Abstract

Mandarin (Citrus reticulata) is one of the most popular fruits in tropical and sub-tropical countries around the world. It contains about 22–34 seeds per fruit. This study investigated the potential of non-edible mandarin seed oil as an alternative fuel in Australia. The seeds were prepared after drying in the oven for 20 h to attain an optimum moisture content of around 13.22%. The crude oil was extracted from the crushed seed using 98% n-hexane solution. The biodiesel conversion reaction (transesterification) was designed according to the acid value (mg KOH/g) of the crude oil. The study also critically examined the effect of various reaction parameters (such as effect of methanol: oil molar ratio, % of catalyst concentration, etc.) on the biodiesel conversion yield. After successful conversion of the bio-oil into biodiesel, the physio-chemical fuel properties of the virgin biodiesel were measured according to relevant ASTM standards and compared with ultra-low sulphur diesel (ULSD) and standard biodiesel ASTM D6751. The fatty acid methyl esters (FAMEs) were analysed by gas chromatography (GC) using the EN 14103 standard. The behaviour of the biodiesel (variation of density and kinematic viscosity) at various temperatures (10–40 °C) was obtained and compared with that of diesel fuel. Finally, mass and energy balances were conducted for both the oil extraction and biodiesel conversion processes to analyse the total process losses of the system. The study found 49.23 wt % oil yield from mandarin seed and 96.82% conversion efficiency for converting oil to biodiesel using the designated transesterification reaction. The GC test identified eleven FAMEs. The biodiesel mainly contains palmitic acid (C16:0) 26.80 vol %, stearic acid (C18:0) 4.93 vol %, oleic acid (C18:1) 21.43 vol % (including cis. and trans.), linoleic acid (C18:2) 4.07 vol %, and less than one percent each of other fatty acids. It is an important source of energy because it has a higher heating value of 41.446 MJ/kg which is close to ULSD (45.665 MJ/kg). In mass and energy balances, 49.23% mass was recovered as crude bio-oil and 84.48% energy was recovered as biodiesel from the total biomass.

Highlights

  • The analyses of mass and energy balances were conducted on mandarin oil extraction, biodiesel conversion and the total process based on input feedstock and output products

  • The crude oil was converted to biodiesel by an alkali catalyst transesterification reaction

  • Important physicochemical fuel properties were measured under relevant ASTM standards and compared with ultra-low sulphur diesel

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Summary

Introduction

Energy recovery from waste and non‐edible oil seeds is the main focus of this of green mandarin waste which contains about 1.5–2.0 thousand tonnes of seeds. Australia who are currently more than 50,000 hectaresglobally They produce about thousand tonnes of mandarin fruit per contains non-edible oil, is usually waste residue of the fruit. It could be one of the prospective sources of year [7] and export 28% of their total production, market another 15–20% for local consumption as alternative fuel (biodiesel) and has been investigated in this study.

Summary
Seed Collection and Kernel Extraction
10 Moisture
Reaction Design
Conversion Procedure
Fuel Properties
Calculation of Mass and Energy Balances
Effect of Catalyst Concentration
Effect ofratio
Effect of Reaction Temperature
Effect of Reaction Time
Physio-Chemical Fuel Properties of the Biodiesel
Physical Behaviour of Mandarin Biodiesel at Various Temperatures
Mass and Energy
Conclusions

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