Abstract
Recovery and reuse of high-acidity vegetable oil waste (higher content of free fatty acids) is a major concern for reducing their effect on the environment. Moreover, the conventional deacidification processes are known to show drawbacks, such as oil losses or higher costs of wastewater treatment, for which it requires great attention, especially at the industrial scale. This work presents the design of a highly efficient and sustainable process for Camelina sativa oil deacidification by using an ecofriendly method, namely molecular distillation. Experimental studies were performed to identify operating conditions for removing of free fatty acids (FFA) by molecular distillation which involves the oil evaporation in high vacuum conditions. The experimental studies were supported by statistical analysis and technical-economic analysis. Response surface methodology (RSM) was employed to formulate and validate second-order models to predict deacidification efficiency, FFA concentration, and triacylglyceride (TAG) concentration in deodorized oil based on three parameters effects, validated by statistical p-value < 0.05. For a desirability function value of 0.9826, the optimal parameters of evaporator temperature at 173.5 °C, wiper speed at 350 rpm, and feed flowrate at 2 mL/min were selected. The results for process design at optimal conditions (using conventional and molecular distillation methods) showed an efficiency over 92%, a significant reduction in FFA (up to 1%), and an increase in TAG (up to 93%) in refined oil for both methods. From an economical point of view, the deacidification by molecular distillation of Camelina sativa oil is a sustainable process: no wastewater generation, no solvents and water consumption, and lower production costs, obtaining a valuable by-product (FFA).
Highlights
Mono, di- and triglycerides are the main components of crude oils, in addition to tocopherols, squalene, and sterols in traces (200–800 ppm), whose presence improve oil oxidative stability
TAG and acidity value of 7.17 ± 0.07 mg KOH/g oil. These results show the great tendency of this oil for oxidation, due to the presence of components with many double bonds
Deacidification efficiency was around 82% for all samples, and 0.6 g/g oil was collected as wastewater
Summary
Mono-, di- and triglycerides are the main components of crude oils, in addition to tocopherols, squalene, and sterols in traces (200–800 ppm), whose presence improve oil oxidative stability. Besides these desired components, crude oils contain undesirable impurities as phospholipids (100–500 ppm), free fatty acids (FFA) (5–20%), metal ions and metal complexes (2–15 mg·kg−1 ), oxidized products (2–6 meq·kg−1 ), and moisture (1–3%) [1]. FFA content is one of the most important aspects that influences edible oil quality or their usage as raw material in biodiesel production because they are more susceptible to autoxidation than the esterified fatty acids (FFA act like pro-oxidants, initiating the oxidation mechanism in lipids, leading to rancidity) or produce soaps (by mixing with methanol for transesterification reaction) [1].
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