Abstract

Enzymatic hydroesterification is a heterogeneous catalyzed process suitable for the conversion of low-cost feedstocks in biodiesel production, namely, because of its tolerance to high free fatty acid contents. The current study describes the use of Fourier transform infrared spectroscopy (FTIR) to monitor biodiesel production using enzymatic hydroesterification and, as raw materials, acid oil from soapstock and olive pomace oil. Acid oil (~34 wt.% FFA) and olive pomace oil (~50 wt.% FFA) were first hydrolyzed (35 °C, 24 h, 200 rpm, 3 wt.% of lipase from Thermomyces lanuginosus, and 1:0.5 water:oil ratio, w:w), and then enzymatic esterification was performed (35 °C, 7 h, 200 rpm, 2 wt.% of lipase from Thermomyces lanuginosus, and 2:1 molar ratio of methanol to acid). FTIR analyses were conducted on the products using a Jasco FT/IR-4100 with a scanning range of 4000–650 cm−1 at 4 cm−1 spectral resolution and 54 scans. For free fatty acid (FFA) quantification, the C=O band at 1708 cm–1 was used, corresponding to the carboxylic acid, whereas for fatty acid methyl ester (FAME) quantification, the peak corresponding to C=O at 1746 cm−1 was considered, which corresponded to the ester. The results were calibrated using volumetric titration and gas chromatography analyses, concerning FFA and FAME quantification, respectively. The best conditions for analysis were determined, and a calibration method was established. FTIR has shown to be a simple, fast, and clean technique suitable to monitor hydroesterification of low-cost feedstocks.

Highlights

  • Global oil consumption reached an estimated 99 million barrels per day in 2015, and it is projected to reach 116 million by 2030

  • The present study focused on biodiesel production and monitoring using low-cost feedstocks and a commercial lipase as biocatalyst in a hydroesterification process

  • The acid oil from soapstock used in this work had 34 ± 1 wt.% free fatty acid (FFA)

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Summary

Introduction

Global oil consumption reached an estimated 99 million barrels per day in 2015, and it is projected to reach 116 million by 2030. It is expected that energy demands will increase by 50% in 2030 relative to 2011 [1,2]. Among the potential renewable oil/energy sources, biodiesel production from waste feedstocks and other low-cost materials can play an important role in reducing the global energy demand because of its environment-friendly and renewable properties [3]. Alkaline transesterification is one of the most common and attractive chemical processes to produce biodiesel because of its low cost and simplicity (associated with the operational conditions and cost of reagents), and it is widely accepted [4,5]. The homogeneous alkaline catalysis process cannot be applied to materials

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