skip to main content

Catalyst in Basic Oleochemicals

Research and Development Department, PT. Ecogreen Oleochemicals, Jln. Pelabuhan Kav 1, Kabil, Batam, Indonesia

Received: 18 Apr 2007; Revised: 15 Oct 2007; Accepted: 15 Oct 2007; Published: 15 Oct 2007.
Editor(s): Istadi Istadi
Open Access Copyright (c) 2007 by Authors, Published by BCREC Group
Creative Commons License This work is licensed under a Creative Commons Attribution-ShareAlike 4.0 International License.
Fulltext View|Download

Citation Format:
Abstract

Currently Indonesia is the world largest palm oil producer with production volume reaching 16 million tones per annum. The high crude oil and ethylene prices in the last 3 – 4 years contribute to the healthy demand growth for basic oleochemicals: fatty acids and fatty alcohols. Oleochemicals are starting to replace crude oil derived products in various applications. As widely practiced in petrochemical industry, catalyst plays a very important role in the production of basic oleochemicals. Catalytic reactions are abound in the production of oleochemicals: Nickel based catalysts are used in the hydrogenation of unsaturated fatty acids; sodium methylate catalyst in the transesterification of triglycerides; sulfonic based polystyrene resin catalyst in esterification of fatty acids; and copper chromite/copper zinc catalyst in the high pressure hydrogenation of methyl esters or fatty acids to produce fatty alcohols. To maintain long catalyst life, it is crucial to ensure the absence of catalyst poisons and inhibitors in the feed. The preparation methods of nickel and copper chromite catalysts are as follows: precipitation, filtration, drying, and calcinations. Sodium methylate is derived from direct reaction of sodium metal and methanol under inert gas. The sulfonic based polystyrene resin is derived from sulfonation of polystyrene crosslinked with di-vinyl-benzene. © 2007 by Authors, Published by BCREC Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0)

Keywords: catalyst; hydrogenation; oleochemicals; transesterification

Article Metrics:

  1. Felletschin, G., (1982), “Concerning History of Fatty Alcohol”, Fatty Alcohols Raw Materials Methods Uses, 1st Ed, Henkel KGaA Düsseldorf, p. 7
  2. Hastert, R.C., (1996), “Hydrogenation”, Bailey’s Industrial Oil & Fats Products, 5th edition, Ed. Hui, Y.H., Wiley-Interscience, New York, vol. 4, p. 257
  3. Mittelbach, M. and Remschmidt, C., (2005), “Biodiesel”, The Comprehensive Handbook, 2nd Ed., Martin Mittelbach, Austria, p. 50-54
  4. Ma, F., Clements, L.D., and Hanna, M.A. (1998), “The Effects of Catalyst, Free Fatty Acids, and Water on Transesterification of Beef Tallow”, T. ASAE, vol. 41, p. 1261
  5. Jeromin, L., et al., (1981), “Kontinuerliche veresterung in reactions kolonnen“, Fette, Seifen, Anstrichm, vol. 83, p. 493 – 504
  6. Steinnigeweg.,S and Gmehling, J., (2003), “Esterification of a Fatty Acid by Reactive Distillation”, Ind. Eng. Chem. Res., vol. 42, p. 3612 – 3619
  7. Adkins, H. and Folkers, K., (1931), "The Catalytic Hydrogenation of Esters to Alcohols”, The Journal of the American Chemical Society, vol LIII, Jan – Apr 1931, p. 1095 - 1097
  8. Normann, Von W., (1931), “Über die Katalytische Reduktion der Carboxylgruppe”, Ztschr. Angew. Chem. 44, nr. 35, S. 715
  9. Schmidt, Otto, (1931), “Die katalytische Hydrierung der Carboxylgruppe in organischen Verbindungen, insbesondere Solchen höheren Molekulargewichts”, Berichte d. D. Chem. Gesellschaft, Jahrg. LXI, S. 2051
  10. Schrauth, W., O. Schenck und K. Stickdorn, (1931), “Über die Herstellung von Kohlenwasserstoffen und Alkoholen durch Hochdruck-Reduktion von Fettestoffen”, Berichte d. D. Chem. Gesellschaft, Jahrg. LXIV, S. 1314
  11. Van de Scheur, F.T., Sai, G.U.A., Bliek, A., and Staal, L.H., (1995), “The Effect of Free Fatty Acid on the Reactivity of Copper-Based Catalysts for the Hydrogenolysis of Fatty Acid Methyl Esters”, JAOCS, vol. 72, no. 9, p. 1027-1031
  12. Buchold, H. , (1983), “Natural Fats & Oils Route to Fatty Alcohols”, Chem. Eng., vol. 21, p. 42
  13. Kreutzer, Udo R., (1984), “Manufacture of Fatty Alcohols Based on Natural Fats and Oils”, JAOCS, vol. 61, no.2, p. 343 – 348
  14. Stiles, Alvin B., (1983), “Catalyst Manufacture – Laboratory and Commercial Preparations”, Marcel Dekker, Inc., New York, p. 132-133
  15. Lotero, E., Goodwin, J.G., Bruce, D.A., Suwannakarn, K., Liu, Y.J., and Lopez, D.E., (2006), “The Catalysis of Biodiesel Synthesis”, Catalysis, vol. 19, p. 41-83
  16. Nakayama, et al., (2005), “Processes for Producing Alkyl Ester of Fatty Acid”, U.S. Patent No. 6,960,672 B2
  17. Kaita, et al., (2002), “Catalyst for Transesterification”, U.S. Patent No. 6,407,269 B2
  18. Kulkarni, M.G. et al, (2006), “Solid Acid Catalyzed Biodiesel Production by Simultaneous Esterification and Transesterification”, Green Chemistry
  19. Gryglewicz, S., (1999), “Rapeseed Oil Methyl Ester Preparation using Heterogeneous Catalyst” Bioresources Technology, vol. 70, p. 249 – 253
  20. Hiles, A and Kinley, D., (2006), “Davy Ups World Natural Fatty Alcohol Capacity”, Oils & Fats International, January 2006, p. 32-33
  21. Grafahrend, W., (2006), “Fatty Alcohol Ester Routes”, Oils & Fats International, January 2006, p. 29-30
  22. Dasari, M.A., Kiatsimkul, P.P., Sutterlin, W.R., and Suppes, G.J., (2005), “Low Pressure Hydrogenolysis of Glycerol to Propylene Glycol”, Applied Catalysis A: General, vol. 281, p. 225-231

Last update:

No citation recorded.

Last update:

No citation recorded.