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dc.contributor.advisorPreisig, Heinz A.
dc.contributor.authorErstad, Ramn
dc.date.accessioned2017-10-26T14:00:42Z
dc.date.available2017-10-26T14:00:42Z
dc.date.created2017-06-15
dc.date.issued2017
dc.identifierntnudaim:17460
dc.identifier.urihttp://hdl.handle.net/11250/2462434
dc.description.abstractTo achieve the goal of increasing the amount of biofuels, esters with their acid and alcohol components made from lignocellulose can be a sustainable technology. The maximal achievable concentration of carboxylic acids from a fermentation process is low and without an effective means of separation this is not a viable economic option compared to production from petrochemicals. To date the most promising technique for separation is membrane electrodialysis. This technique allows the removal of the acids without harming the fermentation stock. In this master project experiments on an electrodialysis membrane has been designed and the setup and design have been adjusted to each other in order to run the experiment. The design was made to explore a large part of the possible operational area to recommend areas to be further researched. A factorial design was chosen due to the large amount of information given by the few number of experiments. The goal was to see the effects of electrical current and the concentration of acetic acid on different performance indicators. This included the temperature, pH, coulombic efficiency, yield, acetate removal rate and removal time. To analyse the performance different online measurements techniques were applied these included pH, temperature and electrical potential and current logging. Samples from the experiment were analysed by HPLC and analysis of variance was performed on these results to check for any correlations and discover how the system might evolve. The analysis of variance showed that the experimental variables had a significant effect on the Coulombic efficiency and rate of transfer. For both of them, the interaction had a significant effect. The results from the analysis of variance indicated that the best operating conditions were at a high concentration and a strong electrical current. This operational mode had a lower electrical resistance during four hour runs indicating that the optimal economical performance is situated in the same area. The yield showed no significance. The catholyte pH increased in all experiments and reached a steady state around pH 12.5 while the anode pH remained constant. The temperature for both compartments increased because of the electrical resistance.
dc.languageeng
dc.publisherNTNU
dc.subjectIndustriell kjemi og bioteknologi, Prosess-systemteknikk
dc.titleExperiments on ion exchange membrane
dc.typeMaster thesis


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