PageSourceSearch

https://detchem.com/applications

html detchem.com collected 2026-10-07 13:57:25 UTC 29,252 bytes, 93 lines download raw bytes

1<!DOCTYPE html><html lang="en" class="h-full scroll-smooth"><head><meta charSet="utf-8"/><meta name="viewport" content="width=device-width, initial-scale=1"/><link rel="preconnect" href="https://fonts.googleapis.com"/><link rel="preconnect" href="https://fonts.gstatic.com" crossorigin="anonymous"/><link rel="stylesheet" href="https://fonts.googleapis.com/css2?family=Inter:[email protected]&amp;display=swap"/><link rel="stylesheet" href="https://fonts.googleapis.com/css2?family=Lexend:[email protected]&amp;display=swap"/><link rel="stylesheet" href="/assets/tailwind-B5VNUVGY.css"/><link rel="icon" href="/images/detchem-logo-edit_inverted.svg"/></head><body class="flex min-h-screen flex-col justify-between font-sans"><header><nav class=" relative z-50 flex justify-between px-6 py-6 sm:px-10 sm:py-6 mx-auto container"><div class="flex items-center md:gap-x-12"><a data-discover="true" href="/"><span class="sr-only">DETCHEM home page</span><img alt="DETCHEM logo" src="/images/detchem-logo-edit.svg" class="size-12 md:size-14 lg:size-16"/></a></div><div class="flex items-center"><div class="hidden md:block"><div class="relative inline-block" data-headlessui-state=""><button class="inline-flex font-medium items-center ml-5 border px-5 py-2 text-slate-700 hover:bg-slate-100 hover:text-slate-900 rounded-lg border-transparent" type="button" aria-expanded="false" data-headlessui-state=""><span>Software</span><svg xmlns="http://www.w3.org/2000/svg" viewBox="0 0 20 20" fill="currentColor" aria-hidden="true" data-slot="icon" class="size-5"><path fill-rule="evenodd" d="M5.22 8.22a.75.75 0 0 1 1.06 0L10 11.94l3.72-3.72a.75.75 0 1 1 1.06 1.06l-4.25 4.25a.75.75 0 0 1-1.06 0L5.22 9.28a.75.75 0 0 1 0-1.06Z" clip-rule="evenodd"></path></svg></button></div><span hidden="" style="position:fixed;top:1px;left:1px;width:1px;height:0;padding:0;margin:-1px;overflow:hidden;clip:rect(0, 0, 0, 0);white-space:nowrap;border-width:0;display:none"></span><div class="relative inline-block" data-headlessui-state=""><button class="inline-flex font-medium items-center ml-5 border px-5 py-2 text-slate-700 hover:bg-slate-100 hover:text-slate-900 rounded-lg border-transparent" type="button" aria-expanded="false" data-headlessui-state=""><span>Databases</span><svg xmlns="http://www.w3.org/2000/svg" viewBox="0 0 20 20" fill="currentColor" aria-hidden="true" data-slot="icon" class="size-5"><path fill-rule="evenodd" d="M5.22 8.22a.75.75 0 0 1 1.06 0L10 11.94l3.72-3.72a.75.75 0 1 1 1.06 1.06l-4.25 4.25a.75.75 0 0 1-1.06 0L5.22 9.28a.75.75 0 0 1 0-1.06Z" clip-rule="evenodd"></path></svg></button></div><span hidden="" style="position:fixed;top:1px;left:1px;width:1px;height:0;padding:0;margin:-1px;overflow:hidden;clip:rect(0, 0, 0, 0);white-space:nowrap;border-width:0;display:none"></span><a class="font-medium ml-5 border inline-block px-5 py-2 text-slate-700 hover:bg-slate-100 hover:text-slate-900 rounded-lg border-transparent" data-discover="true" href="/applications">Applications</a><a class="font-medium ml-5 border inline-block px-5 py-2 text-slate-700 hover:bg-slate-100 hover:text-slate-900 rounded-lg border-transparent" data-discover="true" href="/contact">Contact</a></div><div class="-mr-1 md:hidden"><div class="relative"><button id="mobile-menu-button" type="button" class="relative inline-flex items-center justify-center rounded-md p-2 border border-slate-700 text-gray-400 bg-white hover:text-omegadot-blue-950 focus:text-gray-400 focus:outline-none focus:ring-2 focus:ring-inset focus:ring-white" aria-controls="mobile-menu" aria-expanded="false"><span class="absolute -inset-0.5"></span><span class="sr-only">Open main menu</span><svg id="mobile-menu-svg-closed" class="block h-6 w-6" fill="none" viewBox="0 0 24 24" stroke-width="1.5" stroke="currentColor" aria-hidden="true"><path stroke-linecap="round" stroke-linejoin="round" d="M3.75 6.75h16.5M3.75 12h16.5m-16.5 5.25h16.5"></path></svg><svg id="mobile-menu-svg-open" class=" h-6 w-6 text-omegadot-blue-950 hidden" fill="none" viewBox="0 0 24 24" stroke-width="1.5" stroke="currentColor" aria-hidden="true"><path stroke-linecap="round" stroke-linejoin="round" d="M6 18L18 6M6 6l12 12"></path></svg></button></div></div></div></nav></header><main class="bg-beams bg-cover min-h-screen"><div class="pt-16 sm:pt-32 pb-8 sm:pb-16 text-center"><h1 class="text-5xl font-medium font-display tracking-light text-slate-900">DETCHEM Applications</h1><p class="px-4 mt-4 max-w-2xl mx-auto text-lg leading-loose text-slate-600">A non-exhaustive list of DETCHEM applications in the fields of catalysis, reactor design, and materials synthesis.</p></div><div class="mx-auto flex flex-row justify-center">
1<div class="min-h-screen 2xl:grid xl:grid-cols-[250px_1fr_250px] "><aside class="p-4 hidden 2xl:flex px-8 pt-24 justify-end top-0"><aside class="w-52"><div class="sticky top-24 h-full"><h2 class="font-display text-lg text-slate-700">Applications of DETCHEM</h2><nav class="mt-8"><ul class="space-y-4"><li><a href="#cpox-reactor" class="group flex items-center gap-3 transition-colors text-slate-500 hover:text-indigo-600"><span class="text-sm font-medium">CPOX Reactor Modeling (DUO)</span></a></li><li><a href="#sofc-stack" class="group flex items-center gap-3 transition-colors text-slate-500 hover:text-indigo-600"><span class="text-sm font-medium">Solid Oxide Fuel Cell (SOFC) Stack Modeling</span></a></li><li><a href="#flow-field" class="group flex items-center gap-3 transition-colors text-slate-500 hover:text-indigo-600"><span class="text-sm font-medium">Flow Field Modeling (DUO)</span></a></li><li><a href="#materials-synthesis" class="group flex items-center gap-3 transition-colors text-slate-500 hover:text-indigo-600"><span class="text-sm font-medium">Materials Synthesis</span></a></li><li><a href="#high-temp-catalysis" class="group flex items-center gap-3 transition-colors text-slate-500 hover:text-indigo-600"><span class="text-sm font-medium">High Temperature Catalysis</span></a></li><li><a href="#automotive-converters" class="group flex items-center gap-3 transition-colors text-slate-500 hover:text-indigo-600"><span class="text-sm font-medium">Automotive Catalytic Converters</span></a></li></ul></nav></div></aside></aside><div class="hidden"></div><div class="container pb-24 pt-16 px-4 lg:px-10 space-y-16"><div class="bg-dark-blue bg-cover py-16 rounded-2xl"><section id="cpox-reactor" class="scroll-mt-20"><div class="px-4 lg:px-10"><h2 class="text-4xl font-medium font-display tracking-light text-white">CPOX Reactor Modeling (DUO)</h2><div class="mt-12 flex flex-col lg:flex-row items-start gap-12 lg:gap-20"><div class="lg:w-1/2 space-y-4"><h3 class="font-display text-lg text-indigo-400">Modeling of a fixed bed reactor</h3><p class="text-lg leading-loose text-slate-300">Modeling of a fixed-bed catalytic tube reactor with 86 particles for catalytic partial oxidation (CPOX) process with the code DUO=OpenFOAM+DETCHEM. The small tube-to-particle diameter ratio of 2 requires the use of 3D Particle-Resolved Computational Fluid Dynamics (PRCFD) models to capture the salient physics, including heat and mass transfer effects. The plot shows on left side a slice and isosurfaces of methane concentration. On the right side some streaklines and the reaction rate of methane on the surface of the particles. Flow is from top to bottom.