Production of Biogasoline via Pyrolysis of Oleic Acid Basic Soaps

Authors

  • Endar Puspawiningtiyas Department of Chemical Engineering, Institut Teknologi Bandung, Jalan Ganesa No. 10, Bandung 40132, West Java, Indonesia
  • Tirto Prakoso Department of Chemical Engineering, Institut Teknologi Bandung, Jalan Ganesa No. 10, Bandung 40132, West Java, Indonesia
  • Meiti Pratiwi Department of Bioenergy and Chemurgy, Institut Teknologi Bandung, Jalan Ganesa No. 10, Bandung 40132, West Java, Indonesia
  • Subagjo Subagjo Department of Chemical Engineering, Institut Teknologi Bandung, Jalan Ganesa No. 10, Bandung 40132, West Java, Indonesia
  • Tatang Hernas Soerawidjaja Department of Bioenergy and Chemurgy, Institut Teknologi Bandung, Jalan Ganesa No. 10, Bandung 40132, West Java, Indonesia

DOI:

https://doi.org/10.5614/j.eng.technol.sci.2022.54.3.11

Keywords:

biohydrocarbon, gasoline, metal soap, oleic acid, pyrolysis

Abstract

In this study, an investigation on the effect of the Ca/Mg/Zn mixing ratio on gasoline-range hydrocarbon production by oleic basic soap pyrolysis was carried out. The ratios of calcium to magnesium used were 15%, 35%, 50%, 65%, and 85% with constant Zn. Oleic basic soap was obtained by saponification with the modified fusion method. Pyrolysis experiments were carried out at 450 C using a semi-continuous reactor with a feed flow rate of 5 g/15 min. The process produced three fractions, i.e., gas, solid, and liquid (bio-hydrocarbon + water). The gas products were characterized by GC-TCD, and the results showed the presence of carbon dioxide, hydrogen, nitrogen, oxygen, and methane. Based on the GC-FID and FT-IR results, the bio-hydrocarbon comprised mainly homologous hydrocarbon from carbon number C7 to C19 containing n-alkanes, alkenes, various iso-alkanes, and some oxygenated compounds. All calcium ratios in the oleic basic soap produced hydrocarbon in the range of gasoline (C7-C11) as the dominant product. The maximum yield of gasoline (74.86%) was achieved at 15% calcium.

Downloads

Download data is not yet available.

Author Biography

Tirto Prakoso, Department of Chemical Engineering, Institut Teknologi Bandung, Jalan Ganesa No. 10, Bandung 40132, West Java, Indonesia

Biodiesel, Biofuel, Oleochemical, Biogasoline, Bioavtur, Green diesel.

References

Lam, S.S., Progress in Waste Oil to Sustainable Energy, with Emphasis on Pyrolysis Techniques, Renewable and Sustainable Energy Reviews, 53, pp. 741-753, 2016.

Scott, D.S., Plskorz, J. & Radleln, D., Liquid Products from the Continuous Flash Pyrolysis of Biomass, Industrial and Engineering Chemistry Process Design and Development, 24(3), pp. 581-588, 1985.

Lede, J., Flash Pyrolysis of Wood in a Cyclone Reactor, Chemical Engineering and Processing, 20(6), pp. 309-317, 1986.

Bridgwater, A.V., Meier, & Radlein, D., An Overview of Fast Pyrolysis of Biomass, Organic Geochemistry, 30(12), pp. 1479-1493, 1999.

Anuar Sharuddin, S.D., A Review on Pyrolysis of Plastic Wastes, Energy Conversion and Management, 115, pp. 308-326, 2016.

Aramideh, S., Numerical Simulation of Biomass Fast Pyrolysis in an Auger Reactor, Fuel, 156, pp. 234-242, 2015.

Kassargy, C., Gasoline and Diesel-Like Fuel Production by Continuous Catalytic Pyrolysis of Waste Polyethylene and Polypropylene Mixtures Over USY Zeolite, Fuel, 224, p. 764-773, 2018.

