Steady state simulation of a packed bed reactor for the partial oxidation of methanol to formaldehyde. Influence of diffusional phenomena and catalyst activity distribution within the pellets

被引：0

作者：

Gonzo, E.E. ^{[1
]}

Gottifredi, J.C. ^{[1
]}

机构：

[1] Universidad Nacional de Salta, Salta, Argentina

来源：

Chemical Engineering Communications | 1998年 / 168卷

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引用

页码：127 / 143

共 11 条

[1] Steady state simulation of a packed bed reactor for the partial oxidation of methanol to formaldehyde. Influence of diffusional phenomena and catalyst activity distribution within the pellets
Gonzo, EE
Gottifredi, JC
CHEMICAL ENGINEERING COMMUNICATIONS, 1998, 168 : 127 - 143
[2] STEADY-STATE AND DYNAMIC MODELING OF A PACKED-BED REACTOR FOR THE PARTIAL OXIDATION OF METHANOL TO FORMALDEHYDE .1. MODEL DEVELOPMENT
WINDES, LC
SCHWEDOCK, MJ
RAY, WH
CHEMICAL ENGINEERING COMMUNICATIONS, 1989, 78 : 1 - 43
[3] Catalytic oxidation of methanol to formaldehyde: an example of kinetics with transport phenomena in a packed-bed reactor
Tesser, R
Di Serio, M
Santacesaria, E
CATALYSIS TODAY, 2003, 77 (04) : 325 - 333
[4] STEADY-STATE AND DYNAMIC MODELING OF A PACKED-BED REACTOR FOR THE PARTIAL OXIDATION OF METHANOL TO FORMALDEHYDE .2. EXPERIMENTAL RESULTS COMPARED WITH MODEL PREDICTIONS
SCHWEDOCK, MJ
WINDES, LC
RAY, WH
CHEMICAL ENGINEERING COMMUNICATIONS, 1989, 78 : 45 - 71
[5] Modeling and Simulation of Partial Oxidation of Methanol to Formaldehyde on FeO/MoO3 Catalyst in a Catalytic Fixed Bed Reactor
Olatunde, Abayomi Olaniyi
Olafadehan, Olaosebikan Abidoye
Usman, Moham Awwal
IRANIAN JOURNAL OF CHEMISTRY & CHEMICAL ENGINEERING-INTERNATIONAL ENGLISH EDITION, 2021, 40 (06): : 1800 - 1813
[6] Simulation of coke and metal deposition in catalyst pellets using a non-steady state fixed bed reactor model
Vogelaar, Bas M.
Berger, Rob J.
Bezemer, Bas
Janssens, Jean-Paul
van Langeveld, A. Dick
Eijsbouts, Sonja
Moulijn, Jacob A.
CHEMICAL ENGINEERING SCIENCE, 2006, 61 (22) : 7463 - 7478
[7] Experiment of catalyst activity distribution effect on methanol steam reforming performance in the packed bed plate-type reactor
Wang, Guoqiang
Wang, Feng
Li, Longjian
Zhang, Guofu
ENERGY, 2013, 51 : 267 - 272
[8] Simulation studies of the hydrogen production from methanol partial oxidation steam reforming by a tubular packed-bed catalytic reactor
Jiang, YL
Lim, MS
Kim, DH
CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2001, 9 (03) : 297 - 305
[9] Simulation Studies of the Hydrogen Production from Methanol Partial Oxidation Steam Reforming by a Tubular Packed-bed Catalytic Reactor
蒋元力
林美淑
金东显
ChineseJournalofChemicalEngineering, 2001, (03) : 73 - 81
[10] Modeling the Partial Oxidation of o-Xylene in an Industrial Packed-Bed Catalytic Reactor: The Role of Hydrodynamics and Catalyst Activity in the Heat Transport
Castillo-Araiza, C. O.
Lopez-Isunza, F.
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (15) : 6845 - 6853

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