</p></div><div class="lg:w-1/2 w-full "><div class="flex flex-col sm:flex-row gap-8 w-full justify-center"><div class="flex items-center flex-col"><p class="mb-4 text-sm text-center text-slate-300 sm:text-left">CONCENTRATION CH₄</p><img src="/images/cfd1.jpg" alt="Methane Concentration" class="w-[200px] h-auto object-contain rounded-md border-white border-2 max-h-[300px]"/></div><div class="flex items-center flex-col"><p class="mb-4 text-sm text-center text-slate-300 sm:text-left">SURFACE RATE CH₄</p><img src="/images/cfd2.jpg" alt="Methane Surface Rate" class="w-[200px] h-auto object-contain rounded-md border-white border-2 max-h-[300px]"/></div></div><div class="mt-4 text-xs text-slate-300"><b>Reference:</b> <!-- -->E. Daymo, M. Hettel, O. Deutschmann, G. Wehinger. Accelerating particle-resolved CFD simulations of catalytic fixed-bed reactors with DUO. Chemical Engineering Science 250 (2022) 117408<!-- --> <a href="https://doi.org/10.1016/j.ces.2021.117408" target="_blank" rel="noopener noreferrer" class="text-indigo-400 hover:underline">Read More</a></div></div></div><div class="mt-12 flex flex-col lg:flex-row items-start gap-12 lg:gap-20"><div class="lg:w-1/2 space-y-4"><p class="text-lg leading-loose text-slate-300">The effect of Cell Agglomeration (CA) technique on calculation speed and accuracy was investigated. Speedup factor was between 7 for catalytic partial oxidation (CPOX) and 35 for dry reforming of methane (DRM). Picture shows CPOX case: a.) conversion rate of methane (reference case), b.) conversion rate of methane (CA case), c.) local calculation error, d.) bin interval for rate of methane using 5 bins.<p class="mb-2 mt-4 max-w-3xl md:mb-0 md:mt-6"><a class="group inline-flex items-center justify-center rounded-full py-2 px-4 text-sm  font-semibold focus:outline-none focus-visible:outline-2 focus-visible:outline-offset-2 bg-omegadot-blue-950 text-white hover:bg-slate-700 hover:text-slate-100 active:bg-slate-800 active:text-slate-300 focus-visible:outline-slate-900  " href="https://doi.org/10.1016/j.ces.2021.117408" target="_blank">Read research article<!-- --> <span class="sr-only"> on CFD data</span><svg class="ml-3 overflow-visible" width="3" height="6" viewBox="0 0 3 6" fill="none" stroke="currentColor" stroke-width="2" stroke-linecap="round" stroke-linejoin="round"><path d="M0 0L3 3L0 6"></path></svg></a></p></p></div><div class="lg:w-1/2 w-full "><img src="/images/applications/DUO_5_alpha.png" alt="CPOX reactor modeling with Cell Agglomeration" class="rounded-lg border-2 border-slate-700 w-full object-contain bg-white max-h-[300px]"/><div class="mt-4 text-xs text-slate-300"><b>Reference:</b> <!-- -->E. Daymo, M. Hettel, O. Deutschmann, G. Wehinger. Accelerating particle-resolved CFD simulations of catalytic fixed-bed reactors with DUO. Chemical Engineering Science 250 (2022) 117408<!-- --> <a href="https://doi.org/10.1016/j.ces.2021.117408" target="_blank" rel="noopener noreferrer" class="text-indigo-400 hover:underline">Read More</a></div></div></div><div class="mt-12 flex flex-col lg:flex-row items-start gap-12 lg:gap-20"><div class="lg:w-1/2 space-y-4"><p class="text-lg leading-loose text-slate-300">Temperature field of the fluid part and the two solid bodies (only the second one is coated). Fluid part and solid regions are solved with OpenFOAM® whereas the detailed surface reaction is calculated by DETCHEM. Additionally, some streaklines are plotted. The slice at the end of the calculation domain shows the distribution of the velocity into z-direction.