Abstract

The supercritical carbon dioxide (SC-CO2) extraction technique has emerged as one of the best possible alternatives to organic solvent (hexane) extraction. However, very limited information is available on process optimization for this extraction technique and the lack of available engineering data is causing the slow growth of this technique. In the present investigation, SC-CO2 extraction was carried out to extract the oil from wheat germ under various operating conditions and the oil samples were characterized for properties such as phosphorous and tocol contents (vitamin E). A three-level Box Behnken design from response surface methodology was applied to optimize the SC-CO2 extraction parameters such as pressure, temperature and CO2 flow rate with an objective to obtain high oil yield, rich tocol contents and low phosphorous content. The process parameters were maintained between 30 to 50 MPa, 40 to 60 °C and a flow rate of 10 to 30 g·min-1 in a Box Behnken design matrix. Three different second order polynomial models were obtained for oil yield, phosphorous content and tocol contents with high R2 values. The optimum conditions were found to be 50 M Pa, 60 °C and 30 g·min-1 where the predicted oil yield, phosphorous content and tocol contents were found to be 8.87%, 31.86 mg·Kg-1 and 2059.92 mg·Kg-1 respectively. Under the optimum conditions, the experimental oil yield, phosphorous content and tocol contents obtained were found to be very close to the values predicted by the model.

Highlights

  • Extraction is a primary unit operation for the processing of vegetable oils and fats

  • The SC-CO2 extraction of wheat germ was ­carried out under 17 experimental conditions which were obtained from the Box Behnken design

  • The oil yield, phosphorous content and tocol content values varied in the range of 3.92 to 9.8%, 26 to 48.4 mg·Kg-1 and 1384 to 2286.3 mg·Kg-1, respectively, in the Box

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Summary

Introduction

Extraction is a primary unit operation for the processing of vegetable oils and fats. Oils and fats are extracted using hexane, a solvent obtained from a petroleum source. It has been identified and enlisted as a hazardous air pollutant by the US EPA in the Clean Air Amendments of 1990. Traces of hexane present in the extracted oil reduce the food and nutritional value of the oil. SC-CO2 extraction shows supercritical properties at near to ambient temperature and it helps in processing heat-sensitive products. Because of all these reasons, in recent years, SC-CO2 extraction has gained huge importance as a green solvent. The process is not properly understood as studies on process optimization are yet to be done

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