Heterogeneous reactor modeling for simulation of catalytic oxidation and steam reforming of methane

Chemical Engineering Science

Volumn 56, Issue 2, 2001, Pages 641-649

  Avci, A K ^a   Trimm, D L ^b   Ilsen Onsan Z ^a  

^a BOGAZICI UNIVERSITY   (Turkey)

^b UNIVERSITY OF NEW SOUTH WALES   (Australia)

Author keywords

Autothermal operation; Dual catalyst; Fixed bed reactor; Methane oxidation; Methane steam reforming; Reactor simulation

Indexed keywords

CATALYSIS; CATALYST ACTIVITY; COMPUTER SIMULATION; ELECTRIC REACTORS; HYDROGEN; METHANE; MODELS; OXIDATION; REFORMING REACTIONS; STEAM;

HETEROGENEOUS REACTOR MODELING;

CHEMICAL ENGINEERING;

CHEMICAL REACTOR; METHANE; OXIDATION; STEAM REFORMING;

EID: 0035030116     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0009-2509(00)00271-2     Document Type: Article

References (18)

1. 2
2. Simulation of the catalytic partial oxidation of methane to synthesis gas
3. Selection of catalysts and reactors for hydroprocessing
4. Production of syngas by direct catalytic oxidation of methane
5. On-board generation of hydrogen-rich goseous fuels - a review
6. 2 mixtures over a nickel containing catalyst
7. Alternative catalyst bed configurations for the autothermic conversion of methane to hydrogen
8. The design and testing of an autothermal reactor for the conversion of light hydrocarbons to hydrogen I. The kinetics of the catalytic oxidation of light hydrocarbons
9. New catalytic routes for syngas and hydrogen production
10. Thermodynamic investigation of hydrogen production by steam-methane reforming
11. Catalysis for the control of coking during steam reforming
12. Methane steam reforming, methanation and water-gas shift: I. Intrinsic kinetics
13. Methane steam reforming: II. Diffusional limitations and reactor simulation