A techno-economic comparison of various process options for the production of 1,1-diethoxy butane

Journal of Chemical Technology and Biotechnology

Volumn 87, Issue 7, 2012, Pages 943-954

  Agirre, Ion ^a,b   Güemez, María Belén ^a   Motelica, Anatolie ^b   van Veen, Henk M ^b   Vente, Jaap F ^b   Arias, Pedro L ^a  

^a UNIVERSITY OF THE BASQUE COUNTRY UPV EHU   (Spain)

^b TNO   (Netherlands)

Author keywords

Acetal; Biodiesel; HybSi; Membrane separation; Modeling

Indexed keywords

ACETAL; ENERGY DEMANDS; EXPERIMENTAL DATA; HYBSI; IN-SITU; MEMBRANE AREA; MEMBRANE MODULE; MEMBRANE PROCESS; MEMBRANE SEPARATION; MEMBRANE-BASED PROCESS; PERVAPORATION MEMBRANES; REACTION MIXTURE; REACTIVE DISTILLATIONS; RECYCLE RATE; TECHNO-ECONOMICS; TUBULAR REACTORS; UNIT DIMENSION; WATER REMOVAL;

ALDEHYDES; BIODIESEL; BIOREACTORS; BUTANE; DEHYDRATION; DEWATERING; DISTILLATION COLUMNS; ENERGY MANAGEMENT; MODELS; PERVAPORATION; REACTION RATES; RECYCLING;

MEMBRANES;

1,1 DIETHOXY BUTANE; ACETAL; BIODIESEL; CHEMICAL COMPOUND; UNCLASSIFIED DRUG;

ARTICLE; BIOFUEL PRODUCTION; CONTROLLED STUDY; DISTILLATION; INTERMETHOD COMPARISON; MEMBRANE REACTOR; MODEL;

EID: 84862229934     PISSN: 02682575     EISSN: 10974660     Source Type: Journal    
DOI: 10.1002/jctb.3704     Document Type: Article

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