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EFFECTS OF EXTRACTION AND REFINING ON THE ...I also greatly appreciate my lab mates and friends...
Transcript of EFFECTS OF EXTRACTION AND REFINING ON THE ...I also greatly appreciate my lab mates and friends...
EFFECTS OF EXTRACTION AND REFINING ON THE QUALITY AND COMPOSITION OF MUSCADINE GRAPE SEED OILS AND FLOUR OF THE NOBLE AND CARLOS
CULTIVARS
By
BRIAN K. WADA
A THESIS PRESENTED TO THE GRADUATE SCHOOL
OF THE UNIVERSITY OF FLORIDA IN PARTIAL FULFILLMENT OF THE REQUIREMENTS FOR THE DEGREE OF
MASTER OF SCIENCE
UNIVERSITY OF FLORIDA
2018
© 2018 Brian K. Wada
To my family, Jerry, Lisa, and Michelle, for supporting me throughout my endeavors
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ACKNOWLEDGMENTS
I would like to thank Dr. Liwei Gu for giving me the opportunity to pursue my
master’s degree and for guiding and motivating me as I pursued an entirely new path in
my life. I would like to thank Dr. Yavuz for motivating me and guiding me through my
research. I would also like to thank Dr. Cheryl Rock for giving me the courage to move
across the country and pursue food science. I also greatly appreciate my lab mates and
friends Ruiqi Li, Mohammed Alrugaibah, Shaomin Zhao, Chi Gao,Ye Feng, and Jamie
Klaben. I would finally like to thank my girlfriend Jessica Lee.
I would like to acknowledge Muscadine Products Corporation and Lakeridge
Winery and Vineyard for providing me with muscadine pomace and seeds. I would also
like to thank the Florida Department of Agriculture & Consumer Sciences for providing
funding for this research
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TABLE OF CONTENTS page
ACKNOWLEDGMENTS .................................................................................................. 4
LIST OF TABLES ............................................................................................................ 7
LIST OF FIGURES .......................................................................................................... 8
LIST OF ABBREVIATIONS ............................................................................................. 9
ABSTRACT ................................................................................................................... 10
CHAPTER
1 INTRODUCTION .................................................................................................... 12
Muscadine Grape ................................................................................................... 12 Tocopherol and Tocotrienol .................................................................................... 16
Oil Extraction .......................................................................................................... 13 Oil Refining ............................................................................................................. 15 Phytochemicals in Muscadine Grapes .................................................................... 18
Summary ................................................................................................................ 18 Research Objectives ............................................................................................... 19
2 COMPARING EXTRACTIONS OF CRUDE AND REFINED OIL FROM MUSCADINE SEEDS FROM THE NOBLE AND CARLOS CULTIVARS ............... 23
Background ............................................................................................................. 23 Materials and Methods............................................................................................ 24
Chemicals ......................................................................................................... 24 Sample Preparation .......................................................................................... 24 Oil Extraction .................................................................................................... 25
Peroxide and Free Fatty Acid Content Analysis ............................................... 26 Determination of Fatty Acid Composition ......................................................... 27 Determination of Vitamin E Content ................................................................. 27
Oil Refining ....................................................................................................... 28 Statistical Analysis ............................................................................................ 28
Results and Discussion........................................................................................... 28 Oil Extraction .................................................................................................... 28 Peroxide Values and Free Fatty Acid Concentration ........................................ 30 Fatty Acid Composition .................................................................................... 32 Determination of Vitamin E Content ................................................................. 32
Refining Oil Yield .............................................................................................. 33 Peroxide and Free Fatty Acid Concentration .................................................... 35 Vitamin E Concentration After Refining ............................................................ 35
Summary ................................................................................................................ 37
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3 MUSCADINE GRAPE SEED FLOUR ..................................................................... 52
Background ............................................................................................................. 52
Materials and Methods............................................................................................ 52 Chemicals ......................................................................................................... 52 Preparation of Flour .......................................................................................... 53 Proximate Analysis of Flour .............................................................................. 53 Phytochemical Extraction ................................................................................. 55
Total Phenolic Content ..................................................................................... 55 DPPH Assay ..................................................................................................... 56 HPLC Analysis of Muscadine Flour Phytochemicals ........................................ 56
Results and Discussions ......................................................................................... 57 Proximate Composition of Flour ....................................................................... 57
Total Phenolic Content and Antioxidant Capacity ............................................. 59 Characterization of Muscadine Flour Phytochemicals ...................................... 60
Summary ................................................................................................................ 62
4 CONCLUSIONS ..................................................................................................... 70
LIST OF REFERENCES ............................................................................................... 71
BIOGRAPHICAL SKETCH ............................................................................................ 77
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LIST OF TABLES
Table page
2-1 Extraction yield of seed oil from Noble and Carlos muscadine seeds using different extraction methods ............................................................................... 39
2-2 Impact of extraction and refining on peroxide value and free fatty acids in Noble muscadine seed oil .................................................................................. 40
2-3 Impact of extraction and refining on peroxide and free fatty acid content of Carlos seed oil. ................................................................................................... 41
2-4 Fatty acid composition of Noble seed oil using different extraction methods. ..... 42
2-5 Fatty acid composition of Carlos seed oil using different extraction methods ..... 43
2-6 Impact of different extraction methods on the vitamin E concentration (mg/100 g) of crude Noble seed oil ..................................................................... 44
2-7 Impact of different extraction methods on the vitamin E concentration (mg/100 g) of refined Noble seed oil. .................................................................. 45
2-8 Impact of extraction methods on vitamin E concentration (mg/100 g) of crude Carlos seed oil. ................................................................................................... 46
2-9 Impact of extraction methods on vitamin E concentration (mg/100g) of refined Carlos seed oil .................................................................................................... 47
2-10 Refining yield (%, w/w) of seed oil from Noble and Carlos muscadine seeds at different steps of refining. ............................................................................... 48
3-1 Impact of extraction method on proximate analysis (%, w/w) of Noble seed flour and Carlos seed flour. ................................................................................ 64
3-2 Impact of extraction method on total phenols and antioxidant capacity of Noble seed flour and Carlos seed flour. ............................................................. 65
3-3 Impact of extraction method on phytochemical content (mg/100g) of Noble seed flour ............................................................................................................ 66
3-4 Impact of extraction method on phytochemical content (mg/100g) of Carlos seed flour ............................................................................................................ 67
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LIST OF FIGURES
Figure page
1-1 Chemical Structure of tocopherol isomers ( and tocotrienol isomers
(. ........................................................................................................... 20
1-2 Chemical structure of flavonoid compounds, quercetin and kaempferol, in muscadine grape seeds. .................................................................................... 21
1-3 Anthocyanin compounds found in muscadine seeds .......................................... 22
2-1 Concentrations of tocopherol and tocotrienol in Noble seed oil after the refining process. Results are mean with error bars denoting standard deviation.. ........................................................................................................... 49
2-2 Concentrations of tocopherol and tocotrienol in Carlos seed oil after the refining process.. ................................................................................................ 50
2-3 Peroxide value in Carlos seed oil extracted using enzyme-assisted aqueous extraction with protease after treatment with bleaching earth clay of different concentrations.. .................................................................................................. 51
3-1 HPLC-DAD chromatogram of the anthocyanins in Noble grape seed flour at 520 nm.. ............................................................................................................. 68
3-2 HPLC-DAD chromatogram of the anthocyanins in Noble seed flour and Carlos seed flour at 360 nm. Peaks 1, 2, and 3 were myricetin, quercetin, and kaempferol, respectively. ............................................................................. 69
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LIST OF ABBREVIATIONS
DPPH 2,2-diphenyl-1-picrylhydrazyl
FAME Fatty acid methyl esters
g Gram
g G-force
GAE Gallic acid equivalence
HPLC High performance liquid chromatography
L Liter
g Microgram
L MicroLiter
min Minute(s)
mL Milliliters
nm Nanometer
TE Trolox equivalence
Trolox 6-Hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid
UV Ultraviolet
V Volume
Vis Visible
w Weight
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Abstract of Thesis Presented to the Graduate School of the University of Florida in Partial Fulfillment of the Requirements for the Degree of Master of Science
EFFECTS OF EXTRACTION AND REFINING ON THE QUALITY AND COMPOSITION
OF MUSCADINE GRAPE SEED OILS AND FLOUR OF THE NOBLE AND CARLOS CULTIVARS
By
Brian K. Wada
May 2018
Chair: Liwei Gu Major: Food Science and Human Nutrition
Wine making or juicing using muscadine grapes results in large amounts of
discarded seeds in pomace. Muscadine seeds contain oil that consist predominantly of
polyunsaturated fatty acids and tocopherols. The objective of this research was to
investigate efficient extraction and refining technologies to produce muscadine seed oils
of good quality and characterize muscadine seed oils and flour. Seed oils were
extracted using a Soxhlet extractor by hexane, mechanical press at different moisture
and temperatures, or enzyme-assisted aqueous extraction using different enzymes.
Crude and refined oil was evaluated for peroxide value, free fatty acid content, fatty acid
composition and vitamin E content. Flour was analyzed for proximate composition,
antioxidant capacity, and phytochemicals. Hexane extracted oil resulted in significantly
higher yield for both Noble and Carlos seeds with the least amount of peroxides and
free fatty acids. Linoleic acid accounted for 72-79% total fatty acid in all oils.
Concentrations of tocopherols and tocotrienols in muscadine seed oil ranged from 11.8
to 53.8 mg/100 g and 25.3 to 44.3 mg/100 g, respectively. Oil refining removed
peroxides and free fatty acids but also removed 44-100% and 11-95% of tocopherols
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and tocotrienols, respectively. Flours have up to 17.1% protein and 53.6% fiber. DPPH
values range from 101.3 to 183.3 Mol Trolox/ mg and total phenols range from 10.0 to
37.3 GAE (mg/mL). The predominant anthocyanin isomer and flavonal was malvidin 3,
5-glucoside (167 mg/100 g) and myricetin (235 mg/100 g). Muscadine seeds have the
potential to become a source of antioxidant rich oil and flour.
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CHAPTER 1 INTRODUCTION
Muscadine Grape
The muscadine grape (Vitis rotundifolia) is a grape species indigenous to the
southeast United States and northern Mexico. Muscadine grapes have relatively large
berries with a thicker outer skin and two to six large seeds compared to the common
grape (Vitis vinifera). Muscadine grapes are resistant to disease, require little pesticides,
need little to no irrigation to grow on a farm, and thrive in warmer and humid climates
which is not suitable for Vitis vinifera (Olien, 1990). Grapes are sold in farmers’
markets, roadside stands, and “U-pick” operations, but a majority of muscadine grapes
are used for juice and wine production (Peter C. Anderson, 2013). Wine production
utilizing the muscadine grape in Florida totals 450,000 gallons of wine annually (Mueller,
2014). Extraction of the juice from the muscadine grapes gives a byproduct of pomace,
which consists of the leftover skin, stem, leaves, and seeds. Accounting for 10–20% of
the grapes weight, the pomace is typically put in landfills after the juice has been
extracted (Xu et al., 2014). Cell culture studies showed that phytochemicals of the
muscadine grapes inhibited proliferation of colon cancer cells and induced apoptosis in
them (Mertens-Talcott, Lee, Percival, & Talcott, 2006; Yi, Fischer, & Akoh, 2005).
Additionally, mice studies suggested that the phytochemicals of the muscadine grape
prevent obesity-associated metabolic complications and alleviate bowel inflammation
(Gourineni, Shay, Chung, Sandhu, & Gu, 2012; Li, Kim, Sandhu, Gao, & Gu, 2017; Li,
Sandhu, Gao, & Gu, 2016).
