Cordero-Lanzac et al., 2020 - Google Patents
A comprehensive approach for designing different configurations of isothermal reactors with fast catalyst deactivationCordero-Lanzac et al., 2020
View PDF- Document ID
- 18251231346267660106
- Author
- Cordero-Lanzac T
- Aguayo A
- Gayubo A
- Castaño P
- Bilbao J
- Publication year
- Publication venue
- Chemical Engineering Journal
External Links
Snippet
A methodology for simulating the performance of different reactor configurations for processes with complex reaction networks and fast catalyst deactivation has been proposed. These reaction configurations are: packed bed, moving bed and fluidized bed reactors with …
- 239000003054 catalyst 0 title abstract description 145
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00026—Controlling or regulating the heat exchange system
- B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Cordero-Lanzac et al. | A comprehensive approach for designing different configurations of isothermal reactors with fast catalyst deactivation | |
| Ye et al. | MTO processes development: the key of mesoscale studies | |
| Ying et al. | A seven lumped kinetic model for industrial catalyst in DMTO process | |
| Cordero-Lanzac et al. | Simultaneous modeling of the kinetics for n-pentane cracking and the deactivation of a HZSM-5 based catalyst | |
| Yuan et al. | Comparative study of MTO kinetics over SAPO-34 catalyst in fixed and fluidized bed reactors | |
| Li et al. | Deactivation kinetics with activity coefficient of the methanol to aromatics process over modified ZSM-5 | |
| Cordero-Lanzac et al. | Reactor–regenerator system for the dimethyl ether-to-olefins process over HZSM-5 catalysts: Conceptual development and analysis of the process variables | |
| Jiang et al. | Methanol to propylene process in a moving bed reactor with byproducts recycling: kinetic study and reactor simulation | |
| Kaarsholm et al. | Kinetic modeling of methanol-to-olefin reaction over ZSM-5 in fluid bed | |
| Cordero-Lanzac et al. | Consideration of the activity distribution using the population balance theory for designing a dual fluidized bed reactor-regenerator system. Application to the MTO process | |
| Huang et al. | A computationally efficient multi-scale simulation of a multi-stage fixed-bed reactor for methanol to propylene reactions | |
| Du et al. | Equivalent reactor network model for the modeling of fluid catalytic cracking riser reactor | |
| Jin et al. | Single-event kinetic modeling of ethene oligomerization on ZSM-5 | |
| Du et al. | Experimental and computational fluid dynamics investigations of light alkane dehydrogenation in a fluidized bed reactor | |
| Chen et al. | Prediction of molecular distribution and temperature profile of FCC process through molecular-level kinetic modeling | |
| Zhu et al. | Application of machine learning to process simulation of n-pentane cracking to produce ethylene and propene | |
| Wang et al. | Lumps and kinetics for the secondary reactions in catalytically cracked gasoline | |
| Zergani et al. | Modeling and simulation analysis of methanol conversion to olefins (MTO): A critical comparison of a honeycomb monolith and a fixed-bed of cylindrical extruded HZSM-5 catalyst | |
| Zhang et al. | CFD simulation of an industrial MTO fluidized bed by coupling a population balance model of coke content | |
| Zapater et al. | Temperature and dilution effects on MTO process with a SAPO-34-based catalyst in fluidized bed reactor | |
| Li et al. | Study of Catalyst Coke Distribution Based on Population Balance Theory: Application to Methanol to Olefins Process. | |
| Vicente et al. | Dual-cycle-based lumped kinetic model for methanol-to-aromatics (MTA) reaction over H-ZSM-5 zeolites of different Si/Al ratio | |
| Polovina et al. | Modeling a reaction section of a commercial continuous catalytic reformer | |
| Du et al. | Ten-lump kinetic model for the two-stage riser catalytic cracking for maximizing propylene yield (TMP) process | |
| Zhang et al. | Kinetic perspective on methanol to propylene process via HZSM-5 catalyst: balancing between reaction and diffusion |