Abstract: The liquefaction process of cork based tree barks has led to an increase of interest due to its potential innovation in the lumber and wood industries. In this particular study the bark of Quercus cerris (Turkish oak) is used due to its appreciable amount of cork tissue, although of inferior quality when compared to the cork provided by other Quercus trees. This study aims to optimize alkaline catalysis liquefaction conditions, regarding several parameters. To better comprehend the possible chemical characteristics of the bark of Quercus cerris, a complete chemical analysis was performed. The liquefaction process was performed in a double-jacket reactor heated with oil, using glycerol and a mixture of glycerol/ethylene glycol as solvents, potassium hydroxide as a catalyst, and varying the temperature, liquefaction time and granulometry. Due to low liquefaction efficiency resulting from the first experimental procedures a study was made regarding different washing techniques after the filtration process using methanol and methanol/water. The chemical analysis stated that the bark of Quercus cerris is mostly composed by suberin (ca. 30%) and lignin (ca. 24%) as well as insolvent hemicelluloses in hot water (ca. 23%). On the liquefaction stage, the results that led to higher yields were: using a mixture of methanol/ethylene glycol as reagents and a time and temperature of 120 minutes and 200 ºC, respectively. It is concluded that using a granulometry of
Abstract: Transesterification reactions free of catalyst between
roasted chicken fat with methanol were carried out in a batch reactor
in order to produce biodiesel to temperatures from 120°C to 140°C.
Parameters related to the transesterification reactions, including
temperature, time and the molar ratio of chicken fat to methanol also
investigated. The maximum yield of the reaction was of 98% under
conditions of 140°C, 4 h of reaction time and a molar ratio of chicken
fat to methanol of 1:31. The biodiesel thus obtained exhibited a
viscosity of 6.3 mm2/s and a density of 895.9 kg/m3. The results
showed this process can be right choice to produce biodiesel since
this process does not use any catalyst. Therefore, the steps of
neutralization and washing are avoided, indispensables in the case of
the alkaline catalysis.