The muscadine grape seeds in pomace contain a large variety of antioxidant
phytochemicals. They are reported to contain hydroxybenzoic acid, quercetin
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rhamnoside, hydrolysable tannins, ellagic acid, and flavan-3-ols and condensed tannins.
(Sandhu & Gu, 2010) The seeds contain 11-15% (w/w) edible oil. Although little
research has been done on the oil, it has been reported that the oil is predominantly
poly-unsaturated fatty acids (68.1-72.5%), and has a fatty acid profile comprised mostly
of linoleic acid (C18:2) (67.9-72.3%) (Zhao et al., 2015). Muscadine seed oil also
contains tocopherol and tocotrienol, classes of vitamin E (Zhao et al., 2015). Extracts of
the oil have been shown to attenuate obesity and exhibit dose-dependent inhibition of
cancer cell growth in vitro (Lutterodt, Slavin, Whent, Turner, & Yu, 2011; Zhao et al.,
2015). The goal of current research is to investigate extraction and refining
technologies to produce muscadine seeds oil of high quality and to characterize the
composition of seed oil and defatted seed flour. Comparison of different concentrations
of peroxide values, free fatty acid values, fatty acid composition, and vitamin E
concentration, will be done in oil before and after refining.
Oil Extraction
There are multiple technologies of oil extraction from lipid containing seeds but
the most common one is mechanical expression. The use of sheer pressure to destroy
oil bodies to release the oil has been a common practice throughout history. Much
larger, scaled up versions are used for industrial purposes and one of the most common
mill types is the continuous screw presses (Ajibola, Eniyemo, Fasina, & Adeeko, 1990).
Screw presses are common as they come in various sizes, are a continuous process,
and requires low maintenance. Screw presses are relatively easy to use as they do not
require chemicals and can be continuously fed. However, screw presses and all other
forms of expression crush oil bodies and extract about 60% of oil depending on
moisture, heat, and material (Ward, 1976). More commonly used in commercial
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operations is solvent extraction using hexane because it is cheap and can retrieve oil at
a yield of 95% with about 95% solvent recovery (Rosenthal, Pyle, & Niranjan, 1996).
However, solvent disposal can be environmentally dangerous and expensive to
continually purchase.
An older form of oil extraction, aqueous extraction, utilizes hot water to release oil
from seeds and allow oils to separate based on the insolubility of oil in water. Recently,
studies have been conducted to determine whether the process can be made viable in
an industrial setting. The technique can be optimized through the uses of enzymes to
breakdown oil containing seeds. Enzymes facilitate release of oil without heat of
mechanical expression or use of hexane (Latif, Diosady, & Anwar, 2008). Yields of
aqueous extraction are typically lower than the other two forms of extraction. However,
since the lower heat preserves bioactive and heat-sensitive components of extracted oil,
there is still research interest in this method.
Previous research has been performed on cold-pressed muscadine seed oil and
hexane extracted muscadine seed oil, but neither considered the effect of extraction
method on the quality of oil (Lutterodt et al., 2011; Zhao et al., 2015). Additionally,
previous research on the enzyme-assisted aqueous extraction of oil from the seeds of
common table grapes has also been conducted, but never applied to the muscadine
seed (Passos, Yilmaz, Silva, & Coimbra, 2009). Muscadine seeds have lower oil
content (13-20%) compared to other seeds such as peanuts (50%). Developing an
efficient extraction method is crucial for muscadine seed oil due to low oil content but
high content of polyunsaturated fatty acids.
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Oil Refining
The refining of edible oils is a process that requires both chemical reactions and
physical separation with the intention to remove oxidation products and other
components that cause off flavors or contribute to the rancidity of oil. There are three
important reactions in refining. They are hydration of phospholipids, neutralization of
free fatty acids, and removal of pigments (Wiedermann, 1981). These three reactions
occur in three separate refining steps: degumming, neutralizing, and bleaching.
Degumming is necessary to remove phospholipids in oil, by adding hot water to
hydrolyze and separate the phospholipids. If they are not removed they can emulsify the
oil or degrade and give the oil a dark color (Zufarov, Schmidt, & Sekretár, 2008).
Neutralization saponifies free fatty acids by using an alkali solution, removing them for
the oil in the form of soap. Free fatty acids are less stable than normal triglycerides and
are thus more likely to oxidize (Sanchez-Machado et al., 2015). Bleaching removes
color containing compounds like chlorophyll, residual phospholipids, and peroxyl
compounds.
Refining requires heating and chemical treatment to remove all undesirable
components that diminish the quality of the oil. However, the refining process also
removes desirable components of the oil, including tocopherol and tocotrienol. Previous
work showed the losses of vitamin E during refining of different types of oil with varying
results (Gogolewski, Nogala‐Kalucka, & Szeliga, 2000; Pestana-Bauer, Zambiazi,
Mendonça, Beneito-Cambra, & Ramis-Ramos, 2012; Puah, Choo, Ma, & Chuah, 2007;
Tasan & Demirci, 2005; Van Hoed et al., 2006). Gogolewski, Nogala-Kalucka et al.
observed that the refining of rapeseed oil had losses of 30% of total tocopherol from the
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oil. In the work done by Puah, Choo et al. tocopherol concentrations were observed to
decrease at every step of the oil refining process.
Tocopherol and Tocotrienol
Muscadine grape seed oil is rich in tocopherol and tocotrienol with variances
among cultivars and growing seasons. The structure for -tocopherol and -tocotrienol
are shown in figure 1-1 and 1-2. Both tocopherol and tocotrienol occur naturally in four
isomers Among the isomers of tocopherol, -tocopherol has been the
main focus of previous research since tocopherol is the most predominant vitamin E
isomer in plasma and tissue of humans. Tocopherol’s structure allows it to interact
with the cell membrane and trap free radicals more efficiently than the other isomers,
making it the more preferentially absorbed form of vitamin E in humans (Booth &
Bradford, 1963). Research on tocopherol primarily notes its antioxidant capabilities
and anti-inflammatory capabilities (Reiter, Jiang, & Christen, 2007). In human studies,
tocopherol supplementation has been shown to improve indicators of immune
function including the increase of interleukin 2, a signaling molecule that regulates the
activity of white blood cells, and decrease prostaglandin E2, a pro-inflammatory
mediator (Meydani et al., 1990). Although tocopherol is the main isomer used in
vitamin E supplementation, tocopherol, a less predominant form of vitamin E, has
been shown to have the capability of having a bioavailability of up to 30-50% (Burton et
al., 1998). It is naturally found in corn and soybean oil, and in diets of the United states
where use of those oils are common it has an estimated 20% of total vitamin E activity
(Bieri & Evarts, 1974). Additionally, tocopherol has observed to inhibit
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cyclooxygenase activity, meaning it also has anti-inflammatory properties (Jiang,
Christen, Shigenaga, & Ames, 2001).
Tocotrienols are structurally similar to tocopherol with a common chromanol head
and a side chain at the C2 position, but the two have different side chains (Theriault,
Chao, Wang, Gapor, & Adeli, 1999). Similarly, tocotrienols are primarily known for their
antioxidant capabilities, however they have other health promoting properties.
Tocotrienols have been reported to lower plasma cholesterol levels and other risk
factors of cardiovascular disease (Theriault et al., 1999). Recent studies suggest that
various forms of tocotrienol can protect against emphysema, obesity-related
inflammation, and oxidative stress (Goon, Azman, Ghani, Hamid, & Ngah, 2017; Peh et
al., 2017; Ramalingam et al., 2017).
Muscadine seed oil is a rich source of tocopherols and tocotrienols in
comparable to rice bran oil. In previous research, a tocotrienol-rich fraction of
muscadine seed oil extract was found to reduce adipocyte formation and adipogenesis
(Zhao et al., 2015). The treatment of human-adipose stem cells with the tocotrienol
fraction of muscadine seed oil showed significant reduction of transcription factors
responsible for adipogenesis. Another study done by Lutterodt et al. showed that
extracts from muscadine seed flour and oil inhibited the growth and proliferation of
cancer cells in vitro. Studies on the health benefits of muscadine seed oil typically used
oil extracted by hexane or cold pressing, however research on how different oil
extraction methods may impact the bioactive components of the oil have not been
conducted.
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Phytochemicals in Muscadine Grapes
Phytochemicals are biologically-active, non-nutritive secondary metabolites in
plants that contribute to color and a bitter astringent flavor (Damodaran, Parkin, &
Fennema, 2007). Research regarding phytochemicals has demonstrated their ability to
reduce the risk of cancer, cardiovascular disease, Alzheimer’s, and other chronic
diseases associated with complication from oxidative stress (Liu, 2003). Muscadine
grapes possess a unique phytochemical profile compared to other member of the Vitis
species of grapes (Hudson et al., 2007). Muscadine grape seeds contain quercetin,
kaempferol, and anthocyanin 3,5-diglucosides (Figure 1-3 and 1-4) (Li et al., 2017).
Phytochemicals extracted from the muscadine grape have been shown to reduce
inflammation and metabolic complications and in vivo and adipogenesis in vitro
(Gourineni et al., 2012; Li et al., 2017; Zhao et al., 2015). Within the muscadine grape,
approximately 80% of the phytochemicals are located within the seeds (Sandhu & Gu,
2010).
Summary
Muscadine grape pomace is an underutilized byproduct of wine making. Seeds
and skin in pomace contain high concentration of polyphenols. In addition, seeds
possess oils consisting of predominantly polyunsaturated fatty acids and rich in
tocopherol and tocotrienol.
The extraction method of the oil is crucial as it dictates the yield and the quality of
the resulting oil. No studies have been conducted to determine the effect different
extraction technologies on the yield and quality of muscadine seed oil. Refining the oil
will also improve oxidative stability and ideally safe for consumption. It was unknown
how refining impacts the quality of oil and the content of vitamin E.
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Extraction of oil from seeds results in defatted seeds, which can be ground and
sieved to make flour. Little previous research has been done on the defatted seed flour
of the muscadine grape seed.
Research Objectives
In this research, oils were extracted from muscadine seeds of two cultivars
(Noble and Carlos) using three oil extraction technologies. Noble is a purple grape
variety and Carlos is a bronze grape variety. Crude oils were refined to meet the quality
standards of edible oil. Quality and composition of the oils and seed flours were
characterized. The specific objectives of the research were:
1. To evaluate the yield of crude oil from Noble and Carlos seeds using Soxhlet
extraction with hexane, continuous screw pressings, and enzyme-assisted
aqueous extraction and to assess oxidative stability, fatty acid composition and
vitamin E concentration
2. To investigate the effects of refining on the oils oxidative stability, fatty acid
composition, and vitamin E concentration.
3. To assess the proximate composition, antioxidant capacity, and polyphenol
profiles in defatted seed flours.
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-Tocopherol -Tocopherol l
-Tocopherol -Tocopherol
-Tocotrienol -Tocotrienol
-Tocotrienol -Tocotrienol
Figure 1-1. Chemical structure of tocopherol isomers ( and tocotrienol isomers
(.
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Quercetin Kaempferol
Figure 1-2. Chemical structure of flavonoid compounds, quercetin and kaempferol, in muscadine grape seeds.
