Journal Pre-proofs Short communication New type of green extractant for oil production: citric acid/citric acid sodium extraction system Wen-Can Huang, Binglinlin Li, Xiangming Qi, Xiangzhao Mao PII: DOI: Reference:
S0308-8146(19)31949-1 https://doi.org/10.1016/j.foodchem.2019.125815 FOCH 125815
To appear in:
Food Chemistry
Received Date: Revised Date: Accepted Date:
8 August 2018 8 October 2019 27 October 2019
Please cite this article as: Huang, W-C., Li, B., Qi, X., Mao, X., New type of green extractant for oil production: citric acid/citric acid sodium extraction system, Food Chemistry (2019), doi: https://doi.org/10.1016/j.foodchem. 2019.125815
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New type of green extractant for oil production: citric acid/citric acid sodium
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extraction system
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Wen-Can Huanga§, Binglinlin Lia§, Xiangming Qia*, Xiangzhao Maoab*
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aCollege
of Food Science and Engineering, Ocean University of China, Qingdao
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266003, China bLaboratory
for Marine Drugs and Bioproducts of Qingdao National Laboratory for Marine Science and Technology, Qingdao 266237, China
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* Corresponding author:
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Professor Xiangming Qi; E-mail:
[email protected]
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Professor Xiangzhao Mao; E-mail:
[email protected]
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§ These authors contributed equally.
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ABSTRACT
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Developing green solvents with low toxicity and low energy consumption is an
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important issue for edible oil production. In this study, a novel extraction system,
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specifically a citric acid/citric acid sodium mixture, was developed for oil extraction
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from seed crops. Peanut and pumpkin seeds were used to evaluate extraction
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efficiency and more than 70% and 57% oils, respectively, were extracted from peanut
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and pumpkin seeds at 4 ºC. After extraction, the oils floated on the surface of the
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solution and could be separated from the solvent system without evaporation. The
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extraction of edible oils was achieved without the use of toxic chemicals or
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energy-intensive equipment. This study provided a green and efficient method, and
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showed the potential of the proposed citric acid/citric acid sodium extraction system
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for production of edible oils from natural sources.
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Keywords: Citric acid, Citric acid sodium, Green extractant, Vegetable Oils,
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Extraction, Nature products, Peanut seeds, Pumpkin seeds
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1. Introduction
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Vegetable oils extracted from plants are used widely in the food, pharmaceutical,
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and cosmetic industries (Jiao, Li, Gai, Li, Wei, Fu, et al., 2014; Juliano, Cossu,
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Alamanni, & Piu, 2005; Rahate & Nagarkar, 2007). Edible vegetable oils contain a
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variety of bioactive substances and nutrients including vitamin E, phospholipids,
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choline, and omega-3 and omega-6 fatty acids as well as other polyunsaturated,
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monounsaturated, and saturated fats (Jiao, et al., 2014; Lu, Zhao, Yu, & Feng, 2015;
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Maier, Schieber, Kammerer, & Carle, 2009; Zhong, Bedgood, Bishop, Prenzler, &
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Robards, 2007). Because vegetable oils have high energy contents, some (e.g.
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soybean and corn oil) are also used as biodiesel feedstocks (Martínez, Sánchez,
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Encinar, & González, 2014; Patil & Deng, 2009).
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Various extraction techniques have been used for extraction, such as solvent,
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supercritical fluid, mechanical pressing, enzymatic, ultrasonic, and heat reflux
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extraction methods (Deng, Li, Li, Zaaboul, Jiang, Li, et al., 2018; Ghafoor, Choi, Jeon,
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& Jo, 2009; Wang & Weller, 2006). Among these techniques, solvent and
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supercritical fluid extractions, and mechanical pressing are used most commonly.
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Extraction using organic solvents is rapid and effective, but most organic solvents are
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highly toxic, and their use can have undesirable effects on oil quality (Jiao, et al.,
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2014). Furthermore, organic solvent extraction requires energy-intensive evaporation
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for removal of the solvent, and the solvent can lead to environmental pollution (Lai,
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De Francesco, Aguinaga, Parameswaran, & Rittmann, 2016; Mubarak, Shaija, &
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Suchithra, 2015). In contrast to organic solvent methods, supercritical fluid extraction
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has lower viscosities and higher diffusivities (Leunissen, Davidson, & Kakuda, 1996;
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Palmer & Ting, 1995). However, despite its potential advantages, use of supercritical
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fluid extraction is limited due to high installation and operating costs (Lam & Lee,
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2012). Mechanical pressing is commonly used to extract oils from nuts and seeds.