<p class="mb-2 mt-4 max-w-3xl md:mb-0 md:mt-6"><a class="group inline-flex items-center justify-center rounded-full py-2 px-4 text-sm  font-semibold focus:outline-none focus-visible:outline-2 focus-visible:outline-offset-2 bg-omegadot-blue-950 text-white hover:bg-slate-700 hover:text-slate-100 active:bg-slate-800 active:text-slate-300 focus-visible:outline-slate-900  " href="https://doi.org/10.1016/j.compchemeng.2017.11.005" target="_blank">Read research article<!-- --> <span class="sr-only"> on CFD data</span><svg class="ml-3 overflow-visible" width="3" height="6" viewBox="0 0 3 6" fill="none" stroke="currentColor" stroke-width="2" stroke-linecap="round" stroke-linejoin="round"><path d="M0 0L3 3L0 6"></path></svg></a></p></p></div><div class="lg:w-1/2 w-full "><img src="/images/applications/DUO_3_alpha.png" alt="CPOX reactor temperature field" class="rounded-lg border-2 border-slate-700 w-full object-contain bg-white max-h-[300px]"/><div class="mt-4 text-xs text-slate-300"><b>Reference:</b> <!-- -->M. Hettel, E. Daymo, O. Deutschmann. 3D modeling of a CPOX-reformer including detailed chemistry and radiation effects with DUO. Computers and Chemical Engineering, 
1Vol 109 (2018) 166–178.<!-- --> <a href="https://doi.org/10.1016/j.compchemeng.2017.11.005" target="_blank" rel="noopener noreferrer" class="text-indigo-400 hover:underline">Read More</a></div></div></div></div></section></div><div class="bg-dark-blue bg-cover py-16 rounded-2xl"><section id="sofc-stack" class="scroll-mt-20"><div class="px-4 lg:px-10"><h2 class="text-4xl font-medium font-display tracking-light text-white">Solid Oxide Fuel Cell (SOFC) Stack Modeling</h2><div class="mt-12 flex flex-col lg:flex-row items-start gap-12 lg:gap-20"><div class="lg:w-1/2 space-y-4"><h3 class="font-display text-lg text-indigo-400">Modeling thermal cycling behavior in high-power density SOFC stacks</h3><p class="text-lg leading-loose text-slate-300">Simulating the start-up behavior of a 10 kWe-class high-power density metal-supported Ni-CGO/CGO/YSZ/CGO/LSCF-CGO 120-cell stack for stationary and mobile power generation. Shown is the temperature profile of the stack solid phase including a microporous silica-based insulation layer at the stack’s periphery. The model includes convective and radiative heat loss to the ambient surroundings.<p class="mb-2 mt-4 max-w-3xl md:mb-0 md:mt-6"><a class="group inline-flex items-center justify-center rounded-full py-2 px-4 text-sm  font-semibold focus:outline-none focus-visible:outline-2 focus-visible:outline-offset-2 bg-omegadot-blue-950 text-white hover:bg-slate-700 hover:text-slate-100 active:bg-slate-800 active:text-slate-300 focus-visible:outline-slate-900  " href="https://doi.org/10.1021/acsenvironau.1c00014" target="_blank">Read research article<!-- --> <span class="sr-only"> on CFD data</span><svg class="ml-3 overflow-visible" width="3" height="6" viewBox="0 0 3 6" fill="none" stroke="currentColor" stroke-width="2" stroke-linecap="round" stroke-linejoin="round"><path d="M0 0L3 3L0 6"></path></svg></a></p></p></div><div class="lg:w-1/2 w-full "><video src="/images/video/SOFC_Start-Up.mp4" controls="" autoplay="" muted="" loop="" class="rounded-lg border-2 border-slate-700 w-full object-contain bg-white max-h-[400px]"></video><div class="mt-4 text-xs text-slate-300"><b>Reference:</b> <!-- -->L. Wehrle, Y. Wang, P. Boldrin, N.P. Brandon, O. Deutschmann, A. Banerjee. Optimizing solid oxide fuel cell performance to re-evaluate its role in the mobility sector. ACS Environmental Au 2 (2022) 42-64.<!