Abstract

The objective of this work was to evaluate the ability of CCC as an adsorbent material for the acidity removal of RFO, aiming at the application of the oil in biodiesel production. For that, a RCCD was used for FFA removal by applying the CCC and CAC for comparative purposes. In the RCCD removal assays the effect of the Temperature, Agitation and Mass factors were assessed over acidity removal of the oil. Under the best conditions from RCCD, an evaluation of adsorption kinetics was performed, wherein it was observed the equilibrium was reached within 4 h, for the CCC. Also, the influence of the adsorbent dosage was performed. It was verified that 4 g was sufficient to allow the system to reach the maximum FFA removal. Overall, the CCC presented results approximately twice as high than those obtained by the CAC, mainly due to the pore size distribution which led to a “molecular sieving effect” for the CCC adsorbent. It allowed the major diffusion of the FFA molecules inside its narrow-distributed pores, whereas the CAC with a wider pore distribution (up to 260 Å) resulted in the larger molecules competition for the active sites inside the porous structure. The adsorbents’ characterization also evidenced that CCC adsorbent presented a higher content of oxygenated groups in its surface which acted as potential active sites for the FFA molecules resulting in an enhanced adsorbent-adsorbate affinity. Lastly, the wastes generated in the adsorption experiments, were evaluated as to their calorific power resulting in a value of 31,933 J g-1, suggesting that it could be further used for energetic purposes, such as a solid fuel for boilers and furnaces to generate thermal energy. Based on these results, the CCC stands out as a promising material for RFO acidity removal.

Highlights

  • Higher specific surface area and larger volume of pores were observed for the commercial activated carbon (CAC), a fact that may be related to the differentiated conditions of this sample production, since it is a commercial activated carbon, unlike other samples that have not gone through any type of activation

  • In the analysis of pHPZC both samples showed basic character surface (CCC: 8.61 and CAC: 8.04), which is a desirable feature for the adsorbents, since the goal of this project is to promote the adsorption of free fatty acids molecules present in the frying residual oil, reducing their acidity index

  • The value obtained in this mixture may be the result of the interaction among the characteristics of each component, or only the predominance of frying residual oil. These results show that the residue obtained on the use of carbonized corn cobs as adsorbent in the free acidity removal of frying residual oil can be used in the burning in boilers and furnaces for thermal energy generation

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Summary

Introduction

The use of waste vegetable oil originated from the frying food process as a fatty material source for biodiesel production can significantly reduce the cost, besides being considered an important step for the waste minimization and recycling. Its physical and chemical characteristics are closely associated with the presence of contaminants such as water, derived from the food and free fatty acids processing (FFA), as well as dimers and polymers that directly influence the transesterification reaction (Diya’uddeen, Albul Aziz, Daud, & Chakrabarti, 2012; Fonseca et al, 2019 ; Rocha Junior et al, 2019; Vieitez et al, 2014). A pre-treatment of the raw material, should aim better reaction yields and better product quality, acting physically in the removal of any suspended solids and contaminants, and chemically, deacidifying the medium (Berrios & Skelton, 2008; Maddikeri, Pandit, & Gogate, 2012; Casallas et al, 2018)

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