Fortes, I.C.P. & Baugh, P.J., Pyrolysis-GC/MS Studies of Vegetable Oils from Macauba Fruit, Journal of Analytical and Applied Pyrolysis, 72(1), pp. 103-111, 2004.

Buzetzki, E., Effects of Oil Type on Products Obtained by Cracking of Oils and Fats, Fuel Processing Technology, 92(10), pp. 2041-2047, 2011.

Chiaramonti, D., Bio-Hydrocarbons Through Catalytic Pyrolysis of Used Cooking Oils: Towards Sustainable Jet and Road Fuels, in 70th Conference of the Italian Thermal Machines Engineering Association, ATI 2015, Elsevier Ltd., 2015.

Li, L., Catalytic Hydrothermal Conversion of Triglycerides to Non-Ester Biofuels, Energy and Fuels, 24(2), pp. 1305-1315, 2010.

Herskowitz, M., A Commercially-viable, One-Step Process for Production of Green Diesel from Soybean Oil on Pt/SAPO-11, Fuel, 111, pp. 157-164, 2013.

Asomaning, J., Mussone, P. & Bressler, D.C., Thermal Cracking of Free Fatty Acids in Inert and Light Hydrocarbon Gas Atmospheres, Fuel, 126, pp. 250-255, 2014.

Dandik, L., Aksoy, H.A. & Erdem-Senatalar, A., Catalytic Conversion of Used Oil to Hydrocarbon Fuels in A Fractionating Pyrolysis Reactor, Energy and Fuels, 12(6), pp. 1148-1152, 1998.

Kufeld, S.E., Production of Diesel from Safflower oil by a Soap-Pyrolysis Process, Thesis, Master of Science in Chemical Engineering, Montana State University,United States, 1988.

Hilten, R., Production of Aromatic Green Gasoline Additives Via Catalytic Pyrolysis of Acidulated Peanut Oil Soap Stock, Bioresource Technology, 102(17), pp. 8288-8294, 2011.

Santos, M.C., Gasoline-Like Hydrocarbons by Catalytic Cracking of Soap Phase Residue of Neutralization Process of Palm Oil (Elaeis Guineensis Jacq), Journal of the Taiwan Institute of Chemical Engineers, 2016.

Kaisha, N.G.K.K., A Method of Manucafturing Hydrocarbon Oils from Oils, Fats or Fatty Acids, 1923.

Hsu, O.G., Pyrolysis of the Calcium Salts of Fatty Acid, Industrial and Engineering Chemistry, pp. 2141-2145, Oct.1950.

Schwab, A.W., Diesel Fuel from Thermal Decomposition of Soybean Oil, Journal of the American Oil Chemists' Society, 65(11), pp. 1781-1786, 1988.

Hirsch, A. & Fleischer, E., Process for The Production of Basic Soaps of Divalent Metals in Powder Form, US Patent No: 4.927.548, 1990, 22 May 1990.

Worschech, K.W.P., Jaeckel, M. & Fleischer, E., Basic Calcium/ Zinc Mixed Soaps, Canadian Journal of Chemical Engineering, Canada Patent No CA2156929C, 1995.

Worschech, K.F.E., Basische Magonesium/Zinc- Seifan, Verfahren zur ihrer herstellung und ihre Verwendung als Stabilisatoren fur thermopastische Kunstoffe, German Patent no DE4204866, 1993, 26 August 1993.

Rogers, R.H. & Blew, W.R., Manufacture of Metal Soaps, US Patent No: 2.890.232, 1956, Serial No. 588.265, 31 May 1956.

McAskie, W., Ruminant Feedstuffs, Their Production and Apparatus for Use Therein, US Patent No: 4.826.694, 1989, 2 May 1989.