-- --> <a href="https://doi.org/10.1021/acsenvironau.1c00014" target="_blank" rel="noopener noreferrer" class="text-indigo-400 hover:underline">Read More</a></div></div></div></div></section></div><div class="bg-dark-blue bg-cover py-16 rounded-2xl"><section id="flow-field" class="scroll-mt-20"><div class="px-4 lg:px-10"><h2 class="text-4xl font-medium font-display tracking-light text-white">Flow Field Modeling (DUO)</h2><div class="mt-12 flex flex-col lg:flex-row items-start gap-12 lg:gap-20"><div class="lg:w-1/2 space-y-4"><h3 class="font-display text-lg text-indigo-400">Modeling of flow field up and downstream of a monolith</h3><p class="text-lg leading-loose text-slate-300">Two coupled flow domains using different turbulence models and numerical parameters have been solved. The pressure loss of each of the 1100 channels of the monolith (one quarter of catalyst assembly) was derived on basis of a developed laminar flow.<p class="mb-2 mt-4 max-w-3xl md:mb-0 md:mt-6"><a class="group inline-flex items-center justify-center rounded-full py-2 px-4 text-sm  font-semibold focus:outline-none focus-visible:outline-2 focus-visible:outline-offset-2 bg-omegadot-blue-950 text-white hover:bg-slate-700 hover:text-slate-100 active:bg-slate-800 active:text-slate-300 focus-visible:outline-slate-900  " href="https://doi.org/10.1016/j.cep.2019.107728" target="_blank">Read research article<!-- --> <span class="sr-only"> on CFD data</span><svg class="ml-3 overflow-visible" width="3" height="6" viewBox="0 0 3 6" fill="none" stroke="currentColor" stroke-width="2" stroke-linecap="round" stroke-linejoin="round"><path d="M0 0L3 3L0 6"></path></svg></a></p></p></div><div class="lg:w-1/2 w-full "><video src="/images/video/Automotive_catalytic_converters_3.mp4" controls="" autoplay="" muted="" loop="" class="rounded-lg border-2 border-slate-700 w-full object-contain bg-white max-h-[400px]"></video><div class="mt-4 text-xs text-slate-300"><b>Reference:</b> <!-- -->M. Hettel, E. Daymo, T. Schmidt, O. Deutschmann. CFD-Modeling of Fluid Domains with Embedded Monoliths with Emphasis on Automotive Converters. Chemical Engineering &amp; Processing: Process Intensification 147 (2020) 107728<!-- --> <a href="https://doi.org/10.1016/j.cep.2019.107728" target="_blank" rel="noopener noreferrer" class="text-indigo-400 hover:underline">Read More</a></div></div></div></div></section></div><div class="bg-dark-blue bg-cover py-16 rounded-2xl"><section id="materials-synthesis" class="scroll-mt-20"><div class="px-4 lg:px-10"><h2 class="text-4xl font-medium font-display tracking-light text-white">Materials Synthesis</h2><div class="mt-12 flex flex-col lg:flex-row items-start gap-12 lg:gap-20"><div class="lg:w-1/2 space-y-4"><h3 class="font-display text-lg text-indigo-400">Production of advanced carbon materials by pyrolysis and chemical vap
1or infiltration</h3><p class="text-lg leading-loose text-slate-300">Numerical predicted temporal development of 2d spatial of density and species concentration profiles within in carbon felts. Based on multi-step reaction and deposition models including the hydrogen inhibition model of pyrocarbon growth, transient 2D simulations of chemical vapor infiltration of methane were carried out by a finite element method (FEM).<p class="mb-2 mt-4 max-w-3xl md:mb-0 md:mt-6"><a class="group inline-flex items-center justify-center rounded-full py-2 px-4 text-sm  font-semibold focus:outline-none focus-visible:outline-2 focus-visible:outline-offset-2 bg-omegadot-blue-950 text-white hover:bg-slate-700 hover:text-slate-100 active:bg-slate-800 active:text-slate-300 focus-visible:outline-slate-900  " href="https://dx.doi.org/10.1016/j.ces.2007.01.069" target="_blank">Read research article<!-- --> <span class="sr-only"> on CFD data</span><svg class="ml-3 overflow-visible" width="3" height="6" viewBox="0 0 3 6" fill="none" stroke="currentColor" stroke-width="2" stroke-linecap="round" stroke-linejoin="round"><path d="M0 0L3 3L0 6"></path></svg></a></p></p></div><div class="lg:w-1/2 w-full "><video src="/images/video/materialSynth_bulkDensity.mp4" controls="" autoplay="" muted="" loop="" class="rounded-lg border-2 border-slate-700 w-full object-contain bg-white max-h-[400px]"></video><div class="mt-4 text-xs text-slate-300"><b>Reference:</b> <!