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Anthocyanins R1 R2 R3 R4
Delphinidin 3,5-diglucoside OH OH glucose glucose
Cyanidin 3,5-diglucoside OH H glucose glucose
Petunidin 3,5-diglucoside OCH3 OH glucose glucose
Pelargonidin 3,5-diglucoside H H glucose glucose
Peonidin 3,5-diglucoside OCH3 H glucose glucose
Malvidin 3,5-diglucoside OCH3 OCH3 glucose glucose
Figure 1-3. Anthocyanin compounds found in muscadine seeds
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CHAPTER 2 COMPARING EXTRACTIONS OF CRUDE AND REFINED OIL FROM MUSCADINE
SEEDS FROM THE NOBLE AND CARLOS CULTIVARS
Background
Over 90% of muscadine grapes are used for making wine, which requires
fermenting grapes or grape juicing and discarding the pomace. Each year
approximately 500 tons of pomace are discarded, 300 tons of which are seeds (Zhao et
al., 2015). The seeds contain 13-15% edible oil, rich in antioxidants. It is possible to
retrieve approximately 38 tons of muscadine seed oil and 250 tons of defatted seed
flour from this currently wasted material (Peter C. Anderson, 2013).
Muscadine seed oil is known to have many forms of tocopherol and tocotrienol.
These compounds are known for their antioxidant abilities and capacity to prevent
cancer, heart disease, and inflammation (Burton et al., 1998; Goon et al., 2017; Reiter
et al., 2007). Previous research supports that it is essential to choose the right
extraction method to obtain oil with high yield as well as preserve beneficial components
like vitamin E.
Refined edible oils are composed of triglycerides with little to no color, odor, or
oxidation products that cause off flavors and odors. Crude oil must undergo a multiple
step refining process to reach this state. The first step is degumming, where hot water is
added to crude oil to bind and aggregate phosphatides in order to separate them from
oil (Zufarov et al., 2008). Free fatty acids in a crude oil must then be neutralized by
alkali so they be removed as soaps from the oil (Sanchez-Machado et al., 2015). The
third necessary refining step is bleaching. Activated carbon or bleaching earth clay are
used to absorb colored compounds, residual soaps and phosphatides, and other
oxidation products (Rossi, Gianazza, Alamprese, & Stanga, 2001).
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Refining steps remove the unwanted products in oil to make them more
appealing and pleasing to taste. However, it may also remove desirable lipids like
vitamin E. In this study, different oil extraction methods were used to obtain muscadine
seed oil from the seeds of two cultivars (Noble and Carlos). The objectives of this
research were to compare the extraction efficiency of different methods, determine
peroxide values and free fatty acids, analyze the fatty acid composition, determine
vitamin E concentrations, and evaluate effects of refining on oil quality.
Materials and Methods
Chemicals
N-Hexane, methanol, acetic acid, chloroform, saturated potassium iodide, starch,
ethanol, sodium hydroxide, 0.5 M sodium methylate in methanol, isooctane, sodium
bisulfate, Folin-Ciocalteu reagent, phenolphthalein, and formic acid were purchased
from Fischer Scientific (Pittsburg, PA, USA). Tocopherol and tocotrienol standards were
obtained from Santa Cruz Biotechnology Inc. (Dallas, TX, USA). Enzymes cellulase,
protease, pectinase, and hemicellulase were purchased from Sigma-Aldrich (St. Louis,
MO, USA). Muscadine grape pomace of the Carlos cultivar and seeds of the Noble
cultivar were obtained from Lakeridge Winery and Vineyard (Clermont, FL, USA) and
dried muscadine seeds of the Noble and Carlos cultivar were obtained from Muscadine
Products Corporation (Wray, GA, USA).
Sample Preparation
Wet Carlos pomace and Noble seeds were obtained from Lakeridge Winery and
Vineyard (Clermont, FL, USA) and dry pomace was obtained from Muscadine Products
Corporation (Wray, GA, USA). Large twigs and skins were removed from wet Carlos
pomace by sifting through poultry netting with 1x1 inch openings. Noble seeds were
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separated out after the fermenting process, where they were placed with juice and skins
to ferment. The sifted Carlos pomace and Noble seeds were placed in separate baking
pans and placed in an oven to dry at 77°C for 16 hours. Seeds were separated from the
rest of the dried pomace by wind sifting. Dried seeds were mixed with their respective
cultivar from Florida and Georgia in a 1:3 ratio (w:w) to obtain enough samples for all
methods of extraction. A portion of Noble and Carlos were separated and mixed with
deionized water, to moisten seeds to 13% and 16% (w/w). The seeds were mixed in a
bucket and sealed until the moisture was equilibrated. Prior to extractions seeds were
grinded using a RHH-1000 multi-function grinder (Enerburg, Guangzhou, China).
Oil Extraction
For mechanical expression, a Tokul Tarim Ekotok 1 continuous oil screw press
(Izmir, Turkey) was used. Pressing was conducted at 85° C, 90° C, 105° C, and 125° C
with initial moisture content of 9.83 ± 0.25 % and 10.3 ± 1.2 % for Noble and Carlos
seeds, respectively. Additional pressings were done at 90°C for at moisture contents of
13 % and 16%, wet basis. Soxhlet extractions were performed according to AOCS
official method Ba 3-38 (Firestone & American Oil Chemists, 2011). Seeds were grinded
using a RRH-1000 high-speed multifunction grinder (Enerburg, Guangzhou, China) and
approximately 50 g were placed in a fiberglass thimble and into the Soxhlet sample
holder. Samples were refluxed in Soxhlet extractors for 8 hours before hexane was
evaporated using a Buchi R-II rotary evaporator (Delaware, USA). A previously reported
enzyme-assisted aqueous extraction method was used with modification (Passos et al.,
2009). Seeds were grinded using the RRH-1000 high-speed multifunction grinder and
50 g were placed in 950 mL mason jars with the enzyme at 1% concentrations (v:w).
250 mL of citrate buffer with a pH of 5.0, 4.5, 4.0, 5.0, and 4.5 were used for cellulase,
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hemicellulase, pectinase, protease, and a cocktail of all 4 enzymes, respectively. The
mixture was incubated in a reciprocal water bath shaker model R-76 (Edison, New
Jersey, USA) for 15 hours at 37° C, 40° C, 25° C, 45° C, and 37°C for cellulase,
hemicellulase, pectinase, protease, and a cocktail of all 4 enzymes, respectively. After
incubation, the mixture was placed in 500 mL polycarbonate centrifuge tubes and
centrifuged for 30 minutes at 1,450 g. The supernatant was mixed with 50 mL of hexane
in a centrifuge tube and centrifuged again. The upper hexane layer was collected in a
round bottom flask and evaporated using a Buchi R-II rotary evaporator to retrieve oil.
Oil yield was expressed as percentage of the weight of the oil obtained relative to the
dry weight of seeds extracted.
Peroxide and Free Fatty Acid Content Analysis
Peroxide values were determined using an AOAC official method 965.33
(International, 1995). Briefly, 5 g of oil were placed into a 250-mL Erlenmeyer flask and
mixed with 30 mL of acetic acid and chloroform (3:2, v/v). The solution was mixed
before adding 0.5 mL of saturated potassium iodide and stirring for one minute. After
that, 30 mL of water were added stirred with 0.5 mL of starch were added producing a
dark black color. The solution was then titrated using 0.10 M sodium thiosulfate until
clear. Titration volume was used to calculate peroxide content in mEq/kg.
Free fatty acid concentration was determine using an AOAC official method
940.28 (International, 1995). Briefly, five grams of oil were placed into a 250 mL
Erlenmeyer flask with 50 mL of ethanol. Phenolphthalein indicator was added to the
solution and titrated with 0.1M sodium hydroxide until a faint pink color was formed.
27
Determination of Fatty Acid Composition
Fatty acid methyl esters (FAMEs) were prepared for both crude and refined oils
by basic methylation procedure. Briefly, 1 mL of sodium methylate in methanol (0.5 N)
was mixed with approximately 10 mg of extracted oil. The mixture was allowed to stand
in room temperature for 10 min, followed by the addition of 500 µL isooctane and 200
µL sodium bisulfate (5%).The mixture was centrifuged for 3 min at 14,500x g and the
upper isooctane layer containing the FAMEs was transferred to GC vials and stored at
−20°C until further analysis by gas chromatography (GC). A gas chromatography (GC)
(6890 Series, Agilent, and Wilmington DE) equipped with a flame ionization detector
using a DB-225MS column (30 mx0.25 mm x 0.25 m) at a flow rate of 0.8 mL/min was
used to separate 1 L of injected FAMEs. The oven temperature program began with an
initial temperature of 120 °C then temperature was increased at a rate of 4°C/min to a
final temperature of 220 °C with a hold time of 35 min. Fatty acids were identified by a
comparison of the retentions times with a standard mixture (Supleco® 37 component
Fatty Acid Methyl Ester Mix, Sigma-Aldrich, St. Louis, MO).
Determination of Vitamin E Content
Vitamin E content was determined for both crude and refined oils using a HPLC
system equipped with fluorescence detector and normal phase column (Luna 5 m
silica 100 Å, 250 x 4.6mm) as previously described.(Zhao et al., 2015) Briefly, seed oils
were weighed and dissolved in 10 mL of hexane. Separation and quantification was
conducted with a mobile phase consisting of hexane, isopropanol, ethyl acetate, and
acetic acid (97.6:0.8:0.8:0.8; v/v/v/v) at 1 mL/min. The wavelength was set at 270 nm for
excitation and 330 nm for emission.
28
Oil Refining
Degumming, neutralizing, and bleaching of the oil was done according to
Sanchez-Machdo et. al with modifications.(Sanchez-Machado et al., 2015) Crude
muscadine seed oil was heated in a water bath to 70 °C and boiling water was added
(20%, v/v). The mixture was stirred for 10 minutes before being placed in a 50 mL
centrifuge tube and oil was recovered by centrifugation at 1450x g for 15 minutes. Oil
was vacuum filtered with Whatman No. 1 filter paper and recovered. Neutralization was
done by adding a pre-determined amount of 20% sodium hydroxide and heated to 65°C
under reduced pressure. After 15 minutes the oil was washed with deionized water
(20%, v:v). After oil was separated from water and soap by centrifugation at 900 g for 15
minutes, the oil supernatant was then vacuum filtered through Whitman No. 1 filter
paper. Bleaching was performed with 10% bleaching earth clay (w/w) that was stirred
into oil and heated to 110°C for 10 minutes. After the oil was centrifuged and vacuum
filtered a final time. Collected refined oil was placed in screw top tubes and placed the
freezer after nitrogen flushing.
Statistical Analysis
Results are presented as mean ± standard error of the mean. One-way ANOVA
with Tukey’s multiple comparison tests were performed with JMP software (Version
13.0, SAS Institute Inc. Cary, NC). A difference with p < 0.05 was considered significant.
Results and Discussion
Oil Extraction
Soxhlet extraction using hexane was the most efficient method for obtaining oil in
both Noble and Carlos seeds (Table 1). Hexane is used to extract oil in industrial
settings because it can extract over 95% oils from seeds (Rosenthal et al., 1996). The
29
mechanical expression of Noble seeds had the highest yield at 85° at the initial
moisture content of 9.83% (wet basis). Expression of Noble seeds were only
significantly different among expression temperatures and conditions from the greatest
yield at 85°C (7.08%) and the lowest yield 125°C (6.11%). Expression at 85°C was
likely gave the highest yield among expressions of Noble seeds, because higher
temperatures can damage oil bodies and prevent them from releasing their oil.
Expression of Carlos seeds were at 90 °C and 125 °C with a higher oil yield than all
other expression extractions at 90 °C and at a moisture content of 13%. Higher moisture
contents prevent solvents from accessing oils in seeds, but a higher moisture content in
seed expression can bind the seeds during expression. This causes an increase in
pressure in the screw chamber, thus increasing the oil yield. This may be the case with
the Carlos seeds that were pressed at 90°C with a moisture content of 13% (Ajibola et
al., 1990).
