changes is the gas you use to do it. That gas has usually been made from coal, natural gas, and commercial plants have decades of experience running on it. Then hydrogen arrived as the alternative — and when someone asked how a furnace would actually behave once it switched over, there was no confident answer.

Diagram of a pellet in a gas stream with reduction reaction equations for hydrogen and carbon monoxide.
Iron ore reduction using hydrogen and carbon monoxide.
Schematic of gas diffusing into a porous iron ore pellet, reacting, and product gas diffusing out.
Gas diffusion and reaction inside a pellet.

You cannot find the answer by watching. An industrial furnace is millions of pellets stacked several storeys deep, sinking slowly through a reducing gas mixture, and nothing about the inside of that pile is visible from outside it. So the question had to be made smaller. We took a single pellet, hung it on a wire, and lowered it into a furnace on its own — one pellet at a time reduced using different gas mixtures, at different temperatures, followed from start to finish. How long did it take to turn iron ore into iron, and what held it back? These experiments helped us obtain the chemical kinetics of the reduction process.

Laboratory reduction furnace and gas handling rig used for single-pellet experiments.
The lab furnace experimental setup for reducing pellets.
A single dark grey iron ore pellet, its surface visibly cracked, held in a small wire cradle and hanging from a thin wire in the laboratory.
A single pellet on its wire hanger, ready to go into the furnace.

Do that enough times and a pattern appears. The data obtained from the pattern goes into a model, and once the model can reproduce what the pellet did on the laboratory scale, you can start asking it about pellets nobody has tested — a different gas, a different mixture, a furnace that has not been built yet. That is what the whole exercise is for. A question that used to be settled by trial and error on a running plant gets answered on a computer first. The measurements and the model are set out in the paper.

Simulated hematite concentration inside a pellet during reduction, animated. Fe2O3
Simulation of a single pellet — the raw ore being used up.
Simulated metallic iron fraction developing inside the same pellet. Fe
The same run — iron metal appearing in its place.
Gas Separation

Membranes and Electrospun Fibers for Gas Separation

Arizona State University · IIT Bombay · Tata Centre · 2015–2021

  • 84 citations on the resulting review paper
  • 99+ different gases can be tested
  • 50 % less time to test a membrane

A membrane is a thin sheet of polymer that pulls one gas out of a mixture without ever having to turn it into a liquid. All it needs is higher pressure on one side than the other, and one gas slips through faster than the rest. The catch is a stubborn one, and it is about the material rather than the machinery: the sheets that are fussiest about which gas they let through are also the slowest, and the quick ones are not fussy enough. You can have a clean separation or a fast one, but not both — which is what has kept membranes out of the harder jobs. Mixing tiny crystals into the polymer is one way around it. The most promising ones are called metal–organic frameworks: they are riddled with holes of a very exact size, so small molecules pass through and larger ones cannot, their structure can be tuned to the job, and they sit comfortably in the polymer rather than fighting it. My co-authors and I set that case out in a review of the field for the Journal of Polymer Science.

Two membrane modules compared. Left, a hollow fiber module drawn as a cutaway cylinder: a
                          dense bundle of parallel hollow fibers sealed at both ends in resin potting, raw biogas
                          entering the fiber bores at one end, carbon dioxide, hydrogen sulfide and water passing out
                          through the fiber walls to a shell port as permeate, and methane continuing along the bores
                          to leave as biomethane. A cross-section inset shows the shell packed with fiber circles, and
                          a magnified callout shows one fiber wall as a thin dense layer over a thicker porous support.
                          Right, a flat sheet module drawn as an exploded plate-and-frame stack: upper plate, feed
                          spacer, flat membrane sheet, permeate spacer and lower plate, with the feed sweeping across
                          the sheet, permeate leaving below and biomethane leaving at the far edge.
Two ways to package the same membrane. In both, the unwanted gases pass through it and are drawn off to the side; the methane never crosses it, and comes out of the far end.
Three panels. Left, a dense polymer film shown edge-on with tangled chains: a crowded feed of
                          methane and carbon dioxide on one side, carbon dioxide dissolving into and diffusing through
                          the film, and a sparse carbon-dioxide-rich permeate on the other. Centre, a log-log plot of
                          selectivity against permeability in which a cloud of points trends downward to the right
                          beneath a straight upper bound line, with an arrow pointing up and across it. Right, the same
                          polymer film now holding dispersed faceted crystals, with two magnified callouts showing an
                          ordered cubic framework of metal nodes and linkers, a carbon dioxide molecule passing through
                          a window and a larger methane molecule rejected.
Left: gas works its way through a solid polymer sheet. Middle: the sheets that separate best are the slowest. Right: crystals mixed into the polymer are a way past that.

At Arizona State University I built a setup that makes electrospun fibers with those crystals inside fibers. It draws a single thread out of two liquids at once, one wrapped around the other, so the crystals and other tiny particles end up sealed inside the thread rather than sitting on its surface. Fibers made this way separate a gas by a different trick from the sheets: instead of letting one gas through, they catch it and hold on to it in the adsorption process at high pressure. The two approaches were running side by side. I also built the test rig that measures how the sheets themselves perform, in both of the shapes they are made in — flat sheets, and bundles of fine hollow tubes.

