Simulation and kinetic study of transesterification of triolein to biodiesel using modular reactors

Chemical Engineering Journal

Volumn 207-208, Issue , 2012, Pages 285-298

  Portha, J F ^a   Allain, F ^a   Coupard, V ^b   Dandeu, A ^b   Girot, E ^a   Schaer, E ^a   Falk, L ^a  

^a UNIVERSITÉ DE LORRAINE   (France)

^b IFP ENERGIES NOUVELLES   (France)

Author keywords

D; DGE; E; Finite volume method; G; Heterogeneous catalytic reactors; IFPEn; Intensification; M; MeG; MeOH; Series and parallel reversible reactions; T; Transesterification of biodiesel; W

Indexed keywords

CATALYTIC REACTOR; DGE; E; G; IFPEN; INTENSIFICATION; M; MEG; MEOH; REVERSIBLE REACTION; T;

BIODIESEL; CATALYSTS; DEUTERIUM; ENERGY UTILIZATION; FINITE VOLUME METHOD; KINETICS; MASS TRANSFER; METHANOL; REACTION RATES; TUNGSTEN; VEGETABLE OILS;

TRANSESTERIFICATION;

EID: 84866876044     PISSN: 13858947     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.cej.2012.06.106     Document Type: Article

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