Among enzyme-assisted aqueous extractions, the use of the enzyme cocktail
gave a higher oil yield (3.73 %) from Noble seeds than any individual enzyme. Carlos
seed oil yield utilizing the enzyme cocktail (9.31 %) was significantly greater than three
forms of mechanical expression. Oil extracted using aqueous extraction is surrounded
by buffer, that bind and aggregate phospholipids that would be considered in the yield of
crude Soxhlet oil. Hydrolytic enzymes are not as effective at penetrating lipid bodies and
obtaining oil as hexane, also resulting in a lower yield. Enzyme-assisted aqueous
extraction using a cocktail of all four enzymes (cellulase, hemicellulase, protease,
pectinase) obtained significantly higher yield than the use of a single enzyme for both
Noble and Carlos seeds. By using all four enzymes in a cocktail, the structural
30
polysaccharides making up the cell wall and proteins that form the lipid body
membranes were hydrolyzed, resulting in greater yield than a single enzyme (Passos et
al., 2009). In both oils, there was no significant difference in the yield of oils extracted
using one enzyme. Extraction using only one enzyme likely left either the
polysaccharide cell walls or lipid containing protein bodies intact, decreasing oil yield.
Noble seeds were not as responsive to the enzymes, likely due to a higher polyphenol
content than Carlos seeds (Sandhu & Gu, 2010). Similar polyphenols from other
sources have been reported to inhibit digestive enzymes including protease (Mcdougall
& Stewart, 2005).
Peroxide Values and Free Fatty Acid Concentration
Hydroperoxides are the primary products of lipid oxidation that eventually break
down into alcohols, aldehydes, free fatty acids, and ketones as secondary products
(Damodaran et al., 2007). Both peroxide values and free fatty acids are used to test the
extent of rancidity in oil samples. The peroxide values of grape seed oil extracted from
Noble and Carlos seeds are presented in Tables 2-2 and 2-3. Oil extracted from freeze-
dried seeds using a Soxhlet apparatus and hexane possessed lowest peroxide values
than all other oils collected, including seeds dried in an oven and extracted in the same
manner. This held true for both freeze dried Noble seed oil (2.33 mEq/kg) and Carlos
seed oil (6.33 mEq/kg). It suggests that drying the seeds in a conventional oven causes
oxidation of oil in seeds. Among seeds dried in the oven, Soxhlet extraction using
hexane had a significantly lower peroxide value than other forms of oil extraction
methods. Oils extracted using enzyme-assisted method had significantly higher
peroxide values than all other extractions for Noble seed oil and for all extractions
except expression at 125°C for Carlos seed oil. This data suggested that oil oxidation
31
occurred during the enzymatic incubation period. Similar observations were made in
previous studies on enzyme-assisted aqueous extraction (Embong & Jelen, 1977).
Screw expression exposes the seeds and oil temperatures of 85°C or more in
atmospheric conditions promoting the formation of hydroperoxides. Enzyme-assisted
aqueous extracted oil possessed even higher levels of peroxide formation, likely forming
during the 15 hour incubation period.
Free fatty acid content of muscadine grape seed oil from seeds of the Noble and
Carlos cultivars are presented in Tables 2-2 and 2-3. Soxhlet extractions utilizing
hexane had significantly less free fatty acid than other forms of extraction with 2.59%
and 0.99% for Noble and Carlos seed oil, respectively. Expression and enzyme-
assisted aqueous extraction had a significantly higher free fatty acid content.
Mechanical expression at 125°C had the greatest percentage for both cultivars, likely
since the high temperature and direct exposure to the oil promoted free fatty acid
formation. Free fatty acids content of the Noble and Carlos seed oil ranged from 2.59-
8.65% and 0.99-6.30%, respectively. Muscadine seed oil had lower free fatty acid
content than observations made in previous studies of hexane extracted grape seed oil
(Gómez, López, & de la Ossa, 1996). Thermal degradation is a common cause of free
fatty acid formation in oil. Long term exposure to incubation temperatures causes
significantly more free fatty acids to form in enzyme-assisted aqueous extracted oil.
Similarly, exposure to expression temperatures result in free fatty acid formation
(Nawar, 1969). Screw expressed oils showed patterns of thermal degradation, since
expression at higher temperatures resulted in higher free fatty acid content in both
Noble and Carlos seed oil.
32
Fatty Acid Composition
Fatty acid results (Tables 2-4 and 2-5) showed that polyunsaturated fatty acids
ranged from 72.9-74.0% and 73.3-79.3% for Noble and Carlos seed oil, respectively.
Monounsaturated fatty acids were the next most abundant for Noble seed oil (15.4-
16.6%) and Carlos seed oil (14.4-15.7%), followed by saturated fatty acids ranging from
9.35-10.8% and 10.94-12.31%, respectively. In Noble seed and Carlos seed oils,
linoleic acid (C18:2) is the most predominant (72.9-74.0% and 73.3-79.3%). The
following most abundant fatty acids are oleic (C18:1), palmitic (C16:0), and steric
(C18:0) acids, with ranges of 15.4-16.6% and 14.4-15.7%, 6.79-7.13% and 6.94-7.69%,
and 2.55-3.75% and 4.00-4.90% for Noble and Carlos seed oil, respectively. For oils
from the seeds of both cultivars, no significant differences were found among the fatty
acid percentages of different extraction methods. The results were similar to previously
reported fatty acid compositions (Lutterodt et al., 2011; Zhao et al., 2015). Fatty acid
profiles of Noble and Carlos seed oil suggest that they would be more susceptible to
oxidation. Linoleic acid is 10 times more susceptible to oxidation than oleic acid due to
its unconjugated double bonds. The oils susceptibility to oxidation could be responsible
for the oxidation that occurred during the drying process, screw expression, and
enzyme-assisted aqueous extraction.
Determination of Vitamin E Content
Concentrations of vitamin E in muscadine grape seed oil for both the Carlos and
Noble cultivars were analyzed by normal-phase HPLC (Tables 2-6, 2-7, 2-8, and 2-9).
Vitamin E in Noble seed oil were predominantly γ-tocopherol, ranging from 23.0-42.2
mg/100g. Noble seed oil had the highest concentration of γ-tocopherol when extracted
by the aqueous extraction using cellulase (42.2 mg/100g), followed by Soxhlet
33
extraction using hexane (39.8 mg/100g), and aqueous extraction using hemicellulase
(38.0 mg/100g). Noble seed oil extracted at 90°C at a moisture content of 16%
possessed significantly higher amounts of -tocopherol than any other oil extracted with
expression. Carlos seed oil was predominantly composed of α-tocotrienol, γ-
tocopherol, and γ-tocotrienol, with ranges of 9.35-18.9 mg/100g, 9.25-25.4 mg/100g,
and 15.8-19.7 mg/100g, respectively. The amount of γ-Tocotrienol in Carlos seed oil
showed no significant difference among various extraction methods. The highest
concentration of α-Tocotrienol was seen in the oil extracted by aqueous extraction with
assistance from hemicellulase (16.6 mg/100 g), protease (18.9 mg/100 g), and
pectinase (18.2 mg/100 g), and the combination of all four enzymes into a cocktail (15.1
mg/100 g). γ-Tocopherol had the highest concentration in oil extracted by the aqueous
method assisted by protease (25.4 mg/100 g) and pectinase (23.2 mg/100 g).
Tocopherol and tocotrienol concentrations were lower than previously reported values
from muscadine seed oil extracted by cold hexane (Zhao et al., 2015). This was likely
due to difference in extraction and analysis methods as well as vitamin E content in
seeds. This data suggests that enzymatic aqueous extraction is a better oil extraction
method for preserving tocopherol and tocotrienol in muscadine seed oil. Thermal
degradation is likely the cause of lower tocopherol and tocotrienol concentrations in the
oil, as enzyme-assisted aqueous extraction utilizes the least amount of heat.
Refining Oil Yield
Degumming is the first step of oil refining. It utilizes water to aggregate and
separate phospholipids from the oil.(Wiedermann, 1981) The “gum” removed from oil
contains water, phospholipids, and triglycerides. After degumming step, enzyme-
34
assisted aqueous extracted oil showed the highest yield for oils extracted from seeds of
both cultivars (Table 2-10). Enzyme-assisted aqueous extracted oil is separated from
the muscadine seeds by enzymatic hydrolysis in a citrate buffer. Water buffer
aggregated a majority of the phospholipids from the oil before the degumming step
(Latif et al., 2008). Data suggests that phospholipid content is higher than in the oil from
Vitis vinifera seeds (1%) (Ohnishi, Hirose, Kawaguchi, Ito, & Fujino, 1990). It is likely
that an emulsification of a portion of muscadine seed oil and water formed during
mixing, resulting in loss of triglycerides and low yield of oil after degumming. Based on
the data, muscadine grape seed oil could be a potential source of phospholipids, which
has been shown to benefit cognitive function and cardiovascular health (Muldoon et al.,
2010).
Neutralization removes free fatty acids by utilizing a low pressure heated
environment and an alkali solution (Sanchez-Machado et al., 2015). Neutralization
showed similar yields among oils of different extraction methods. However,
neutralization did remove more than the free fatty acids which accounted for 1-9% of the
oil. Losses of oil were likely due to excess alkali treatment being used during the
removal of free fatty acids and losses of oil sticking to the evaporation flask and being
absorbed by the filter paper.
Using bleaching earth clay, the oils are separated from hydroperoxides as well
as trace metals, and any remnant soaps and phosphatides (Rossi et al., 2001). Yield
after bleaching was only statistically significant between the two types of extraction
methods that required degumming (Soxhlet and screw press expression) and enzyme-
assisted aqueous extracted oil, for oil from both cultivars. Bleaching yields were similar
35
to previously reported work (Sanchez-Machado et al., 2015). Bleaching losses were
likely due to oil being absorbed by filter paper as well as the bleaching earth clay.
Peroxide and Free Fatty Acid Concentration
The refining process was effective in removing free fatty acids and peroxides
from the initial crude oil as seen in Tables 2-2 and 2-3. Bleaching earth clay effectively
removed peroxides in oil from seeds of both cultivar with values ranging from 0.00 to
0.06 (mEq/kg oil). Free fatty acids were also effectively removed ranging from 0.00 to
0.07 (% as oleic acid w/w). Utilizing caustic sodium hydroxide and a low-pressure
container with heat applied, free fatty acids were both neutralized and evaporated to be
removed from the oil (Sanchez-Machado et al., 2015). According to section 2 of the
codex standards, grape seed oil derived from grape seeds (Vitis vinifera), can have a
peroxide value of up to 10 mEq/ kg oil and 0.3% free fatty acids expressed as oleic acid
(Alimentarius, 1999). Refined muscadine seed oil from both the Noble and Carlos
cultivar are within quality standards. Less refining could be done to the oil to preserve
more tocopherol and tocotrienol, while still keeping the oil within standards. However, by
refining well below standards oil will remain oxidatively stable longer.
Vitamin E Concentration After Refining
Refining is an effective way to remove oxidative products and other unwanted
components from crude oil. However, the refining process also decreases the
concentration of vitamin E within the oil. Total tocopherol and tocotrienol concentrations
after refining are shown in Figures 2-1 and 2-2. Refined Noble seed oil extracted using
the Soxhlet method had a vitamin E retention of 45.8% of total tocopherol and
tocotrienol. After refining, -tocopherol was still the most predominant form of vitamin E
in the oil (18.2 mg/100 g), followed by the more bioactive forms -tocotrienol (9.80
36
mg/100 g) and -tocopherol (6.89 mg/100 g). Refined Noble seed oil extracted by the
Soxhlet method and screw press expression at 105°C had significantly greater retention
than all other oils of different extraction methods, followed by all other forms of
expression. Enzyme-assisted aqueous extracted oils had significantly lower vitamin E
retention than all other Noble seed oils.