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However, the oil produced with high temperature pressing technique has a poor
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sensory quality and a significant loss of vitamin E, sterol, wheat germ phenol,
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phospholipid, and other nutritional factors, and moreover, the stability of the oil is
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poor. On the other hand, only less than 10% of peanut oil can be extracted by using
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cold pressing technique. Thus, a cheap, safe, and environmentally friendly method for
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industrial-scale extraction of edible oils.
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In this study, a green extraction system, citric acid/citric acid sodium, was
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developed. Peanut and pumpkin seeds were used to evaluate extraction efficiency.
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Edible oil extraction was achieved without the use of toxic chemicals or any
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energy-consuming processes, such as cell disruption or solvent evaporation.
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2. Materials and methods
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2.1. Materials
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Nile red, a standard mixture of 37 fatty acids methyl esters (FAMEs), and
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nonadecanoic acid methyl ester were purchased from Sigma-Aldrich (St. Louis, MO,
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USA); citric acid, sodium citrate, chloroform, and methanol were purchased from
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Sinopharm Chemical Reagent Co., Ltd. (Shanghai, China); peanut and pumpkin seeds
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were purchased from a local market (Qingdao, China).
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2.2. Oil extraction
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The peanut and pumpkin seeds were dried in an oven at 60 °C and then ground.
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The volume ratio of citric acid (0.1 mol/L) and citric acid sodium (0.1 mol/L) was
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varied to adjust the pH to 2.2, 3.0, 3.2, 3.4, and 3.8. The mass ratio of ground peanut
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or pumpkin seeds to solvent was fixed at 1:2. The mixtures were maintained at 4 ºC
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for 48 h before the oils were collected from the top of the solution using a pipet. Each
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sample was extracted one time and all the experiments were replicated three times.
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2.3. Total oil extraction
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Total lipids were extracted from the peanut and pumpkin seeds using the Folch
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method (Folch, Lees, & Sloane Stanley, 1957). Briefly, 10 g of freeze-dried peanut
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and pumpkin seeds were grounded and then added to chloroform-methanol (2:1);
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lipids were obtained by evaporating the solvents after extraction. Experiments were
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replicated three times.
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2.4. Conversion of oils
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To determine the oil contents, isolated oils were converted to fatty acid methyl
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esters (FAMEs) via transesterification. Briefly, samples of the crude oils (100 mg)
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were dissolved in 3 mL chloroform/methanol (1:1) and sulfuric acid was added to
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each as a catalyst, and 100 μL of nonadecanoic acid methyl ester as an internal
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standard was added to the solution. The mixtures were heated at 85 ºC for 1 h in a
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water bath.
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FAME contents were analyzed by gas chromatography–mass spectrometry
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(Trace 1310 GC, Thermo Fisher Scientific, Waltham, MA, USA). The injection port
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temperature was 290 °C. Analytes were separated by a TG-5MS column, with helium
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as carrier gas. Mass spectra were recorded under electron ionization (70 eV) with the
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m/z range of 30 to 400 amu. The temperature of the column was increased from 80 °C
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to 200 °C at 10 °C min-1, from 200 °C to 250 °C at 5 °C min-1, and from 250 °C to
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270 °C at 2 °C min-1.
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The oil extraction efficiency (EE) was determined using:
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where Oils
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extraction system, and Oils chloroform/methanol is the oils extracted by Folch method.
citric acid/citric acid sodium
is the oils extracted by citric acid/citric acid sodium
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2.5. Microscopic observation
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To observe any changes in the oil drops before and after treatment, peanut and
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pumpkin seed cells were stained with Nile red. The stain was pre-prepared as a stock
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solution (1 mg/ml) in ethanol and samples stained for 10 min prior to observation
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using confocal laser microscopy (FV1000, Olympus, Tokyo, Japan).
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Structural changes in the samples before and after citric acid/citric acid sodium
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treatment were observed using scanning electron microscopy (JSM-840 SEM, JEOL
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Ltd., Tokyo, Japan). Dried samples were placed on a metal substrate using carbon
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tape and sputter-coated with gold and the results recorded at an acceleration voltage
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of 10 kV.
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3. Results and discussion
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3.1. Oil extraction of citric acid/citric acid sodium extraction system
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The extraction efficiency of the citric acid/citric acid sodium system was
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investigated under various conditions. As shown in Fig. 1, extraction efficiency was
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best when the pH of the citric acid/citric acid sodium mixture was less than 3.
