Engineering a Nickel–Oxygen Vacancy Interface for Enhanced Dry Reforming of Methane: A Promoted Effect of CeO2 Introduction into Ni/MgO

X Ding, Y Yang, Z Li, P Huang, X Liu, Y Guo… - ACS …, 2023 - ACS Publications
Nickel, the most commonly used active metal for the dry reforming of methane (DRM), often
encounters the challenge of severe deactivation due to sintering and carbon deposition. In …

The mathematical catalyst deactivation models: a mini review

ZM Shakor, EN Al-Shafei - RSC advances, 2023 - pubs.rsc.org
Catalyst deactivation is a complex phenomenon and identifying an appropriate deactivation
model is a key effort in the catalytic industry and plays a significant role in catalyst design …

[HTML][HTML] Cracking of plastic pyrolysis oil over FCC equilibrium catalysts to produce fuels: Kinetic modeling

R Palos, E Rodríguez, A Gutierrez, J Bilbao… - Fuel, 2022 - Elsevier
The kinetics of the catalytic cracking of plastic pyrolysis oil (PPO) over three FCC (fluid
catalytic cracking) equilibrium commercial catalysts has been modeled. The PPO comes …

Fuel production by cracking of polyolefins pyrolysis waxes under fluid catalytic cracking (FCC) operating conditions

E Rodríguez, A Gutiérrez, R Palos, FJ Vela… - Waste management, 2019 - Elsevier
The catalytic cracking of high–density polyethylene pyrolysis waxes under fluidized catalytic
cracking conditions has been investigated with the aim of producing fuels at large–scale …

Estimation of catalytic cracking of vacuum gas oil by ZSM-5-and β-zeolite-containing two-layered and novel three-layered hierarchical catalysts using Curie point …

T Yoshimura, S Tanaka, N Matsuda… - Journal of Analytical and …, 2024 - Elsevier
Abstract ZSM-5-and β-zeolite-containing two-layered hierarchical catalysts (2 LZ and 2 L-β)
were prepared using a template of malic acid and novel three-layered hierarchical catalysts …

Kinetic modeling for the catalytic cracking of tires pyrolysis oil

R Palos, E Rodríguez, A Gutiérrez, J Bilbao… - Fuel, 2022 - Elsevier
The parameters of a 6-lump kinetic model for the catalytic cracking of tire pyrolysis oil (TPO)
in conditions of the industrial fluid catalytic cracking (FCC) unit have been computed. The …

Adaptive data dimensionality reduction for chemical process modeling based on the information criterion related to data association and redundancy

L Luo, G He, C Chen, X Ji, L Zhou, Y Dai… - Industrial & …, 2022 - ACS Publications
Chemical process modeling is the basis for research and applications in related fields. With
the development of industrial informatization, data-driven process modeling techniques are …

Upgrading of heavy coker naphtha by means of catalytic cracking in refinery FCC unit

R Palos, A Gutiérrez, ML Fernández, D Trueba… - Fuel processing …, 2020 - Elsevier
The upgrading of heavy coker naphtha under conditions of the industrial fluid catalytic
cracking (FCC) unit has been investigated, with the aim of obtaining light olefins and a …

A detailed reaction kinetic model of heavy naphtha reforming

ZM Shakor, AA AbdulRazak, KA Sukkar - Arabian Journal for Science and …, 2020 - Springer
A detailed reaction kinetic model was developed to describe heavy naphtha reforming
reactions. The kinetic model involved 32 lumps and 132 reactions; the lumps were one to 11 …

Multi-objective optimization strategy for industrial catalytic cracking units: Kinetic model and enhanced SPEA-2 algorithm with economic, CO2, and SO2 emission …

L Wan, K Deng, X Li, L Zhao, J Long - Chemical Engineering Science, 2023 - Elsevier
The multi-objective optimization of the economics and environmental protection of the
fluidized catalytic cracking reaction-regeneration (FCC-RR) process can achieve a balanced …