Denicking of fatty acid pitch |
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Authors: | G Aly S Stenström F Bertilsson M Beijer |
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Affiliation: | (1) Department of Chemical Engineering I, University of Lund, P.O. Box 124, S-22100 Lund, Sweden |
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Abstract: | Unsaturated fatty acids are usually hydrogenated with a nickel catalyst. As a side reaction, nickel dissolves in the fatty
acids and forms nickel soaps. On refining the crude fatty acid feedstock by distillation, these nickel soaps are enriched
in the bottom fraction (pitch) to a concentration range of 2,500–5,500 ppm. With a heat value comparable to heavy fuel oil,
the pitch has been used as fuel. However, due to new environmental restrictions, the nickel concentration must be considerably
reduced to limit gas emission of nickel. In this study, solvent extraction was investigated as a separation method for denickling
of this valuable oleochemical by-product. At a temperature of 80°C, the nickel content in the pitch was reduced from 2,900
ppm to 4 ppm in three extraction steps by means of 1 wt% citric acid in water. Based on experimental results, a preliminary
process flowsheet is presented consisting of extraction, stripping, acid washing and electrolysis. An economic analysis, performed
on the extraction process and a process based on direct combustion followed by electrostatic precipitation revealed that direct
combustion is economically more advantageous. However, the compatibility of the extraction alternative can be considerably
improved by process optimization. The type and concentration of the stripping and acid washing agents, phase ratios, temperature,
ionic strength and the equilibrium pH of the aqueous and acid phases are important process parameters that should be considered
in the optimization process. |
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Keywords: | Denickling fatty acids pitch solvent extraction |
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