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However, the greatest oil extraction efficiency was at pH 3; above pH 3, the
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extraction efficiency decreased gradually. At pH 3, more than 70% and 57% of oils
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were extracted from peanut seeds and pumpkin seeds, respectively. Although oil
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could not be extracted from peanut seeds at pH 2.2 and 3.8, 25% and 20% of oil
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contents were extracted from pumpkin seeds at pH of 2.2 and 3.8, respectively. The
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citric acid/citric acid sodium extraction system, as a green extractant possesses many
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properties, such as being nonvolatile, biodegradable, nontoxic, recyclable, and stable.
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Furthermore, in comparison with other extraction methods, such as solvent extraction
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and supercritical fluid extraction, the citric acid/citric acid sodium extraction system
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does not require energy-consuming processes or high operating cost. On the other
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hand, compared with cold pressing method, which is considered having a promising
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market prospects, the citric acid/citric acid sodium extraction system resulted in much
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higher oil yield. The oil extraction mechanism of the citric acid/citric acid sodium
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system is not yet well understood and requires further research.
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3.2. Microscopic analysis
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The peanut and pumpkin oils, before and after extraction, were imaged using
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laser scanning confocal microscopy. As shown in Fig. 2, before extraction, the peanut
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and pumpkin oil drops were small and regular with a diameter of about 1 µm. The
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size was in accordance with a previously reported oil drop size distribution in peanut
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cotyledons (Carlton, Halse, Maphossa, & Mallett, 2001), indicating that oils had not
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been released before citric acid/citric acid sodium treatment. After extraction, some
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large coalesced oil droplets were observed. Since surface tension always allows small
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droplets to coalesce and maintain a nearly spherical shape permitting ready drainage
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of surrounding fluid (Neitzel & Dell'Aversana, 2002), this result suggested that oils
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previously bound to the cell structure were separated by citric acid/citric acid sodium
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extraction system and released into the solution after citric acid/citric acid sodium
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treatment.
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The morphology of peanut and pumpkin seed cells, before and after extraction,
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were examined using scanning electron microscopy (SEM). As shown in Fig. 3a and
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3c, SEM images of peanut and pumpkin seeds without treatment were blur. It was
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because before citric acid/citric acid sodium treatment, there were oils on the surface
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of the ground peanut and pumpkin seeds. Oils can affect the current of SEM, resulting
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in blurred images. After treatment, SEM images became clear (Fig. 3b and 3c). The
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results of microscopic analysis indicated that acid/citric acid sodium extraction system
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can effectively extract oils from peanut and pumpkin seeds.
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4. Conclusions
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In this study, citric acid/citric acid sodium extraction system suggest its potential
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for edible oil extraction. Using this system, significant amounts of oils were isolated
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from peanut and pumpkin seeds, which floated on the surface allowing easy
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separation from the aqueous phase without solvent evaporation, avoiding the use of
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volatile solvents and reducing energy consumed in their removal. The proposed
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extraction system could be applied for the extraction and recovery of plant oils with
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the products being used by pharmaceutical, cosmetics, and food industries. Further
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research will be required to determine the citric acid/citric acid sodium extraction
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system mechanisms of action and implications for edible oil production at industrial
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scales.
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Acknowledgments This work was supported by the Key Research and Development Project of Shandong Province (No. 2016YYSP015).
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References
191
Carlton, K. J., Halse, M. R., Maphossa, A. M., & Mallett, M. J. D. (2001). NMR
192
stray-field analysis of oil drop size distribution in peanut cotyledons. Eur.
193
Biophys. J., 29(8), 574-578.
194
Deng, B. X., Li, B., Li, X. D., Zaaboul, F., Jiang, J., Li, J. W., Li, Q., Cao, P. R., &
195
Liu, Y. F. (2018). Using Short‐Wave Infrared Radiation to Improve Aqueous
196
Enzymatic Extraction of Peanut Oil: Evaluation of Peanut Cotyledon
197
Microstructure and Oil Quality. Eur. J. Lipid Sci. Technol., 120(2), 1700285.
198
de Boer, K., Moheimani, N. R., Borowitzka, M. A., & Bahri, P. A. (2012). Extraction
199
and conversion pathways for microalgae to biodiesel: a review focused on
200
energy consumption. J. Appl. Phycol., 24(6), 1681-1698.
201
Folch, J., Lees, M., & Sloane Stanley, G. H. (1957). A simple method for the isolation
202
and purification of total lipides from animal tissues. J. Biol. Chem., 226(1),
203
497-509.
204
Ghafoor, K., Choi, Y. H., Jeon, J. Y., & Jo, I. H. (2009). Optimization of
205
ultrasound-assisted extraction of phenolic compounds, antioxidants, and
206
anthocyanins from grape (Vitis vinifera) seeds. J. Agric. Food Chem., 57(11),
207
4988-4994.
