Two-stage equilibrium model applicable to the wide range of operating conditions in entrained-flow coal gasifiers

Fuel

Volumn 89, Issue 12, 2010, Pages 3901-3910

  Nguyen, Thanh D B ^a   Lim, Young Il ^a   Song, Byung Ho ^b   Kim, Si Moon ^c   Joo, Yong Jin ^c   Ahn, Dal Hong ^c  

^a Hankyong National University   (South Korea)

^b Kunsan National University   (South Korea)

^c Korea Electric Power Research Institute (KEPRI)   (South Korea)

Author keywords

Carbon conversion; Coal gasification; Entrained flow gasifier; Equilibrium model; Product gas composition

Indexed keywords

CARBON CONVERSIONS; COAL GASIFIERS; ENTRAINED FLOW; ENTRAINED FLOW GASIFIERS; EQUILIBRIUM MODELS; EQUILIBRIUM REACTIONS; EXPERIMENTAL DATA; GAS-PHASE REACTIONS; GASIFIERS; OPERATING CONDITION; PRODUCT GAS; SOLID GAS REACTION; TOTAL YIELD; TWO STAGE; WATER CONSUMPTION;

CARBONIZATION; COAL GASIFICATION; COAL GASIFICATION PLANTS; COAL INDUSTRY; EXPONENTIAL FUNCTIONS; GAS GENERATORS; GAS PRODUCERS; GASES; OXYGEN; PHASE INTERFACES; WATER SUPPLY;

COAL;

EID: 77956614838     PISSN: 00162361     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.fuel.2010.06.044     Document Type: Article

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