Carlos seed oil had significantly greater vitamin E retention in refined Soxhlet
extracted oil. Carlos seed oil had greatest retention of tocopherol and tocotrienol in
Soxhlet extracted oil (70.8%) followed by enzyme assisted aqueous extracted oil using
an enzyme cocktail (40.5%) and continuous screw pressed oil at 105°C (26.5%). The
predominant form of vitamin E in refined Soxhlet extracted oil was -tocotrienol (13.8
mg/100g) followed by, -tocopherol (8.04 mg/100g), and -tocotrienol (7.42 mg/100g)
Although refined Soxhlet extracted oil had greater retention of vitamin E in Carlos seed
oil, it should be noted that Noble seed oil had higher initial concentrations. Refined
Soxhlet extracted oils likely had higher retentions of vitamin E, because they possessed
lower peroxide and free fatty acid concentrations. A lower peroxide concentration could
mean there was less oxidation of the oils to diminish vitamin E concentrations. Lower
free fatty acid concentrations would require less exposure to a caustic base during
refining; minimal exposure to a caustic base could increase retention of tocopherol and
tocotrienol. The bleaching process likely contributed to the loss of tocopherols and
tocotrienols. Bleaching earth clay in concentrations of 10% (w/w) were needed to
remove peroxides from the oil (Figure 2-3). Concentrations from 1-5% of activated
carbon or bleaching earth clay were used in the oil refining process in past work (Rossi
et al., 2001; Sanchez-Machado et al., 2015). Low concentrations of bleaching earth clay
37
have been reported to have a minor effect on tocopherol and tocotrienol concentrations,
but greater concentrations of bleaching earth clay have been shown to decrease
tocopherol and tocotrienol levels (Wei, May, Ngan, & Hock, 2004).These findings
support previous work that chemical and physical oil refining decrease tocopherol and
tocotrienol content in oil (Tasan & Demirci, 2005). Tocopherol and tocotrienol
concentrations are likely lower than previous findings, due to the initial oxidation of the
oil during seed drying and during the following oil extraction methods. Further loss of
tocopherol and tocotrienol likely occurred during neutralizing and bleaching, with caustic
base and bleaching earth clay altering and removing it from the oil.
Summary
Our results indicate that the oil extraction method and conditions affect yield,
peroxide and free fatty acid content, and vitamin E concentration. However, the type of
extraction does not produce significant changes in the fatty acid composition of the oil.
Soxhlet extraction using hexane was successful at obtaining the highest yield for both
Noble and Carlos seed oil while maintaining lower peroxide and free fatty acid
concentration. Additionally, vitamin E content was highest in oil extracted using a
Soxhlet apparatus and hexane. Refining was shown to use up a considerable amount of
oil, especially in the degumming step, but was able to successfully remove peroxides
and free fatty acids from the oil. Refining also proved to diminish vitamin E
concentrations to varying degrees in the muscadine seed oils of different extraction
methods. Muscadine seed oil has the potential to be a tocopherol and tocotrienol rich oil
for culinary or cosmetic purposes. Findings suggest that tocopherol and tocotrienol
concentrations could be preserved with optimized drying and extraction conditions.
38
Additionally, findings support that muscadine seed oil could be a potential source of
phospholipids.
39
Table 2-1. Extraction yield of seed oil from Noble and Carlos muscadine seeds using different extraction methods
Oil Extraction Methods Extraction yield (%, w/w dry base)
Noble Carlos
Soxhlet extraction
Hexane 11.1 ± 0.9a 13.9 ± 0.5a
Screw expression
85°C 7.08 ± 1.92b, AB 8.62 ± 0.45bc
90°C 7.21 ± 0.26b, A 9.52 ± 1.00bc
90°C at 13% Moisture* 5.27 ± 0.6bcd, AB 9.77 ± 0.68b 90°C at 16% Moisture 4.77 ± 0.42cd, B 7.69 ± 0.48c 105°C 5.22 ± 0.23cd, AB 8.30 ± 1.53bc
125°C 6.11 ± 0.25bcd, AB 10.0 ± 0.59b
Enzyme-assisted aqueous extraction Enzyme Cocktail 3.73 ± 0.25de,A 9.31 ± 0.39bc, A Cellulase 1.65 ± 0.08f, B 3.82 ± 0.44d, BC
Hemicellulase 2.27 ± 0.39ef, B 3.55 ± 0.21d, C
Pectinase 2.05 ± 0.34ef, B 4.13 ± 0.31d, BC Protease 1.56 ± 0.08f, B 4.65 ± 0.13d, B
All data represents means ± standard deviation (n=3). Oil yield was expressed as percentage of the weight of the oil obtained relative to the dry weight of seeds extracted. Noble and Carlos seeds were dried to an initial moisture content of 9.83 ± 0.25% and 10.3 ± 1.2%, respectively. Different lower-case superscripts denote difference across extraction types. Different upper case superscripts denote difference within the same extraction type at p ≤ 0.05 using Tukey's test.
40
Table 2-2. Impact of extraction and refining on peroxide value and free fatty acids in Noble muscadine seed oil
Oil extraction methods Peroxide value (mEq/kg oil) Free fatty acid (% as oleic acid w/w)
Unrefined oil Refined oil Unrefined oil Refined oil
Soxhlet using extraction hexane
Freeze dried seeds 2.33 ± 1.15h, B n/a n/a n/a
Air dried seeds 17.0 ± 0.0g, A 0 .00 ± 0.00 2.59 ± 0.08j 0.00 ± 0.00
Screw expression
85°C 29.3 ± 0.6d, A 0 .00 ± 0.00 4.09 ± 0.00i, F 0.00 ± 0.00
90°C 23.0 ± 2.0ef, BC 0.00 ± 0.00 6.49 ± 0.14f, D 0.00 ± 0.00
90°C at 13% Moisture 19.0 ± 0.0fg, D 0.00 ± 0.00 6.77 ± 0.00e, C 0.02 ± 0.04 90°C at 16% Moisture 25.7 ± 1.2de, B 0.03 ± 0.06 6.25 ± 0.08g, E 0.02 ± 0.04 105°C 19.7 ± 1.2fg, D 0.03 ± 0.06 7.47 ± 0.00d, B 0.05 ± 0.04 125°C 21.0 ± 0.0efg, CD 0.03 ± 0.06 8.65 ± 0.08a, A 0.02 ± 0.04 Enzyme-assisted aqueous extraction Enzyme Cocktail 52.3 ± 5.8b, B 0.00 ± 0.00 8.65 ± 0.08a, A 0.00 ± 0.00 Cellulase 43.0 ± 0.0c, C 0.03 ± 0.06 7.71 ± 0.08c, C 0.05 ± 0.04 Hemicellulase 61.7 ± 1.2a, A 0.03 ± 0.06 6.49 ± 0.00f, D 0.00 ± 0.00 Pectinase 63.7 ± 1.2a, A 0.03 ± 0.06 8.18 ± 0.00b, B 0.05 ± 0.04 Protease 59.0 ± 0.0a, AB 0.03 ± 0.06 5.97 ± 0.08h, E 0.00 ± 0.00
All data represent means ± standard deviation (n=3). Initial moisture content of dried Noble seeds was 9.83 ± 0.25%. Different lower-case superscripts denote difference across extraction types. Different upper case superscripts denote difference within the same extraction type at p ≤ 0.05 using Tukey's test. n/a is not applicable
41
Table 2-3. Impact of extraction and refining on peroxide and free fatty acid content of Carlos seed oil.
Oil extraction methods Peroxide value (mEq/kg oil) Free fatty acid (% as oleic acid w/w)
Unrefined oil Refined oil Unrefined oil Refined oil
Soxhlet extraction using hexane Freeze dried seeds 6.33 ± 1.15h, B n/a n/a n/a Air dried seeds 35.0 ± 0.0g, A 0.00 ± 0.00 0.99 ± 0.00i 0.00 ± 0.00 Screw press expression
85°C 47.7 ± 1.2f, E 0.00 ± 0.00 2.59 ± 0.08h, E 0.00 ± 0.00 90°C 79.7 ± 1.2c, B 0.06 ± 0.06 3.85 ± 0.16g, D 0.00 ± 0.00 90°C at 13% Moisture 75.0 ± 0.0d, C 0.03 ± 0.06 4.98 ± 0.08de, B 0.02 ± 0.04 90°C at 16% Moisture 69.0 ± 0.0e, D 0.00 ± 0.00 4.51 ± 0.00f, C 0.02 ± 0.04 105°C 73.0 ± 0.0d, C 0.03 ± 0.06 4.84 ± 0.08e, B 0.00 ± 0.00 125°C 86.3 ± 1.2b, A 0.06 ± 0.06 7.14 ± 0.16a, A 0.02 ± 0.04
Enzyme-assisted aqueous extraction
Enzyme Cocktail 86.3 ± 1.2b,B 0.00 ± 0.00 5.12 ± 0.08d, C 0.02 ± 0.04 Cellulase 81.7 ± 1.2c, C 0.00 ± 0.00 5.12 ± 0.08d, C 0.00 ± 0.00
Hemicellulase 85.0 ± 0.0b, B 0.00 ± 0.00 5.59 ± 0.08c, B 0.07 ± 0.05 Pectinase 81.0 ± 0.0c, C 0.00 ± 0.00 4.09 ± 0.00g, D 0.00 ± 0.00 Protease 89.0 ± 0.0a, A 0.00 ± 0.00 6.30 ± 0.08b, A 0.00 ± 0.00
All data represent means ± standard deviation (n=3). Initial moisture content of dried Carlos seeds was 10.3 ± 1.2%, respectively. Different lower-case superscripts denote difference across extraction types. Different upper-case superscripts denote difference within the same extraction type at p ≤ 0.05 using Tukey's test. n/a is not applicable.
42
Table 2-4. Fatty acid composition of Noble seed oil using different extraction methods. Oil extraction method Palmitic Acid Stearic Acid Oleic Acid Linoleic acid
Soxhlet extraction
Hexane 7.13 ± 1.92 3.25 ± 0.68 16.3 ± 5.7 72.9 ± 16.2 Screw expression 85°C 7.09 ± 2.31 3.01 ± 1.19 16.4 ± 5.6 73.1 ± 16.1
90°C 7.11 ± 2.39 2.85 ± 0.52 16.5 ± 6.3 73.1 ± 17.4 90°C at 13% moisture 7.11 ± 2.37 3.10 ± 0.83 16.5 ± 5.8 73.0 ± 14.1 90°C at 16% moisture 7.06 ± 1.64 3.05 ± 0.40 16.6 ± 4.1 72.9 ± 8.8 105°C 6.80 ± 1.41 2.55 ± 0.74 16.3 ± 3.5 74.0 ± 12.8 125°C 6.88 ± 0.34 3.07 ± 0.72 16.0 ± 1.5 73.7 ± 16.5 Enzyme-assisted aqueous extraction Enzyme Cocktail 6.98 ± 1.22 3.75 ± 0.57 15.4 ± 1.6 73.5 ± 4.9 Cellulase 6.90 ± 0.96 3.08 ± 0.85 15.9 ± 3.0 73.7 ± 19.7 Hemicellulase 6.90 ± 0.72 3.46 ± 0.70 15.7 ± 2.2 73.5 ± 11.4 Pectinase 6.79 ± 2.87 3.25 ± 1.45 16.3 ± 7.6 73.2 ± 24.1 Protease 7.10 ± 1.59 3.70 ± 1.46 15.6 ± 3.2 73.2 ± 12.1
All data represent means ± standard deviation (n=6) expressed as % of individual fatty acid to total fatty acids. Different superscripts denote significant differences in each extraction method at p ≤ 0.05 using Tukey's test.
