Influence of a reaction mixture streamline on partial oxidation of methane in an asymmetric microchannel reactor

International Journal of Hydrogen Energy

Volumn 39, Issue 1, 2014, Pages 325-330

  Vorontsov, V A ^a   Gribovskiy, A G ^b,c   Makarshin, L L ^c   Andreev, D V ^c   Ylianitsky, V Y ^d   Parmon, V N ^b,c  

^a NOVOSIBIRSK STATE TECHNICAL UNIVERSITY   (Russian Federation)

^b NOVOSIBIRSK STATE UNIVERSITY   (Russian Federation)

^c BORESKOV INSTITUTE OF CATALYSIS   (Russian Federation)

^d LAVRENTYEV INSTITUTE OF HYDRODYNAMICS   (Russian Federation)

Author keywords

Catalytic microreactor; Hydrogen production; Microchannel plate; Partial oxidation of methane; Syngas

Indexed keywords

CONVERSION OF METHANES; HYDROGEN PRODUCTION RATE; INLET CONFIGURATION; MICRO CHANNEL PLATE; MICRO CHANNEL REACTORS; MICRO-REACTOR; PARTIAL OXIDATION OF METHANE; SYN-GAS;

CARBON DIOXIDE; CARBON MONOXIDE; CATALYTIC OXIDATION; CHEMICAL REACTORS; HYDROGEN PRODUCTION; INLET FLOW; INTAKE SYSTEMS; MICROCHANNELS; OXIDATION; SYNTHESIS GAS;

METHANE;

EID: 84890383939     PISSN: 03603199     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.ijhydene.2013.10.040     Document Type: Article

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