-- -->A. Li, O. Deutschmann, Transient simulation of chemical vapor infiltration of methane using multi-step reaction and deposition models. Chemical Engineering Science 62 (2007) 4976-4982.<!-- --> <a href="https://dx.doi.org/10.1016/j.ces.2007.01.069" target="_blank" rel="noopener noreferrer" class="text-indigo-400 hover:underline">Read More</a></div></div></div></div></section></div><div class="bg-dark-blue bg-cover py-16 rounded-2xl"><section id="high-temp-catalysis" class="scroll-mt-20"><div class="px-4 lg:px-10"><h2 class="text-4xl font-medium font-display tracking-light text-white">High Temperature Catalysis</h2><div class="mt-12 flex flex-col lg:flex-row items-start gap-12 lg:gap-20"><div class="lg:w-1/2 space-y-4"><h3 class="font-display text-lg text-indigo-400">Transient behavior of partial oxidation monoliths</h3><p class="text-lg leading-loose text-slate-300">Light-off of an extruded monolith coated with rhodium as used for partial oxidation of methane to synthesis gas. A cold methane/oxygen/nitrogen mixture flows from left into the preheated cold monolith. The figures reveal the calculated temperature distribution of the monolith and the methane, hydrogen, and water concentrations within three single monolith channels after 2 and 120 seconds of reactor operation.<p class="mb-2 mt-4 max-w-3xl md:mb-0 md:mt-6"><a class="group inline-flex items-center justify-center rounded-full py-2 px-4 text-sm  font-semibold focus:outline-none focus-visible:outline-2 focus-visible:outline-offset-2 bg-omegadot-blue-950 text-white hover:bg-slate-700 hover:text-slate-100 active:bg-slate-800 active:text-slate-300 focus-visible:outline-slate-900  " href="https://doi.org/10.1016/S0009-2509(02)00589-4" target="_blank">Read research article<!-- --> <span class="sr-only"> on CFD data</span><svg class="ml-3 overflow-visible" width="3" height="6" viewBox="0 0 3 6" fill="none" stroke="currentColor" stroke-width="2" stroke-linecap="round" stroke-linejoin="round"><path d="M0 0L3 3L0 6"></path></svg></a></p></p></div><div class="lg:w-1/2 w-full "><video src="/images/video/monolith.mp4" controls="" autoplay="" muted="" loop="" class="rounded-lg border-2 border-slate-700 w-full object-contain bg-white max-h-[400px]"></video><div class="mt-4 text-xs text-slate-300"><b>Reference:</b> <!-- -->R. Schwiedernoch, S. Tischer, C. Correa, O. Deutschmann, Experimental and numerical study of transient behavior of a catalytic partial oxidation monolith. Chem. Eng. Sci. 58, 633-642 (2003)<!-- --> <a href="https://doi.org/10.1016/S0009-2509(02)00589-4" target="_blank" rel="noopener noreferrer" class="text-indigo-400 hover:underline">Read More</a></div></div></div></div></section></div><div class="bg-dark-blue bg-cover py-16 rounded-2xl"><section id="automotive-converters" class="scroll-mt-20"><div class="px-4 lg:px-10"><h2 class="text-4xl font-medium font-display tracking-light text-white">Automotive Catalytic Converters</h2><div class="mt-12 flex flex-col lg:flex-row items-start gap-12 lg:gap-20"><div class="lg:w-1/2 space-y-4"><h3 class="font-display text-lg text-indigo-400">Simulation of the thermal behavior of a three-way catalyst during a driving test</h3><p class="text-lg leading-loose text-slate-300">Light-off of an extruded monolith coated with rhodium as used for partial oxidation of methane to synthesis gas. A cold methane/oxygen/nitrogen mixture flows from left into the preheated cold monolith. The figures reveal the calculated temperature distribution of the monolith and the methane, hydrogen, and water concentrations within three single monolith channels after 2 and 120 seconds of reactor operation.