The development of technology of 9-succinyl-8-decen acid

Authors

  • Джасим Амир Т. Ал-Хаддад Institute of Chemical Technology, Volodymyr Dahl East Ukrainian National University, st. Lenin, 31, Rubizhne, Luhansk region., 93009, Ukraine https://orcid.org/0000-0002-8251-8756
  • Екатерина Валерьевна Киселёва-Логинова Institute of Chemical Technology, Volodymyr Dahl East Ukrainian National University, st. Lenin, 31, Rubizhne, Luhansk region., 93009, Ukraine https://orcid.org/0000-0003-0826-9285
  • Евгений Вадимович Попов Institute of Chemical Technology, Volodymyr Dahl East Ukrainian National University, st. Lenin, 31, Rubizhne, Luhansk region., 93009, Ukraine https://orcid.org/0000-0001-7941-5134

DOI:

https://doi.org/10.15587/2312-8372.2015.51052

Keywords:

maleic anhydride, oleic acid, adduct, technology of 9-succinyl-8-decen acid, flow sheet

Abstract

The technology of 9-succinyl-8 decen acid is proposed. The main stage and flows are shown in the flowchart. Technology type is periodic responds to manual discharge of the crystalline product. Basic stages of technology are: charge of the components, hot filtering, synthesis in the main unit at the reflux temperature (120-123 °C), cooling the reaction mass, secondary filtration of sediments, crystallization of 9-succinyl-8-decen acid, evaporation.

As a result, this technology results in two target product: 9-succinyl-8-decen acid and mixture of raw materials, a residue of oleic acid and byproducts. The second product can be used as the organic solvent and also as semi-finished product of organic synthesis. The total yield of production is 47-49 %.

The advantages and disadvantages of the scheme and the process are considered. The features of the work associated with the properties of reactants, products and solvent are marked. It is recommended the method of charge the maleic anhydride by the melt to prevent foaming of the reaction mass. It is indicated that the liquid phase of the process is preferably moved by gravity or by vacuum of the filtration funnel to simplify the arrangement of the chart. This is possible through the distribution of equipment on several floors.

Also, in the technology it is provided return of organic solvent – perchlorethylene – back in the process to 80-85 % that significantly reduces production costs, reduce production costs and increase environmental impact of production.

Author Biographies

Джасим Амир Т. Ал-Хаддад, Institute of Chemical Technology, Volodymyr Dahl East Ukrainian National University, st. Lenin, 31, Rubizhne, Luhansk region., 93009

Applicant

Department of ecology

Екатерина Валерьевна Киселёва-Логинова, Institute of Chemical Technology, Volodymyr Dahl East Ukrainian National University, st. Lenin, 31, Rubizhne, Luhansk region., 93009

Candidate of Technical Sciences, Associate Professor

Department of ecology

Евгений Вадимович Попов, Institute of Chemical Technology, Volodymyr Dahl East Ukrainian National University, st. Lenin, 31, Rubizhne, Luhansk region., 93009

Doctor of Technical Sciences, Professor, Head of Department

Department of ecology

References

  1. Al-Haddad, J., Kiseliova-Loginova, Ye., Popov, Ye. (2014). The interaction of maleic anhydride and derivatives of long-chain olefins. Eastern-European Journal Of Enterprise Technologies, 3(6(69)), 13–18. doi:10.15587/1729-4061.2014.24996
  2. Al-Haddad, J., Kiseliova-Loginova, Ye. (2014). Kinetika vzaimodeistviia maleinovogo angidrida s oleinovoi kislotoi v srede kislotnogo rastvoritelia. Visnyk Skhidnoukrainskoho natsionalnoho universytetu im. V. Dalia, 10 (217), 34–37.
  3. Vibhute, B. P., Khotpal, R. R., Karadbhajane, V. Y., Kulkarni, A. S. (2013). Preparation of Maleinized Castor oil (MCO) By Conventional Method And It's Application in the Formulation of Liquid Detergent. International Journal of ChemTech Research, Vol. 5, № 2, 1886–1896.
  4. Soni, H. P., Bharambe, D. P. (2006). Synthesis and Evaluation of Polymeric Additives as Flow Improvers for Indian Crude Oil. Iranian Polymer Journal, 15 (12), 943–954.
  5. Al-Sabagh, A. M., Badawi, A. M., Noor El-Den, M. R. (2002, January 11). Breaking water-in-crude oil emulsions by novel demulsifiers based on maleic anhydride–oleic acid adduct. Petroleum Science and Technology, Vol. 20, № 9-10, 887–914. doi:10.1081/lft-120003685
  6. Milton, K.; assignee: Monsanto Chemical Company. (25.09.1951). Method of Preparing adducts. Patent US 2569420 A. Appl. № 144,385. Filed 15.02.1950. Available: http://www.google.com/patents/US2569420
  7. Payne, H. F.; Translated from English: Belenky, E. F. (1959). Organic Coating Technology. Vol. 1. L.: State Scientific and Technical Publishing House of Chemical Literature, 761.
  8. Peng, E., Ding, J., Xue, J. M. (2012). Succinic anhydride functionalized alkenoic ligands: a facile route to synthesize water dispersible nanocrystals. Journal of Materials Chemistry, Vol. 22, № 27, 13832–13840. doi:10.1039/c2jm30942d
  9. Rheineck, A. E., Khoe, T. H. (1969). Reaction of Maleic Anhydride with cis-Isolated Unsaturated Fatty Acid Esters. Fette, Seifen, Anstrichmittel, Vol. 71, № 8, 644–652. doi:10.1002/lipi.19690710814
  10. Holmberg, K., Johansson, J.-A., Bergman, Å., Brunk, U., Dallner, G., Berg, J.-E. (1982). Addition of Maleic Anhydride to Esters of Mono-unsaturated Fatty Acids. Acta Chemica Scandinavica, Vol. 36b, 481–485. doi:10.3891/acta.chem.scand.36b-0481
  11. Stefanoiu, F., Candy, L., Vaca-Garcia, C., Borredon, E. (2008, May). Kinetics and mechanism of the reaction between maleic anhydride and fatty acid esters and the structure of the products. European Journal of Lipid Science and Technology, Vol. 110, № 5, 441–447. doi:10.1002/ejlt.200700181

Published

2015-09-22

How to Cite

Ал-Хаддад, Д. А. Т., Киселёва-Логинова, Е. В., & Попов, Е. В. (2015). The development of technology of 9-succinyl-8-decen acid. Technology Audit and Production Reserves, 5(4(25), 35–40. https://doi.org/10.15587/2312-8372.2015.51052

Issue

Section

Technologies of food, light and chemical industry