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Thermal/catalytic cracking of hydrocarbons for the production of olefins; a state-of-the-art review III: Process modeling and simulation
Ethylene and propylene are among the light olefins which are the main building blocks in
the petrochemical and chemical industry. They are produced from thermal/catalytic cracking …
the petrochemical and chemical industry. They are produced from thermal/catalytic cracking …
Sustainable innovations in steam cracking: CO 2 neutral olefin production
Steam cracking of hydrocarbons is and will continue to be the main industrial process to
produce light olefins in the coming decades. In state of the art steam cracking plants more …
produce light olefins in the coming decades. In state of the art steam cracking plants more …
State-of-the-art of coke formation during steam cracking: Anti-coking surface technologies
SH Symoens, N Olahova… - Industrial & …, 2018 - ACS Publications
Although steam cracking is a mature technology, mitigation of coke formation remains one of
the main challenges in the petrochemical industry. To increase the olefin output of existing …
the main challenges in the petrochemical industry. To increase the olefin output of existing …
Knowledge expression, numerical modeling and optimization application of ethylene thermal cracking: From the perspective of intelligent manufacturing
Applications of process systems engineering (PSE) in plants and enterprises are boosting
industrial reform from automation to digitization and intelligence. For ethylene thermal …
industrial reform from automation to digitization and intelligence. For ethylene thermal …
Dynamic simulation of fouling in steam cracking reactors using CFD
LA Vandewalle, DJ Van Cauwenberge… - Chemical Engineering …, 2017 - Elsevier
Recently computational fluid dynamics (CFD) has been successfully applied for the
evaluation of the start-of-run performance of three-dimensional (3D) coil geometries in …
evaluation of the start-of-run performance of three-dimensional (3D) coil geometries in …
CatchyFOAM: Euler–Euler CFD simulations of fluidized bed reactors with microkinetic modeling of gas-phase and catalytic surface chemistry
Whereas detailed kinetic models have already been implemented widely in computational
fluid dynamics (CFD) simulations of gas-phase processes, CFD modeling of reactive gas …
fluid dynamics (CFD) simulations of gas-phase processes, CFD modeling of reactive gas …
Combined catalytic and pyrolytic coking model for steam cracking of hydrocarbons
Coke formation during steam cracking of gas and liquid feedstocks comprises a catalytic
coke formation phase followed by a pyrolytic coke formation phase. At present, only a very …
coke formation phase followed by a pyrolytic coke formation phase. At present, only a very …
Large eddy simulation of tubular reactors with spherical dimples
JN Dedeyne, DJ Van Cauwenberge… - Chemical Engineering …, 2020 - Elsevier
Spherical dimples are implemented in heat exchanger channels to enhance heat transfer at
a low pressure drop penalty. This combination of enhanced heat transfer and low pressure …
a low pressure drop penalty. This combination of enhanced heat transfer and low pressure …
Computational fluid dynamics‐based optimization of dimpled steam cracking reactors for reduced CO2 emissions
JN Dedeyne, M Geerts, PA Reyniers, F Wéry… - AIChE …, 2020 - Wiley Online Library
Spherical dimples in cylindrical tubes enhance heat transfer and lead to a more uniform
radial temperature profile. To combine these positive properties with a low pressure drop, a …
radial temperature profile. To combine these positive properties with a low pressure drop, a …
Continuous synthesis of 1‐ethoxy‐2, 3‐difluoro‐4‐iodo‐benzene in a microreactor system and the Gaussian and computational fluid dynamics simulations
Q Chen, S **a, Y Wang, G Luo, H Shang… - AIChE Journal, 2021 - Wiley Online Library
A microreactor system consisting of membrane‐dispersion tube‐in‐tube microreactors and
delay loops was developed for the continuous synthesis of 1‐ethoxy‐2, 3‐difluoro‐4‐iodo …
delay loops was developed for the continuous synthesis of 1‐ethoxy‐2, 3‐difluoro‐4‐iodo …