PP-15CaO AND Al 2 O 3 SUPPORT SOLID CATALYSTS FOR BIODIESELPRODUCTIONAna P. Dias 1 , Jaime Puna 2 , João Gomes 2,3 , M. Joana Correia 4 , João Bordado 31 ICEMS, Instituto Superior Técnico (IST-UTL), Lisboa, Portugal, apsoares@ist.utl.pt2 Instituto Superior de Engenharia de Lisboa, Lisboa, Portugal, jpuna@deq.isel.ipl.pt3 IBB – <strong>Institute</strong> <strong>of</strong> Biotechnology and Bioengineering, IST-UTL, Lisboa Portugal4 Centre for Chemical Processes, IST-UTL, Lisboa, PortugalThis paper describes preliminary work done by the authors towards thedevelopment <strong>of</strong> new metallic heterogeneous catalysts that are intended to be used inthe production <strong>of</strong> biodiesel. Biodiesel, is a mixture <strong>of</strong> mono-alkyl esters <strong>of</strong> fatty acids,and is currently manufactured by transesterification <strong>of</strong> triglycerides with methanol,using NaOH or KOH as liquid base catalyst. However, an important drawback relatedwith the use <strong>of</strong> these catalysts is that, the liquid based catalyst has to be neutralizedafter the reaction, thus producing salt streams. Moreover, due to the presence <strong>of</strong> freefatty acids, it reacts to form soaps as unwanted by-products, hence requiring moreexpensive separation processes. Therefore, there is currently a drive towards thedevelopment <strong>of</strong> industrial processes for biodiesel production using solid catalysts. Inaddition to lower separation processes costs, the key benefit <strong>of</strong> using solid acid orbasic catalysts is that, the catalysts don’t have to be removed since they don’t mixwith the biodiesel. This work refers preliminary studies done in these field using CaOand Al 2 O 3 heterogeneous support catalysts, with Li, Sr and Ca as solid precursors.Several analysis techniques were used for catalysts characterization, like MIR, SEM,XRD, TG and BET. The results obtained so far will be presented in this proceeding.References:[1]. Gomes, J.F., Puna, J., Bordado, J.C., Correia, J.N., «Development <strong>of</strong> heterogeneous catalysts fortransesterification <strong>of</strong> triglycerides». Reaction Kinetics and <strong>Catalysis</strong> Letters, 2008, 95(2), 273-279.[2]. Park et. al., «The heterogeneous catalyst system for the continuous conversion <strong>of</strong> free fatty acidsin used vegetable oils for the production <strong>of</strong> biodiesel». <strong>Catalysis</strong> Today, 2008, 131, 238-243.[3]. MacLeod et. al., «Evaluation <strong>of</strong> the activity and stability <strong>of</strong> alkali-doped metal oxide catalysts forapplication to an intensified method <strong>of</strong> biodiesel production». Chemical Engineering Journal,2008, 135, 63-70.[4]. Serio et. al., «Heterogeneous Catalysts for Biodiesel Production». Energy & Fuels, 2008, 22, 207-217.[5]. Huaping et. al., «Preparation <strong>of</strong> Biodiesel Catalyzed by Solid Super Base <strong>of</strong> calcium Oxide and ItsRefining Process». Chinese Journal <strong>of</strong> <strong>Catalysis</strong>, 2006, 27(5), 391-396.[6]. Xie et. al., «Alumina-supported potassium iodide as a heterogeneous catalyst for biodieselproduction from soybean oil». Journal <strong>of</strong> Molecular <strong>Catalysis</strong> A: Chemical, 2006, 255, 1-9.104
PP-16INVESTIGATION OF THE KINETICS OF STRAW ENZYMOLYSISEmelyanov V.M., Nurtdinov R.M., Mukhachev S.G., Ablaev A.R.,Valeeva R.T., Gadelshina G.A.Kazan State Technological University, K. Marks Street, 68, Kazan, <strong>Russia</strong>,phone: +7(843)2314049, fax: +7(843)2314042, e-mail: Emelianov@front.ruOne <strong>of</strong> the promising renewable resources <strong>of</strong> plant raw materials are straw andgreen mass <strong>of</strong> other crops. In <strong>Russia</strong>, this type <strong>of</strong> resource is not used efficiently.There are several works in the field <strong>of</strong> utilization <strong>of</strong> straw hydrolyzates andenzymolyzates in fodder production and as growth media for the processes <strong>of</strong>microbiological synthesis. However, enzymatic hydrolysis <strong>of</strong> cellulose has not yetmastered in industrial biotechnology in <strong>Russia</strong>.The processes <strong>of</strong> enzymatic hydrolysis <strong>of</strong> straw by liquid enzyme preparationsfrom Genencor International PS AO3329-1.OEN GC-440 (with cellulase activity <strong>of</strong>1470-1800 units/g), PS AO3143-1.1EN Optiflow RC 2.0, PS AO3131-1.OEN GC-220and PS AO3197-1.OEN Acellerase CB100 (with cellulase activity <strong>of</strong> 6200-7580units/g) are carried out. Model experiments for studying <strong>of</strong> enzymolysis kinetics arecarried out using paper and cotton as a source <strong>of</strong> cellulose. Further grinded andsifted through a sieve with 1 mm mesh rye straw was used. Experiments werecarried out at varying liquor ratio and concentrations <strong>of</strong> enzyme preparations. Strawwas steamed in an autoclave with excess pressure 0,07 - 0,1 MPa for 0,5 - 1 hour.Change in the total content <strong>of</strong> sugars in hydrolyzate during the process lasting up to8-10 hours is determined. A kinetic model <strong>of</strong> the process <strong>of</strong> straw enzymolysis isdeveloped. The values <strong>of</strong> kinetic constants are determined.105