208
Jiao, J., Li, Z.-G., Gai, Q.-Y., Li, X.-J., Wei, F.-Y., Fu, Y.-J., & Ma, W. (2014).
209
Microwave-assisted aqueous enzymatic extraction of oil from pumpkin seeds
210
and evaluation of its physicochemical properties, fatty acid compositions and
211
antioxidant activities. Food Chem., 147, 17-24.
212
Juliano, C., Cossu, M., Alamanni, M. C., & Piu, L. (2005). Antioxidant activity of
213
gamma-oryzanol: mechanism of action and its effect on oxidative stability of
214
pharmaceutical oils. Int. J Pharm., 299(1-2), 146-154.
215
Lai, Y. S., De Francesco, F., Aguinaga, A., Parameswaran, P., & Rittmann, B. E.
216
(2016). Improving lipid recovery from Scenedesmus wet biomass by
217
surfactant-assisted disruption. Green Chem., 18(5), 1319-1326.
218 219
Lam, M. K., & Lee, K. T. (2012). Microalgae biofuels: A critical review of issues, problems and the way forward. Biotechnol. Adv., 30(3), 673-690.
220
Leunissen, M., Davidson, V. J., & Kakuda, Y. (1996). Analysis of volatile flavor
221
components in roasted peanuts using supercritical fluid extraction and gas
222
chromatography-mass spectrometry. J. Agric. Food Chem., 44(9), 2694-2699.
223
Lu, Q., Zhao, Q., Yu, Q.-W., & Feng, Y.-Q. (2015). Use of Pollen Solid-Phase
224
Extraction for the Determination of trans-Resveratrol in Peanut Oils. J. Agric.
225
Food Chem., 63(19), 4771-4776.
226
Maier, T., Schieber, A., Kammerer, D. R., & Carle, R. (2009). Residues of grape
227
(Vitis vinifera L.) seed oil production as a valuable source of phenolic
228
antioxidants. Food Chem., 112(3), 551-559.
229
Martínez, G., Sánchez, N., Encinar, J., & González, J. (2014). Fuel properties of
230
biodiesel from vegetable oils and oil mixtures. Influence of methyl esters
231
distribution. Biomass Bioenerg., 63, 22-32.
232
Mubarak, M., Shaija, A., & Suchithra, T. V. (2015). A review on the extraction of
233
lipid from microalgae for biodiesel production. Algal Res., 7, 117-123.
234
Neitzel, G. P., & Dell'Aversana, P. (2002). Noncoalescence and nonwetting behavior
235 236 237 238 239
of liquids. Annu. Rev. Fluid Mech., 34(1), 267-289. Palmer, M. V., & Ting, S. S. T. (1995). Applications for supercritical fluid technology in food processing. Food Chem., 52(4), 345-352. Patil, P. D., & Deng, S. (2009). Optimization of biodiesel production from edible and non-edible vegetable oils. Fuel, 88(7), 1302-1306.
240
Rahate, A. R., & Nagarkar, J. M. (2007). Emulsification of vegetable oils using a
241
blend of nonionic Surfactants for cosmetic applications. J. Disper. Sci.
242
Technol., 28(7), 1077-1080.
243 244
Wang, L., & Weller, C. L. (2006). Recent advances in extraction of nutraceuticals from plants. Trends Food Sci. Technol., 17(6), 300-312.
245
Zhong, H., Bedgood, D. R., Jr., Bishop, A. G., Prenzler, P. D., & Robards, K. (2007).
246
Endogenous biophenol, fatty acid and volatile profiles of selected oils. Food
247
Chem., 100(4), 1544-1551.
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Fig. 1. Oil extraction efficiency of citric acid/citric acid sodium extraction system at
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various pH levels.
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Fig. 2. Confocal laser micrographs of peanut seeds (a) without treatment and (b)
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treated with citric acid/citric acid sodium; pumpkin seeds (c) without treatment and
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(d) treated with citric acid/citric acid sodium.
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Fig. 3. SEM images of peanut seeds (a) without treatment and (b) treated with citric
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acid/citric acid sodium; pumpkin seeds (c) without treatment and (d) treated with
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citric acid/citric acid sodium.
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Highlights
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1. A citric acid/citric acid sodium extraction system was developed for vegetable oil extraction. 2. More than 70% and 57% oils were extracted from peanut seeds and pumpkin seeds, respectively. 3. Extracted oils floated on the solution surface and can be separated easily without evaporation.