A platform for research: civil engineering, architecture and urbanism
A platform for research: civil engineering, architecture and urbanism
Palm oil trans-esterification with methanol via hetereogeneous catalysis
Four different solid catalyst' catalytic activity was studied in refined palm oil methanolysis: barium hydroxide, calcium oxide, magenesium oxide and tin oxide (IV). The last two presented low catalytic activity; they were thus discarded. The catalysts were used in powder form suspended in the reaction medium. HPLC was used for testing catalyic activity by measuring the glycerlo produced at the end of the reaction. Experiments were conducted at different pressures: 75 kPa (the pressure in Bogotá), 760 kPa, 1.800 kPa, 5.900 kPa and 11.400 kPa.), 125°C (760 kPa) and 160°C (1.800 kPa). Three different percentages of catalyser were assayed at 75 kPa and two experiments were done at very high pressure (10.9 psi) around methanol's critical point (5.900 and 11.400 kPa). Both barium hidroxide and calcium oxide presented high catalytic activity. 75% - 80% conversion was obtained with them in 8-10 hours at 63.3°C and 1.5 and 3 hours using calcium oxide and barium hydroxide (respectively) at high temperatures and pressures.
Palm oil trans-esterification with methanol via hetereogeneous catalysis
Four different solid catalyst' catalytic activity was studied in refined palm oil methanolysis: barium hydroxide, calcium oxide, magenesium oxide and tin oxide (IV). The last two presented low catalytic activity; they were thus discarded. The catalysts were used in powder form suspended in the reaction medium. HPLC was used for testing catalyic activity by measuring the glycerlo produced at the end of the reaction. Experiments were conducted at different pressures: 75 kPa (the pressure in Bogotá), 760 kPa, 1.800 kPa, 5.900 kPa and 11.400 kPa.), 125°C (760 kPa) and 160°C (1.800 kPa). Three different percentages of catalyser were assayed at 75 kPa and two experiments were done at very high pressure (10.9 psi) around methanol's critical point (5.900 and 11.400 kPa). Both barium hidroxide and calcium oxide presented high catalytic activity. 75% - 80% conversion was obtained with them in 8-10 hours at 63.3°C and 1.5 and 3 hours using calcium oxide and barium hydroxide (respectively) at high temperatures and pressures.
Palm oil trans-esterification with methanol via hetereogeneous catalysis
Julian Andrés Parra Garrido (author) / Alberto Ricardo Albis Arrieta (author) / Francisco José Sánchez Castellanos (author)
2005
Article (Journal)
Electronic Resource
Unknown
Metadata by DOAJ is licensed under CC BY-SA 1.0
| American Institute of Physics | 2013
The Acidic Methanol Esterification of Haloacetic Acids: An Alternative Approach
| British Library Conference Proceedings | 1995