Production of sucroesters using solvent-free reactive systems containing emulsifiers

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Abstract

The transesterification reaction of sucrose and fatty acid methyl esters to produce sucroesters was experimentally evaluated using commercial emulsifiers as compatibility agents. Reactions were carried out at temperatures between 100 and 140°C, using emulsifier concentrations in the range of 5 to 15 %wt, and potassium carbonate as catalyst. Fatty acid methyl esters consumption and sucroesters production was monitored by HPLC analysis of samples. Methyl esters conversions around 40 % were obtained with 68 %wt monoester content in sucroesters mixture. Despite the reaction times were reduced by operating at high temperatures and high emulsifier’s concentration, multiple substitution and color degradation were observed. Higher productivities of sucroester and higher selectivity to monoesters were obtained when potassium palmitate was used as contacting agent. The lower monoester content in the final product was obtained when using a commercial sucroester emulsifier. Results of this study can be used for preliminary process design in a solvent-free production of biobased sucroesters.

Figures

  • Figure 1. Sucrose fatty acid esters production by transesterification of fatty acid methyl ester (FAME) and sucrose. Source: Authors
  • Figure 2. Experimental setting for transesterification of FAME and sucrose to produce sucroester. Source: Authors
  • Figure 3. HPLC chromatogram of a mixture 50:50 of sucrose palmitate and methyl palmitate ester. Peak identifications: (S) Solvent; (1) Sucrose monopalmitate. (2) Sucrose dipalmitate. (3) Sucrose dipalmitate. (4) Methyl palmitate. (5) Sucrose tripalmitate. (6) Sucrose tetrapalmitate. Source: Authors
  • Table 1. Results of reaction during sucroesters production using emulsifiers as contacting agent at different operating conditions.
  • Figure 4. Kinetic profiles in sucrose palmitate production by transesterification of methyl palmitate and sucrose at 120°C using (a) potassium palmitate or (b) glycerol monoestearate as emulsifiers, at different concentrations ( 15 wt%, 10 wt % and 5 wt%). Source: Authors a.
  • Figure 5. Kinetic profiles during sucrose palmitate production by transesterification of methyl palmitate and sucrose using sucrose palmitate as emulsifier at (a) 140°C, (b) 120°C and (c) 100°C, and at different concentrations ( 15 wt%, 10 wt % and 5 wt%). Source: Authors
  • Figure 6. Time of reaction required to reach 20% conversion of methyl palmitate in sucroester production at 100, 120 and 140°C using as emulsifier sucroester at 5%wt and 15%wt. Source: Authors
  • Figure 9. Productivity of solvent-free sucroester production at 120°C using as emulsifier potassium palmitate (KP), sucroester (SE) or glycerol monos-tearate (GMS) 5%wt, 10%wt and 15%wt. Source: Authors

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APA

Gutiérrez, M. F., Orjuela, Á., Rivera, J. L., & Suaza, A. (2018). Production of sucroesters using solvent-free reactive systems containing emulsifiers. Ingenieria e Investigacion, 38(1), 16–23. https://doi.org/10.15446/ing.investig.v38n1.61432

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