43
Table 2-5. Fatty acid composition of Carlos seed oil using different extraction methods Oil extraction method Palmitic Acid Stearic Acid Oleic Acid Linoleic acid
Soxhlet extraction Hexane 7.50 ± 1.88 4.9 ± 1.31 15.1 ± 4.3 77.1 ± 15.8
Screw expression
85°C 6.94 ± 1.08 4.56 ± 1.00 14.5 ± 2.7 73.7 ± 16.7
90°C 7.05 ± 1.22 4.28 ± 0.37 14.4 ± 2.4 73.9 ± 3.9 90°C at 13% moisture 7.10 ± 1.03 4.56 ± 0.35 14.1 ± 1.0 73.9 ± 11.2 90°C at 16% moisture 7.07 ± 0.84 4.30 ± 0.40 14.8 ± 1.2 73.5 ± 7.7 105°C 7.00 ± 1.22 4.23 ± 0.61 14.5 ± 1.6 74.0 ± 13.4 125°C 7.69 ± 2.42 4.62 ± 1.06 15.7 ± 4.2 79.3 ± 20.0
Enzyme-assisted aqueous extraction Enzyme Cocktail 7.02 ± 2.02 4.34 ± 1.02 14.4 ± 3.3 73.9 ± 15.9
Cellulase 7.14 ± 3.33 4.20 ± 1.61 14.4 ± 5.9 74.0 ± 27.0 Hemicellulase 7.11 ± 1.54 4.34 ± 0.51 14.7 ± 3.0 73.5 ± 5.7 Pectinase 6.94 ± 1.12 4.00 ± 1.89 15.1 ± 1.9 73.6 ± 7.0 Protease 7.07 ± 2.46 4.18 ± 1.15 15.1 ± 4.9 73.3 ± 15.1
All data represent means ± standard deviation (n=6) expressed as % of total fatty acids. Different superscripts denote significant differences in each extraction method at p ≤ 0.05 using Tukey's test.
44
Table 2-6. Impact of different extraction methods on the vitamin E concentration (mg/100 g) of crude Noble seed oil
All data represent means ± standard deviation (n=6). Different lower-case superscripts denote difference across extraction types. Different upper-case superscripts denote difference within the same extraction type at p ≤ 0.05 using Tukey's test. n.d. is not detected.
Oil extraction methods α-Tocopherol α-Tocotrienol γ-Tocopherol γ-Tocotrienol δ-Tocotrienol
Soxhlet
Hexane 10.8 ± 2.4abc 21.3 ± 0.4 39.8 ± 1.8ab 15.7 ±0.6abcd 2.95 ± 0.33ab
Screw expression
85°C 7.14 ± 1.03bc 21.3 ± 4.0 24.9 ± 2.1cd, B 14.1 ± 1.4d 2.55 ± 0.36b
90°C 7.57 ± 1.14abc 25.2 ± 2.8 23.6 ± 1.3d, B 15.8 ± 0.7abcd 2.73 ± 0.18ab
90°C at 13% moisture 6.48 ± 0.71c 25.8 ± 3.4 23.0 ± 1.2d, B 15.9 ± 1.4abcd 2.56 ± 0.36b
90°C at 16% moisture 8.74 ± 2.47abc 21.9 ± 3.3 32.1 ±4.4abcd, A 15.0 ± 1.1cd 2.93 ± 0.27ab
105°C 6.60 ±1.17c 23.5 ± 0.8 23.5 ±3.0d, B 15.5 ± 0.4bc 2.63 ± 0.38ab
125°C 6.84 ± 1.05bc 22.8 ± 1.8 23.2 ±2.8d, B 15.4 0.8c 2.94 ± 0.15ab
Enzyme-assisted aqueous extraction
Enzyme cocktail 9.18 ± 3.56abc 20.5 ± 4.3 30.4 ± 10.2bcd 17.5 ± 1.1a, A 2.92 ± 0.15ab
Cellulase 11.6 ± 1.1a 22.0 ± 1.3 42.2 ± 4.9a 15.4 ± 0.7c, B 2.92 ± 0.15ab
Hemicellulase 11.1 ± 3.5ab 22.4 ± 3.7 38.0 ± 6.9ab 16.7 ± 1.1abc, AB 3.23 ± 0.58a
Pectinase 9.16 ± 0.77abc 23.2 ± 2.1 34.3 ± 1.0abc 15.1 ± 0.5cd, B 2.95 ± 0.48ab Protease 10.1 ± 4.2abc 21.6 ±4.2 34.6 ± 10.3abc 17.2 ± 1.2ab, A 3.24 ± 0.25a
45
Table 2-7. Impact of different extraction methods on the vitamin E concentration (mg/100 g) of refined Noble seed oil.
All data represent means ± standard deviation (n=6). Different lower-case superscripts denote difference across extraction types. Different upper-case superscripts denote difference within the same extraction type at p ≤ 0.05 using Tukey's test.
Oil extraction methods α-Tocopherol α-Tocotrienol γ-Tocopherol γ-Tocotrienol δ-Tocotrienol
Soxhlet Hexane 6.89 ± 0.98a 9.80 ± 1.32a 18.2 ± 2.4a 6.67 ± 0.88ab n.d.
Screw expression
85°C 0.716 ± 0.361cd 2.73 ± 0.86cd 4.72 ± 2.58de, B 3.73 ± 2.05c, B n.d. 90°C 0.800 ± 0.030c 3.07 ± 0.03c 6.21 ± 1.10cd, AB 4.82 ± 1.48bc n.d. 90°C at 13% moisture 0.910 ± 0.100c 3.76 ± 0.54 8.03 ± 1.13bc, AB 6.46 ± 1.06ab, AB n.d. 90°C at 16% moisture 0.880 ± 0.190c 3.32 ± 1.29c 6.67 ± 3.23bcd, AB 5.11 ± 3.15bc, AB 0.163 ± 0.401 105°C 1.66 ± 0.35b 7.68 ± 1.78b 9.76 ± 1.78b, A 8.10 ± 1.44a, A 0.293 ± 0.454 125°C 0.530 ± 0.430cde 2.25 ± 0.65cde 7.29 ± 0.65bcd, AB 5.04 ± 1.34bc, AB 0.276 ± 0.428
Enzyme-assisted aqueous extraction
Enzyme cocktail 0.430 ± 0.030cde 1.11 ± 0.07de 1.81 ± 0.21ef, A 0.11 ± 0.28d n.d. Cellulase n.d. 1.10 ± 0.13de n.d. n.d. n.d. Hemicellulase n.d. 0.98 ± 0.21e 0.37 ± 0.41f, C n.d. n.d. Pectinase 0.709 ± 0.104cd 1.34 ± 0.22de 2.02 ± 0.25ef, A n.d. n.d. Protease 0.0565 ± 0.138de 1.03 ± 0.08e 1.18 ± 0.10f, B n.d. n.d.
46
Table 2-8. Impact of extraction methods on vitamin E concentration (mg/100 g) of crude Carlos seed oil. Oil extraction methods α-Tocopherol α-Tocotrienol γ-Tocopherol γ-Tocotrienol δ-Tocotrienol
Soxhlet
Hexane 2.94 ± 0.39 c 9.35 ± 1.23c 14.6 ± 1.4bc 15.8 ± 1.3 1.72 ± 0.16ab
Screw expression
85°C 3.12 ± 0.17 abc 12.5 ± 5.0abc 15.1 ± 4.0bc 18.0 ± 4.0 1.89 ± 0.30ab
90°C 2.39 ± 0.48 abc 12.0 ± 4.5abc 9.62 ± 0.50c 18.3 ± 3.6 1.73 ± 0.08ab
90°C at 13% moisture 4.35 ± 3.39 abc 13.5 ± 6.4abc 17.1 ± 1.0abc 16.6 ± 0.9 1.60 ± 0.16b
90°C at 16% moisture 2.77 ± 0.59bc 11.4 ± 4.9bc 12.6 ± 0.7c 17.4 ± 4.1 1.66 ± 0.05ab
105°C 2.71 ± 0.35abc 14.2 ± 3.6abc 9.60 ± 0.20c 19.1 ± 2.4 1.74 ± 0.12ab
125°C 2.53 ± 0.20abc 13.0 ± 2.7abc 9.25 ± 0.22c 18.8 ± 2.0 1.75 ± 0.17ab
Enzyme-assisted aqueous extraction
Enzyme cocktail 4.10 ± 0.41abc, B 15.1 ± 0.9abc, BC 14.7 ± 1.0bc, B 19.7 ± 0.7 1.76 ± 0.07ab, AB
Cellulase 3.84 ± 0.23 abc, B 14.0 ± 1.8abc, C 14.2 ± 1.8bc, B 18.6 ± 1.5 1.75 ± 0.15ab, AB
Hemicellulase 6.02 ± 2.25ab, AB 16.6 ± 3.4ab, ABC 16.9 ± 2.0abc, AB 19.3 ± 2.3 1.83 ± 0.17ab, AB
Pectinase 6.84 ± 1.53ab, A 18.2 ± 1.3ab, AB 23.2 ± 6.3ab, AB 17.9 ± 4.4 1.69 ± 0.06ab,
Protease 6.52 ± 1.28a, A 18.9 ± 1.0a, A 25.4 ± 10.4a, A 19.3 ± 4.4 1.92 ± 0.12a, AB
All data represent means ± standard deviation (n=6). Different lower-case superscripts denote difference across extraction types. Different upper-case superscripts denote difference within the same extraction type at p ≤ 0.05 using Tukey's test. n.d. is not detected.
47
Table 2-9. Impact of extraction methods on vitamin E concentration (mg/100g) of refined Carlos seed oil Oil extraction methods α-Tocopherol α-Tocotrienol γ-Tocopherol γ-Tocotrienol δ-Tocotrienol
Soxhlet Hexane 1.63 ± 0.20a 7.42 ± 0.64a 8.04 ± 0.68a 13.8 ± 1.3a 1.22 ± 0.01a Screw expression 85°C 0.269 ± 0.416b 1.71 ± 0.23c 0.566 ± 0.647b 1.52 ± 0.79cd 0.412 ± 0.217b 90°C n.d. 1.31 ± 0.19c 0.765 ± 0.660b 1.65 ± 1.15cd n.d. 90°C at 13% moisture n.d. 1.48 ± 0.15c 1.34 ± 0.46b 2.75 ± 1.23cd n.d. 90°C at 16% moisture n.d. 1.20 ± 0.23c n.d. 0.824 ± 0.061cd n.d. 105°C 0.573 ± 0.887b 3.56 ± 3.64bc 3.12 ± 4.58b 5.86 ± 7.01bc 0.391 ± 0.217b 125°C n.d. 1.33 ± 0.14c n.d. 1.05 ± 0.07cd n.d.
Enzyme-assisted aqueous extraction
Enzyme cocktail 1.91 ± 0.45a, A 5.63 ± 1.37ab, A 8.03 ± 1.89b, A 9.36 ± 2.24ab, A n.d. Cellulase n.d. 1.02 ± 0.11c, B n.d. 0.243 ± 0.376d, B n.d. Hemicellulase 0.432 ±0.67b, B 2.74 ± 2.42c, B 2.27 ± 3.52b, B 3.73 ± 5.78cd, B 0.407 ± 0.630b Protease 0.179 ± 0.430b, B 1.23 ± 0.06c, B n.d. n.d. n.d. Pectinase n.d. 1.03 ± 0.28c, B 0.805 ± 0.150b, B n.d. n.d.
All data represent means ± standard deviation (n=6). Different lower-case superscripts denote difference across extraction types. Different upper-case superscripts denote difference within the same extraction type at p ≤ 0.05 using Tukey's test. n.d. is not detected. n.d. is not detected
48
Table 2-10. Refining yield (%, w/w) of seed oil from Noble and Carlos muscadine seeds at different steps of refining.
