Catalytic synthesis of glycerol monoacetate using a continuous expanded bed column reactor packed with cation-exchange resin

Industrial and Engineering Chemistry Research

Volumn 48, Issue 4, 2009, Pages 1816-1823

  Fukumura, Takuya ^a   Toda, Takuji ^b   Seki, Yuichiro ^b   Kubo, Masaki ^b   Shibasaki Kitakawa, Naomi ^b   Yonemoto, Toshikuni ^b  

^a ICHINOSEKI NATIONAL COLLEGE OF TECHNOLOGY   (Japan)

^b TOHOKU UNIVERSITY   (Japan)

Author keywords

[No Author keywords available]

Indexed keywords

ACETIC ACID; ACIDS; CATALYST ACTIVITY; ELECTRIC NETWORK ANALYSIS; ESTERIFICATION; ESTERS; FLUID DYNAMICS; GLYCEROL; ION EXCHANGE RESINS; PH EFFECTS; POSITIVE IONS;

AMBERLYST; BATCH REACTIONS; BATCH SYSTEMS; BED HEIGHTS; CATALYTIC REACTIONS; CATALYTIC RESINS; CATALYTIC SYNTHESIS; CATION-EXCHANGE RESINS; COLUMN REACTORS; CONTINUOUS PRODUCTIONS; CONTINUOUS REACTORS; ESTERIFICATION REACTIONS; EXPANDED BEDS; EXPERIMENTAL DATUM; HETEROGENEOUS CATALYTIC REACTIONS; INTRAPARTICLE; KINETIC MODELS; MASS-TRANSFER RESISTANCES; NUMERICAL CALCULATIONS; OPTIMUM OPERATING CONDITIONS; REACTIVE FLUIDS; TRANSPORT MODELS; TRIACETIN;

CATALYSIS;

EID: 61649099591     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie800625g     Document Type: Article

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