Neonufa, G.F., Biohydrocarbon Production for Jet Fuel from Palm Oil Derivative Products, IOP Conference Series: Materials Science and Engineering, 823, pp. 012-029, 2020.

Joonwichien, S.A.D., A., The Study of Preparation of Biodiesel from Pyrolysis of Palm Stearin and Soap of Palm Stearin Over Catalyst, 2006.

Zheng, Y., Efficient and Stable Ni-Cu Catalysts for Ex Situ Catalytic Pyrolysis Vapor Upgrading of Oleic Acid into Hydrocarbon: Effect of Catalyst Support, Process Parameters and Ni-To-Cu Mixed Ratio, Renewable Energy, 154, pp. 797-812, 2020.

Wang, F., Promoting Hydrocarbon Production from Fatty Acid Pyrolysis Using Transition Metal or Phosphorus Modified Al-MCM-41 Catalyst, Journal of Analytical and Applied Pyrolysis, 156, pp. 105-146, 2021.

Pratiwi, M., Metal Basic Soaps as Intermediate of Biohydrocarbon Production from Vegetable Oil/ Fats, Doctoral Dissertation, Institut Teknologi Bandung, Indonesia, 2019.

Neonufa, G.F., Investigation of Ca/Mg/Zn Metals Mixing Ratio for Production of Soap with High Alkali Content, International Journal of Chemical Engineering and Applications, 10, pp. 149-153, 2019.

Wan and Chang, China's Motor Fuels from Tung Oil, China Vegetable Oil Corporation, pp. 1543-1548, Dec. 1947.

Avidan, A.A. & Shinnar, R., Development of Catalytic Cracking Technology. A Lesson in Chemical Reactor Design, Industrial and Engineering Chemistry Research, 29(6), pp. 931-942, 1990.

Rice, F.O., The Thermal Decomposition of Organic Compounds from the Standpoint of Free Radicals. III. The Calculation of the Products Formed from Paraffin Hydrocarbons, Journal of the American Chemical Society, 55(7), pp. 3035-3040.1933.

Puspawiningtiyas, E., Effect of metal type on basic soap pyrolysis produce bio-gasoline, IOP Conference Series: Materials Science and Engineering, 823: pp. 012-027, 2020.

Fontaine, M.F., Treatment of Reformed Hydrocarbons with a Zinc Oxide-Zinc Chromite Catalyst,US Patent No: 2.967.143, 1961.

Luo, Y., The Thermal Cracking of Soybean/Canola Oils and Their Methyl Esters. Fuel Processing Technology, 91(6), pp. 613-617, 2010.

Idem, R.O., Katikaneni, S.P.R. & Bakhshi, N.N., Thermal Cracking of Canola Oil: Reaction Products in the Presence and Absence of Steam, Energy and Fuels, 10(6), pp. 1150-1162,1996.

Kubov A., New Path in the Thermal Cracking of Triacylglycerols (Canola and Soybean Oil), Fuel, 90(8), pp. 2598-2608, 2011.

Asomaning, J., Mussone, P. & Bressler, D.C., Pyrolysis of Polyunsaturated Fatty Acids, Fuel Processing Technology, 120, pp. 89-95, 2014.

Melero, J.A., Garc, A. & Clavero, M., 15 - Production of Biofuels via Catalytic Cracking, in Handbook of Biofuels Production, Luque, R. Campelo, J. & Clark, J. (Ed.), Woodhead Publishing. pp. 390-419. 2011.

Downloads

Published

2022-05-31

How to Cite

Puspawiningtiyas, E., Prakoso, T., Pratiwi, M., Subagjo, S., & Soerawidjaja, T. H. (2022). Production of Biogasoline via Pyrolysis of Oleic Acid Basic Soaps. Journal of Engineering and Technological Sciences, 54(3), 220311. https://doi.org/10.5614/j.eng.technol.sci.2022.54.3.11

Issue

Section

Articles

Most read articles by the same author(s)