<p class="mb-2 mt-4 max-w-3xl md:mb-0 md:mt-6"><a class="group inline-flex items-center justify-center rounded-full py-2 px-4 text-sm  font-semibold focus:outline-none focus-visible:outline-2 focus-visible:outline-offset-2 bg-omegadot-blue-950 text-white hover:bg-slate-700 hover:text-slate-100 active:bg-slate-800 active:text-slate-300 focus-visible:outline-slate-900  " href="https://doi.org/10.4271/2002-01-0065" target="_blank">Read research article<!-- --> <span class="sr-only"> on CFD data</span><svg class="ml-3 overflow-visible" width="3" height="6" viewBox="0 0 3 6" fill="none" stroke="currentColor" stroke-width="2" stroke-linecap="round" stroke-linejoin="round"><path d="M0 0L3 3L0 6"></path></svg></a></p></p></div><div class="lg:w-1/2 w-full "><video src="/images/video/monolith3dTemp.mp4" controls="" autoplay="" muted="" loop="" class="rounded-lg border-2 border-slate-700 w-full object-contain bg-white max-h-[400px]"></video><div class="mt-4 text-xs text-slate-300"><b>Reference:</b> <!-- -->J. Braun, T. Hauber, H. Többen, J. Windmann, P. Zacke, D. Chatterjee, C. Correa, O. Deutschmann, L. Maier, S. Tischer, J. Warnatz, Three dimensional simulation of transient behavior of a three-way catalytic converter. SAE Technical paper 2002-01-0065 (2022)<!-- --> <a href="https://doi.org/10.4271/2002-01-0065" target="_blank" rel="noopener noreferrer" class="text-indigo-400 hover:underline">Read More</a></div></div></div></div></section></div></div><aside></aside></div></div></main><link rel="modulepreload" href="/assets/entry.client-CuPkAkn2.js"/><link rel="modulepreload" href="/assets/jsx-runtime-0DLF9kdB.js"/><link rel="modulepreload" href="/assets/index-DZ2NVNxh.js"/><link rel="modulepreload" href="/assets/index-CozwGv7F.js"/><link rel="modulepreload" href="/assets/index-mOcIQiaR.js"/><link rel="modulepreload" href="/assets/components-n0rGSRfK.js"/>
1<link rel="modulepreload" href="/assets/clsx-B-dksMZM.js"/><link rel="modulepreload" href="/assets/popover-AS_dDAPc.js"/><link rel="modulepreload" href="/assets/ArrowTopRightOnSquareIcon-CdA6bV5k.js"/><link rel="modulepreload" href="/assets/use-sync-refs-BOW_1FfR.js"/><link rel="modulepreload" href="/assets/use-tab-direction-3TMkarUv.js"/><link rel="modulepreload" href="/assets/dom-BlW_0b_t.js"/><link rel="modulepreload" href="/assets/use-resolve-button-type-D5_JmXkw.js"/><link rel="modulepreload" href="/assets/root-DSJUn5QQ.js"/><link rel="modulepreload" href="/assets/Button-BVSNHnSF.js"/><link rel="modulepreload" href="/assets/applications-DJij5uGb.js"/>
1<script>window.__remixContext = {"basename":"/","future":{"v3_fetcherPersist":true,"v3_relativeSplatPath":true,"v3_throwAbortReason":true,"v3_routeConfig":false,"v3_singleFetch":true,"v3_lazyRouteDiscovery":true,"unstable_optimizeDeps":false},"isSpaMode":false};window.__remixContext.stream = new ReadableStream({start(controller){window.__remixContext.streamController = controller;}}).pipeThrough(new TextEncoderStream());</script>
1<script type="module" async="">;
2import * as route0 from "/assets/root-DSJUn5QQ.js";
3import * as route1 from "/assets/applications-DJij5uGb.js";
4window.__remixManifest = {
5  "entry": {
6    "module": "/assets/entry.client-CuPkAkn2.js",
7    "imports": [
8      "/assets/jsx-runtime-0DLF9kdB.js",
9      "/assets/index-DZ2NVNxh.js",
10      "/assets/index-CozwGv7F.js",
11      "/assets/index-mOcIQiaR.js",
12      "/assets/components-n0rGSRfK.js"
13    ],
14    "css": []
15  },
16  "routes": {
17    "root": {
18      "id": "root",
19      "path": "",
20      "hasAction": false,
21      "hasLoader": false,