Oil extraction method % Yield (w/w)
Noble Carlos
Degumming Neutralizing Bleaching Degumming Neutralizing Bleaching Soxhlet Hexane 64.8 ± 2.9b 47.4 ± 1.0c 41.1 ± 1.6b 84.7 ± 0.5c 64.7 ± 0.8 59.7 ± 1.0b Screw Expression 85°C 59.5 ± 1.5b 45.6 ± 2.1c 40.6 ± 0.1b 78.5 ± 0.9d 63.9 ± 2.6b 59.3 ± 1.9b 90°C 64.1 ± 1.2b 46.1 ± 1.3c 40.7 ± 0.7b 80.6 ± 0.4d 64.7 ± 0.7b 60.0 ± 0.7b 90°C at 13% moisture 59.8 ± 1.0b 46.2 ± 1.1c 39.1 ± 2.3b 78.5 ± 0.3d 64.4 ± 0.4b 59.1 ± 1.4b 90°C at 16% moisture 60.4 ± 1.0b 45.3 ± 1.7c 41.0 ± 1.0b 79.6 ± 0.8d 64.3 ± 1.1b 57.7 ± 0.7b 105°C 61.6 ± 2.1b 44.4 ± 2.2c 41.9 ± 1.0b 79.0 ± 1.0d 63.2 ± 1.2b 60.5 ± 0.6b 125°C 62.5 ± 0.6b 45.6 ± 0.4c 41.0 ±1.1b 75.9 ± 0.3e 62.9 ± 0.5b 59.7 ± 1.8b Enzyme-assisted aqueous extraction Cocktail 93.6 ± 3.7a 80.7 ± 1.6ab 72.7 ± 0.7b 99.2 ± 0.3a 81.2 ± 1.8a 72.5 ± 2.1a Cellulase 95.0 ± 1.6a 79.5 ± 1.0ab 71.6 ± 2.7b 97.4 ± 0.4a 80.0 ± 2.1a 72.9 ± 2.2a Hemicellulase 95.1 ± 1.6a 80.9 ± 2.9ab 72.4 ± 3.4b 97.4 ± 0.4a 81.6 ± 1.9a 70.4 ± 2.7a Pectinase 94.8 ± 0.6a 81.6 ± 2.0a 68.5 ± 2.9b 94.4 ± 1.7b 76.9 ± 3.1a 72.8 ± 2.5a Protease 94.8 ± 1.2a 76.2 ± 1.5b 72.2 ± 0.2b 94.8 ± 0.4b 80.2 ± 2.1a 69.5 ± 2.6a
All data represents means ± standard deviation (n=3). Oil yield was expressed as percentage of mass of oil remaining after refining step compared to initial mass. Different superscripts denote significant differences in each extraction method at p ≤ 0.05 using Tukey's test.
49
Figure 2-1. Concentrations of tocopherol and tocotrienol in Noble seed oil after the refining process. Results are mean
with error bars denoting standard deviation. Different lower-case superscripts denote difference across extraction types. Different upper-case superscripts denote difference within the same extraction type at p ≤ 0.05 using Tukey's test.
a
b b
bb
a
b
c, A
c, C c, BC c, Bc, A
0%
10%
20%
30%
40%
50%
60%
Hex
ane
85°C
90°C
90°C
at
13
% m
ois
ture
90°C
at
16
% m
ois
ture
105
°C
125
°C
Enzy
me
co
ckta
il
Cel
lula
se
Hem
ice
llula
se
Pe
ctin
ase
Pro
teas
e
Soxhlet Screw expression Enzyme-assisted aqueous
Re
ten
tio
n⍺-Tocopherol 𝞬-Tocopherol ⍺-Tocotrienol 𝞬-Tocotrienol δ-Tocotrienol
50
Figure 2-2. Concentrations of tocopherol and tocotrienol in Carlos seed oil after the refining process. Results are mean
with error bars denoting standard deviation. Different lower-case superscripts denote difference across extraction types. Different upper-case superscripts denote difference within the same extraction type at p ≤ 0.05 using Tukey's test.
a
cd cdcd
cd
bc
cd
b, A
d, B
cd, B
d, B d, B
0%
10%
20%
30%
40%
50%
60%
70%
80%
Hex
ane
85°C
90°C
90°C
at
13
% m
ois
ture
90°C
at
16
% m
ois
ture
10
5°C
12
5°C
Enzy
me
co
ckta
il
Cel
lula
se
Hem
ice
llula
se
Pe
ctin
ase
Pro
teas
e
Soxhlet Screw expression Enzyme-assisted aqueous
Re
ten
tio
n⍺-Tocopherol 𝞬-Tocopherol ⍺-Tocotrienol 𝞬-Tocotrienol δ-Tocotrienol
51
Figure 2-3. Peroxide value in Carlos seed oil extracted using enzyme-assisted aqueous extraction with protease after
treatment with bleaching earth clay of different concentrations. Results are mean with error bars denoting standard deviation. Carlos seed oil extracted with assistance of protease had an initial peroxide value of 89.0 mEq/kg oil.
y = 3776.6x2 - 1347x + 94.752R² = 0.9874
0
10
20
30
40
50
60
70
80
90
0.0% 2.0% 4.0% 6.0% 8.0% 10.0% 12.0%
Pero
xid
e v
laue (
mE
q/k
g o
il)
Bleaching earth clay oncentration (%, w/w)
52
CHAPTER 3 MUSCADINE GRAPE SEED FLOUR
Background
Muscadine seeds are a byproduct of juice pressing and wine making. Of the 300
tons of seeds that are disposed of or used as cattle feed, 250 tons could potentially be
utilized as muscadine grape seed flour (Husmann & Dearing, 1916). The muscadine
grape seeds possess unique phytochemicals including hydrolyzable tannins, flavon-3-
ols, condensed tannins, ellagic acid derivatives, and quercetin rhamnoside (Sandhu &
Gu, 2010). Extracts of muscadine seeds showed antioxidant function as well as
antimicrobial activity against E. coli O-157:H7 and E.Sakazakii (Kim et al., 2009; Kim et
al., 2008; Sandhu & Gu, 2010). Additionally, phytochemical extracts of the cold pressed
muscadine seed flour reduced the proliferation of human colon cancer cells (Lutterodt et
al., 2011). Muscadine seed flour was added in baked products to enhance antioxidant
capacity (Hoye Jr & Ross, 2011; Ross, Hoye Jr, & Fernandez‐Plotka, 2011), suggesting
it could be used as a potential replacement for other flours. The aim of this study was to
observe the effects of different oil extraction methods on the proximate composition,
phenolic content, antioxidant capacity, and phytochemical profile of defatted muscadine
seed flour.
Materials and Methods
Chemicals
Methanol (HPLC grade), n-Hexane, 2,2,-Diphenyl-1-picryhydryazyl (DPPH), 6-
Hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid (trolox), potassium sulfate,
Kjeltabs, Kjelsorb, sulfuric acid, sodium hydroxide, formic acid (HPLC grade), and gallic
acid were purchased, fiber glass thimbles from Fisher Scientific Co. Pittsburgh, PA,
53
USA) Quecetin, kaempferol, and myricetin were purchased from Sigma Aldrich (St.
Louis, MO, USA). Anthocyanin standards: delphinidin 3,5-diglucoside, malvidin 3-
5,diglucoside, cyanidin 3,5 diglucoside, petunidin 3,5-diglucoside, pelargonidin 3,5-
diglucoside, and peonidin 3,5-diglucoside were purchased from Phytolab
(Vestenbergreuth,Germany). Filter bags, heat sealer, digestion flasks, and a dessicant
were purchased from Ankom Technology (Macedon, NY, USA)
Preparation of Flour
Defatted seeds were obtained for Soxhlet extraction using hexane and
pressed cake was obtained from expression using a continuous screw press. Pressed
cake contains residual oil, so it was placed in a RRH-A1000 high speed multi-function
grinder and grinded to a fine power. Pressed cake powder was placed in fiber glass
thimbles and into a Soxhlet apparatus. Pressed cake powder was washed with n-
hexane in the Soxhlet apparatus for 8 hours to obtain defatted press cake. Defatted
press cake and defatted seeds for Soxhlet extraction were placed in the RRH-A100 high
speed multi-function grinder to be ground. Once ground defatted seeds from Soxhlet
extraction and ground defatted press cake were run through a No.60 sieve (250 m).
Resulting powder was collected as muscadine flour.
Proximate Analysis of Flour
Ash in flour was determined by a previously described by AOAC official method
923.03 (International, 1995). In summary, 3-5 grams of muscadine seed flour were
placed into an ashing dish that had been ignited, cooled in a desiccator, and weighed
after reaching room temperature. Samples were placed in a furnace at 550°C until it
was a light gray ash. Samples and dishes were placed in a desiccator and weighed
54
after reaching room temperature. Finals weights were compared to initial weights of
sample to receive ash content.
Protein in flour was determined using the Kjeldahl method with modifications to
the one described by AOAC official method 920.87 (International, 1995). One gram of
muscadine seed flour was placed in a digestion flask with one Kjeltab and 10 mL of
sulfuric acid. Flasks were placed in an inclined position and heated gently. Flasks were
allowed to digest for 30 minutes after the solution became clear. Clear contents were
poured into the Labconco Rapidstill I (Labconco Corp, Kansas City, MO, USA) micro-
Kjeldahl distillation unit. Distillation flasks were washed with distilled water and also
poured into the distillation unit.
During the digestion, the micro-Kjeldahl distillation unit was preheated. A cup
containing 30 mL of Kjelsorb was placed near the distillation unit. After digested
samples were placed into the distillation unit, concentrated sodium hydroxide (50%) was
slowly added. Kjelsorb was placed at the end of the distillation unit with swirling to
prevent the initial backflow. Distillation was allowed to run for approximately 10 minutes
or until the final volume was around 70-80 mL.
The Kjelsorb solution was then titrated using 0.05 M hydrochloric acid. Volume of
hydrochloric acid was used to determine nitrogen content. Protein was calculated by
using a conversion factor of 5.3 as described in previously published work (Kamel,
Dawson, & Kakuda, 1985).
Neutral detergent fiber content was analyzed by an external laboratory (Central
Analytical Laboratory, Fayetteville, AR, USA). Neutral detergent fiber was measured
using a filter bag technique (Ankon, 2011).The mass of each filter bag is recorded and
55
0.45 – 0.50 g of prepared flour were placed into each bag. Each bag was sealed closed
and placed into an acetone bath with 20 g of sodium sulfite. Bags were heated in the
solution for 75 minutes. After the bags were rinsed in hot water for five minutes and
placed into a room temperature acetone bath. After, bags were removed, air-dried, and
then dried in an oven at 102°C. After being completely dried, each bag was placed in a
desiccant pouch and cooled to room temperature before being weighed. Weight of the
sample before and after treatment were used to calculate percent neutral detergent
fiber.
Phytochemical Extraction
Phytochemicals in muscadine seed flour were extracted using a previously
described method with modification (Sandhu, Gray, Lu, & Gu, 2011). Briefly, one gram
of seed flour and 10 mL of methanol/water/acetic acid (85:15:0.5; v/v/v) were placed in
a 50 mL conical centrifuge tube. The mixture was vortexed for 30 seconds then
sonicated for five minutes and left in the sonicator to rest for 20 minutes. After the
mixture was vortexed for 30 seconds and centrifuged at 1450 g for eight minutes. The
supernatant was stored at -20°C until used.
