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grants TÁMOP 4.2.1/B-09/1/KONV-2010-0003 and TÁMOP-4.2.2/A-11/1/KONV-2012-0072 greatly acknowledged for the financial support.\nResearch Institute of Chemical and Process Engineering, University of Pannonia, Egyetem u. 10, Veszprém, H-8200, Hungary \n MOL Institutional Department Hydrocarbon and Coal Processing, University of Pannonia, Egyetem u. 10, Veszprém, H-8200, Hungary \n Department of Energy, Power Engineering and Environment, University of Zagreb, Ivana Lucica 5, Zagreb, HR-10002, Croatia \n Centre of Process Integration (CPI), Research Institute of Chemical and Process Engineering, University of Pannonia, Egyetem u. 10, Veszprém, H-8200, Hungary \n Cited By :23 \n Export Date: 1 September 2021 \n CODEN: CENPE \n Correspondence Address: Nagy, E.; Research Institute of Chemical and Process Engineering, University of Pannonia, Egyetem u. 10, Hungary \n Funding details: TÁMOP 4.2.1/B-09/1/KONV-2010-0003 \n Funding text 1: The National Development Agency grants TÁMOP 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Pervaporation, being a membrane separation process, is a promising alternative process to distillation. A detailed analysis was performed considering the energy demand of concentration of ethanol solution obtained during fermentation up to the fuel-grade quality applying both hydrophilic and hydrophobic membranes. It was also discussed how the specific energy demand of the process varies during the pervaporation process and how energy consumption can be reduced applying pervaporation process with different operating modes. It was stated that standalone pervaporation process can provide fuel-grade quality biofuel at very high separation coefficient, only, using consecutively switched hydrophobic and hydrophilic membranes. Three-stage pervaporation process is needed at separation coefficient of 50, and two-stage one at separation coefficient of 100 to achieve the desired quality. Application of a hybrid process with lower membrane separation coefficient can give the desired quality by lower energy than that the distillation alone. Thus, the hybrid process can provide saving of essential amount of energy comparing it with the energy demand of distillation. However, the commercially available membrane, at present, has not the desired selectivity for replacing, at least partly, the distillation. © 2015 Elsevier B.V.", "subjects" : [ { "otype" : "Classification", "mtid" : 11082, "link" : "/api/classification/11082", "label" : "Egyéb műszaki tudományok és technológiák", "published" : true, "snippet" : true }, { "otype" : "Classification", "mtid" : 10799, "link" : "/api/classification/10799", "label" : "Egyéb természettudományok", "published" : true, "snippet" : true }, { "otype" : "Classification", "mtid" : 10293, "link" : "/api/classification/10293", "label" : "Kémiai tudományok", "published" : true, "snippet" : true }, { "otype" : "Classification", "mtid" : 11927, "link" : "/api/classification/11927", "label" : "Környezetmérnöki tudományok", "published" : true, "snippet" : true }, { "otype" : "Classification", "mtid" : 11021, "link" : "/api/classification/11021", "label" : "Vegyészmérnöki tudományok", "published" : true, "snippet" : true } 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