22      "hasClientAction": false,
23      "hasClientLoader": false,
24      "hasErrorBoundary": false,
25      "module": "/assets/root-DSJUn5QQ.js",
26      "imports": [
27        "/assets/jsx-runtime-0DLF9kdB.js",
28        "/assets/index-DZ2NVNxh.js",
29        "/assets/index-CozwGv7F.js",
30        "/assets/index-mOcIQiaR.js",
31        "/assets/components-n0rGSRfK.js",
32        "/assets/clsx-B-dksMZM.js",
33        "/assets/popover-AS_dDAPc.js",
34        "/assets/ArrowTopRightOnSquareIcon-CdA6bV5k.js",
35        "/assets/use-sync-refs-BOW_1FfR.js",
36        "/assets/use-tab-direction-3TMkarUv.js",
37        "/assets/dom-BlW_0b_t.js",
38        "/assets/use-resolve-button-type-D5_JmXkw.js"
39      ],
40      "css": []
41    },
42    "routes/applications": {
43      "id": "routes/applications",
44      "parentId": "root",
45      "path": "applications",
46      "hasAction": false,
47      "hasLoader": false,
48      "hasClientAction": false,
49      "hasClientLoader": false,
50      "hasErrorBoundary": false,
51      "module": "/assets/applications-DJij5uGb.js",
52      "imports": [
53        "/assets/jsx-runtime-0DLF9kdB.js",
54        "/assets/clsx-B-dksMZM.js",
55        "/assets/index-DZ2NVNxh.js",
56        "/assets/Button-BVSNHnSF.js"
57      ],
58      "css": []
59    },
60    "routes/_index": {
61      "id": "routes/_index",
62      "parentId": "root",
63      "index": true,
64      "hasAction": false,
65      "hasLoader": false,
66      "hasClientAction": false,
67      "hasClientLoader": false,
68      "hasErrorBoundary": false,
69      "module": "/assets/_index-j6pfPeXl.js",
70      "imports": [
71        "/assets/jsx-runtime-0DLF9kdB.js",
72        "/assets/clsx-B-dksMZM.js",
73        "/assets/index-DZ2NVNxh.js",
74        "/assets/popover-AS_dDAPc.js",
75        "/assets/Button-BVSNHnSF.js",
76        "/assets/use-sync-refs-BOW_1FfR.js",
77        "/assets/use-resolve-button-type-D5_JmXkw.js",
78        "/assets/use-tab-direction-3TMkarUv.js",
79        "/assets/dom-BlW_0b_t.js",
80        "/assets/index-CozwGv7F.js"
81      ],
82      "css": [
83        "/assets/_index-CT0VjEgY.css"
84      ]
85    }
86  },
87  "url": "/assets/manifest-68d045ba.js",
88  "version": "68d045ba"
89};
90window.__remixRouteModules = {"root":route0,"routes/applications":route1};
91
92import("/assets/entry.client-CuPkAkn2.js");</script>
92<footer class="mx-auto w-full px-6 pb-8 lg:px-8 "><div class="border-t border-gray-900/10 pt-8  "><div class="mx-auto max-w-7xl flex flex-row justify-between px-4 lg:px-16"><p class="text-sm/6 text-gray-600">omegadot software &amp; consulting GmbH</p><p class="text-sm/6 text-gray-600 flex gap-8"><a href="/imprint" class="hover:underline">Imprint</a><a href="/privacy" class="hover:underline">Privacy</a></p></div></div></footer>
92<script type="module" src="https://static.cloudflareinsights.com/beacon.min.js/v31edd6df95cf4e85bb4c19e7a9bdbcba1788362987495" integrity="sha512-iIg7k2xntmwu6/uSb5tpc/hySgZc4eoL31yB29W6tJFo2akwjPWcEqnCEdJvGexCL0KEQwVYv5BlowfhVz26hg==" data-cf-beacon='{"version":"2024.11.0","token":"b6cffa74d32942b2bf7feaa9b650ef5d","r":1,"spa":2}' crossorigin="anonymous"></script>
92
93</body></html><!--$-->
93<script>window.__remixContext.streamController.enqueue("[{\"_1\":2,\"_5\":-5,\"_6\":-5},\"loaderData\",{\"_3\":-5,\"_4\":-5},\"root\",\"routes/applications\",\"actionData\",\"errors\"]\n");</script>
93<!--$-->
93<script>window.__remixContext.streamController.close();</script>
93<!--/$--><!--/$-->

Line numbers count LF bytes from the start of the resource, as the search results do. Vendor segments are library code the classifier recognised; they are stored but not indexed. Bytes are shown as Latin1 characters, one per byte.