OP-II-3

KN-6reaction with ethanol and the basic catalyst, obtaining biodiesel and glycerol asproducts, all the products obtained are separated and the organosolv pretreatedbiomass is submitted to a simultaneous saccharification and fermentation (SSF)process for bioethanol production, this bioethanol is returned to the process as areagent for the transesterification and organosolv pretreatment.Optimization of microalgal biodiesel and bioethanol yield, and reactionparameters for obtaining biodiesel with high quality were performed using thesoftware FEMLAB ® , the management of the selectivity to the desired productsthought management of the reactor operating conditions and parameters is alsoshowed, according with the biorefinery concept. Operating conditions were fixedlooking towards a possible application in a pilot plant scale.Is shown that the multifunctional reactor designed works as a simultaneous thirdgeneration biofuels producer and a one step organosolv pretreatment, oil extractorand biodiesel transesterification processes reactor.The authors thanks to the Iberoamerican Science & Technology DevelopmentProgramme CYTED, the international project 306RTO279 “New technologies forbiofuels production” UNESCO code 330303,332205,530603,330399, the ColombianAgriculture & Rural Development Ministry, and the Colombian Petroleum InstituteICP-ECOPETROL for supporting this work.33