Core–shell electrospinning facility built at Arizona State University to spin fibres carrying metal–organic framework and nanoparticle fillers.
The fiber-spinning machine I built at ASU.
Gas permeation test rig: stainless steel tubing with mass flow controllers, needle valves, rotameter and pressure gauge on an aluminium frame.
The test rig I built at ASU, for measuring both flat sheets and bundles of hollow tubes.
Detail of the gas manifold showing flow controllers and compression fittings.
Close-up of the gas controls.

Earlier, at IIT Bombay and the Tata Centre, I built a test rig of my own. What drove that work was biogas — the gas that comes off rotting organic waste such as cattle dung. It burns, but it comes out watered down with carbon dioxide and other unwanted gases. Take those away and what is left is concentrated methane, the same gas piped into kitchens. I learned to make the hollow tubes there on the Membrane Lab's existing equipment, under Prof. Jayesh Bellare.

Spin fabrication of hollow fiber membranes.
Gas separation test rig on a blue steel frame at IIT Bombay: three pressure gauges along the top, digital mass flow controllers and needle valves on the middle shelf, a membrane cell on a stand, a rotameter and tubing running between them.
The test rig I built at IIT Bombay.

Experience

  1. Postdoctoral Researcher — Computational Science Center

    National Laboratory of the Rockies

    Apr 2024 — Present · Golden, Colorado

  2. Doctoral Researcher — School for Engineering of Matter, Transport and Energy

    Arizona State University

    Aug 2019 — Mar 2024 · Tempe, Arizona

  3. Research Engineer

    Tata Centre for Technology and Design

    Feb 2018 — Jul 2019 · Mumbai, India

  4. Research Intern

    Aristotle University of Thessaloniki

    May 2014 — Jul 2014 · Thessaloniki, Greece

Education

  1. PhD, Chemical Engineering

    Arizona State University

    2019 — 2024 · Tempe, Arizona

  2. BTech & MTech, Chemical Engineering

    Indian Institute of Technology Bombay

    2012 — 2017 · Mumbai, India

Speaking & Press

Conference Talks and Guest Lectures

  1. Oct 2024

    Modeling Iron Ore Reduction on Pilot and Industrial Scale to Determine the Economic Penalty of Pure H2 Operation

    Materials Science & Technology 2024 Technical Meeting

  2. Aug 2024

    Multiphysics Modeling of DRI Pellet Reduction on Laboratory Scale and Pilot Scale

    Rocky Mountain Fluid Mechanics Research Symposium

  3. Apr 2023

    Numerical Modeling of the First Hydrogen Direct Reduction Pilot Plant in the USA

    National Laboratory of the Rockies, Colorado

  4. Jan 2023

    How to Get Accepted for MS/PhD Programs, or Build a Career in Core Industry, with a Low CPI or Backlogs

    Indian Institute of Technology Bombay

In the press

  1. Aug 2023
  2. Apr 2023

Publications

Ten peer-reviewed papers and proceedings, 363 citations. Full list on Google Scholar.

  1. 2026

    Commissioning and Optimization of a Pilot-Scale Hydrogen/Natural Gas DRI Reactor

    AISTech Conference Proceedings

    J. W. Govro, A. Meshram, F. Calderon, Y. Korobeinikov, D. Dalle Nogare and others

  2. 2025

    Quantification of Swelling in Hematite Pellets Reduced Using Hydrogen–Nitrogen Gas Mixture

    Steel Research International, 96(5)

    A. Meshram, Y. Korobeinikov, X. Wei, R. J. O'Malley, S. Sridhar

    7
  3. 2024 1
  4. 2023 15
  5. 2023

    Reduction of Iron-Ore Pellets Using Different Gas Mixtures and Temperatures

    Steel Research International, 94(10)

    Y. Korobeinikov, A. Meshram, C. Harris, O. Kovtun, J. Govro, R. J. O'Malley, O. Volkova, S. Sridhar

    45
  6. 2023

    Melting Behavior of Hydrogen-Reduced DRI in a Simulated EAF Steel Bath

    Iron and Steel Technology, 20(4)

    J. Govro, A. Meena, S. Chakraborty, A. Meshram, Y. Korobeinikov, K. Phillips and others

    10
  7. 2022

    Modeling Isothermal Reduction of Iron Ore Pellet Using Finite Element Analysis Method: Experiments & Validation

    Metals, 12(12), 2026

    A. Meshram, J. Govro, R. J. O'Malley, S. Sridhar, Y. Korobeinikov

    27
  8. 2022

    Modeling of Isothermal Reduction of Hematite Pellets Using Hydrogen

    AISTech Conference Proceedings, 266–274

    A. Meshram, J. Govro, Y. Korobeinikov, S. Chakraborty, R. J. O'Malley, S. Seetharaman

    1
  9. 2021

    Unusual Positive Effect of SO2 on Mn-Ce Mixed-Oxide Catalyst for the SCR Reaction of NOx with NH3

    Chemical Engineering Journal, 407, 127071

    J. Chen, P. Fu, D. Lv, Y. Chen, M. Fan, J. Wu, A. Meshram, B. Mu, X. Li, Q. Xia

    173
  10. 2020

    Metal–Organic Framework-Based Mixed-Matrix Membranes for Gas Separation: An Overview

    Journal of Polymer Science, 58(18), 2518–2546

    J. Winarta, A. Meshram, F. Zhu, R. Li, H. Jafar, K. Parmar, J. Liu, B. Mu

    84

Contact Me

If something here overlaps with what you are working on, I would be glad to hear about it — whether that is a problem you are trying to model, a collaboration, a role you are looking to fill, or an event you are putting together.

Amogh.Meshram@nlr.gov