Total Phenolic Content
Folin-Ciocalteu Reagent purchased from Fisher Scientific (Pittsburg, PA, USA)
was diluted with deionized water 1:9 ratio (v/v) to create a working solution. In a test
tube one mL of Folin-Ciocalteu working solution and 100 mL of deionized water as a
blank. A standard was prepared using seven test tubes with 100 L of gallic acid
solution with concentrations of 0, 100, 200, 300, 400, 500, and 600 mg/mL. A final test
tube contains 100 L of the phytochemical extraction. One mL of was added to each
56
tube before a solution of 15% sodium carbonate was added and vortexed. The mixture
was incubated for 30 minutes before absorbance was read at 765 nm.
DPPH Assay
The DPPH scavenging activity of muscadine seed flour was determined using a
previously published method (Brand-Williams, Cuvelier, & Berset, 1995). A DPPH stock
solution was made by dissolving 20 mg of DPPH into 100 mL of methanol and stored at
-20°C. A DPPH working solution was made by mixing 2.8 mL of DPPH stock solution
and 7.2 mL of methanol. 50 L of methanol was placed in the 96-well plate as a blank,
along with the extract from the muscadine seed flour, and trolox standards with
concentrations of 50,100, 200, 300, 400, and 500 mol/mL. 200 L of DPPH working
solution were put into each well and incubated in the dark at room temperature for 30
minutes. Absorbance was measured at 515 nm on a microplate reader (SPECTRAMax
190, Molecular Devices, Sunnyvale, CA). Results of the DPPH assay were expressed
as micromoles of trolox equivalent (mol trolox/g of flour)
HPLC Analysis of Muscadine Flour Phytochemicals
High-performance liquid chromatography (HPLC) analyses of muscadine seed
flour extract was performed on 1200 system equipped with a binary pump, an
autosampler/injector, and a diode array detector (Agilent Technologies, Palo Alto, CA,
USA). Separation was conducted using a Zorbax-SB C18 column (4.6 mm X 250 mm,
5m, Agilent Technologies). UV vis spectra were scanned from 220 to 600 nm on a
diode array detector with detection wavelengths of 280, 360, and 520 nm. Anthocyanin
analysis quantification was determined using a previously published method (Li et al.,
2017). Muscadine flour extracts were filtered before injection. The mobile phases
57
consisted of methanol (phase A) and 5% formic acid in water (phase B). The linear
gradient was as follows: 0-10 min, 95-85% B; 10-30 min, 85-70% B; 30-45 min, 70% B;
47 min, 30% B; with a flow rate of 0.8 mL/min.
To quantify other phytochemicals including kaempferol and myricetin a previously
published method was used (Sandhu & Gu, 2010). Acid hydrolysis of samples was
done before HPLC analysis. 1.2 M hydrochloric acid was added to muscadine seed
flour methanol extract to create a 50% solution and sonicated for five minutes.
Hydrolysis was conducted in a precision water bath (Thermo Fisher scientific, Waltham,
MA) for 80 minutes at 90°C. The mobile phases consisted of 0.5% aqueous formic acid
solution (phase A) and methanol (phase B). The linear gradient was as follows: 0-2 min,
5% B; 2-10 min, 5-20% B; 10-15 min, 30-35% B; 60-65 min, 80-85% B; 65-70 min, 85-
5% B; with a flow rate of 1 mL/min.
Results and Discussions
Proximate Composition of Flour
Ash content of Noble seed flour and Carlos seed flour are shown in Table 3-1.
The ash content of Noble seed flour ranged from 6.11 to 13.4 g/100 g. Different
methods of extraction, as well as different temperatures of screw press expression, did
not show significant effects on the ash content of Noble seed flour. However, there were
significant differences in the ash content of Carlos seed flour. Flour obtained from
expression at 90 °C with a Carlos seed moisture content of 16% (w/w) had significantly
higher ash content than all other flours (17.2 g/100 g). Muscadine grape seed flour
possessed more ash content than previously reported grape seed flour (Özvural &
Vural, 2011). This data suggests that muscadine seed flour is a greater source of
minerals than grape seed flour than other grapes of the Vitis genus.
58
Table 3-1 displays the protein content of the flours obtained from seven different
extraction methods. Noble seed flour protein content was the highest in Soxhlet defatted
Noble seed flour and expression defatting at 90°C, 105°C, and 125°C Noble seed flour.
Carlos seed flour contained the highest protein content after being expressed at 125°C.
Protein content of both cultivars ranged from 14.3 to 17.8 %. Muscadine seed flour
contained higher levels of protein than previously reported data on Vitis Vinifera grape
seed flour (Kamel et al., 1985). However similar values have been reported in whole
wheat flour (Davis, Cain, Peters, Le Tourneau, & McGinnis, 1981). Differences in
protein content among flours are likely due to thermal treatment differences in each oil
extraction method. This data suggests that muscadine seed flour could provide as much
protein as whole wheat flour, but unlike whole wheat flour, muscadine seed flour does
not contain gluten. Muscadine seed flour has the potential to be a gluten free substitute
for wheat flour.
Noble seed flour had a carbohydrate range from 60.3 to 72.6% and 55.0 to
70.1% for Noble and Carlos, respectively. Among the Noble seed flours, there was
significant difference among the carbohydrate content, with hexane defatted seed flour
possessing the highest carbohydrate content. Among the Carlos seed flours, flour that
underwent expression at 90°C had the highest carbohydrate content. Muscadine seed
flour fiber content ranged from 42.0 to 49.5 and 46.3 to 51.7% for Noble and Carlos,
respectively. Both Noble and Carlos seed flour displayed no significant difference in
fiber content among different defatting conditions to obtain the flour. Muscadine seed
flour possessed similar carbohydrate content to those found in wheat in previous
literature, and more than flour from various Vitis vinifera seeds (Davis et al., 1981;
59
Kamel et al., 1985). Fiber found in Noble and Carlos seed flour is neutral detergent
fiber, which consists of lignin, hemicellulose, and cellulose, components of insoluble
fiber. These results demonstrate that Noble and Carlos seed flours are comparable
sources of carbohydrates and insoluble fibers to that found in wheat flours and are a
greater source than that found in grape seed flour from Vitis vinifera grape seeds.
Lipid content in flour largely depended on the efficiency of oil extraction. Soxhlet
defatted flour of the Noble and Carlos seed flour possessed the least amount of lipids
because they were removed by the hexane. The least efficient oil extraction method for
noble seeds, with pressing conditions of 90°C at 16% moisture, had the Noble seed
flour with the highest lipid content. High moisture resulted in oil expression being less
effective resulting in a higher lipid content flour. Expression of Carlos seed oil was also
less effective than Soxhlet extraction using hexane. As a result, the muscadine seed
flours that underwent expression possessed significantly higher lipid content in flour
than flour exposed to Soxhlet extraction using hexane. This data suggests that,
extraction method plays a significant role in lipid content in flour. Higher lipid
concentrations in flour can result in greater risk of oxidation and rancidity (Galliard,
1986).
Total Phenolic Content and Antioxidant Capacity
Table 3-2 shows the total phenolic content and antioxidant capacity of the
muscadine seed flours defatted by different extraction methods and conditions. Based
on defatting method, Soxhlet extracted Muscadine grape seed flour possessed the
highest phenols expressed in gallic acid equivalence (32.8 mg Gallic acid/mL). Similarly,
Carlos seed flour obtained after a Soxhlet and hexane treatment possessed the most
total phenols (22.4 mg gallic acid/mL). The antioxidant capacity of Noble seed flour was
60
found to be the highest in the flour that underwent oil extraction using expression at
90°C; however, there was no significant difference among the antioxidant capacity of
Noble seed flour. Carlos seed flour displayed significantly higher antioxidant capacity in
seed flour defatted with Soxhlet extraction (151 mol Trolox/100g), and expression at
85°C (184 mol Trolox/100g), 105°C (183 mol Trolox/100g), and 125°C (129 mol
Trolox/100g). Carlos seed flours with the oil extracted using the Soxhlet extraction and
expression at 85°C , 105°C, and 125°C were significantly more effective in neutralizing
DPPH free radicals. Total phenolic content and antioxidant capacity of Noble and Carlos
flour were less than previously reported data (Sandhu & Gu, 2010). The data
demonstrates that Noble and Carlos seed flour experienced losses of total phenolic
content and antioxidant capacity that could likely be attributed to oxidation and thermal
degradation during the oil extraction process. Findings support Soxhlet extraction using
hexane more efficient at preserving phenolic compounds in Noble and Carlos seed flour
than screw expression.
Characterization of Muscadine Flour Phytochemicals
Phytochemical composition of Noble and Carlos seed flour are shown in Tables
3-3 and 3-4, respectively. Phytochemical profiles show similarity to identified
compounds in previous literature (Li et al., 2017). HPLC chromatograms of Noble seed
flour and Carlos seed flour were recorded at 360 and 520 nm (Figures 3-1 and 3-2).
Flavonals had a maximum absorption at 360 nm and anthocyanins at 520 nm. Of the
two flours, only Noble seed flour was shown to possess any anthocyanins. This could
be explained by the wine-making process, in which red Noble grapes are crushed and
seeds and skins are fermented together with juices (Talcott & Lee, 2002). Wine
61
fermentation may also be responsible for concentrating other flavonoids in the seeds, as
Noble seed flour possessed myricetin and kaempferol and Carlos seed flour was only
possessed myricetin. The predominant anthocyanin in the Noble seed flour was
malvidin 3,5-diglucoside. Among fat extraction methods, Noble seed flour that had
undergone only Soxhlet extraction using hexane for defatting contained the highest
malvidin 3,5-diglucoside content (167 mg/100g). Noble seed flour that was defatted
using a Soxhlet extraction also had significantly higher concentrations of delphinidin 3,5-
diglucoside (31.0 mg/100g), cyaniding 3,5-diglucoside (76.9 mg/100g), petunidin 3,5-
diglucoside (36.0 mg/100g), and peonidin 3,5-diglucoside (26.8 mg/100g). Soxhlet
defatted Noble seed flour likely has higher anthocyanin content as it only has to be
defatted once, while pressed flour experiences the pressing temperatures as well as
Soxhlet extraction to remove as much oil from the seeds as possible before the flour
process. High temperature pressings and heated solvent extraction likely diminish the
anthocyanin content of the Noble seed flour. The predominant flavonoid in Noble seed
flour was myricetin, ranging from 211 to 235 mg/100g, followed by kaempferol ranging
from 39.7 to 44.7 mg/100g, with no detection of quercetin. There was no significant
difference in concentration of myricetin among Noble seed flour from different oil
extraction methods. Kaempferol concentrations were highest in Noble seed flour that
underwent expression at 125°C but only significantly higher than Noble seed flour that
underwent expression at 85°C. Similar phytochemical compositions were reported in
previous work (Li et al., 2017). Phytochemical concentrations were higher in Noble seed
flour than Carlos seed flour. This data suggests that the fermentation process, where
seeds and juice are fermented together, concentrates anthocyanins and flavonoids in
62
the Noble seeds. Additionally, the data suggests that Soxhlet extraction using hexane is
the best method for preserving phytochemicals within Noble seed flour. Anthocyanin
and flavonoid concentrations were lower than previously reported values for muscadine
seeds, possibly from losses experienced throughout the oil extraction process.
Carlos seed flour obtained from all oil extraction methods had no detectable
anthocyanins that were found in Noble seed flour. Additionally, Carlos seed flour did not
show any kaempferol, a flavonoid that was found in Noble seed flour. Carlos seed flour
did, however, show similar levels of myricetin, the predominant flavonoid in the Noble
seed flour. Myricetin concentrations in Carlos seed flour ranged from 165 to 234 mg/100
g. Myricetin concentrations in Carlos seed flour showed no difference among seed flour
that underwent different defatting conditions. Carlos seed flour had lower reported
myricetin levels than previous work (Pastrana-Bonilla, Akoh, Sellappan, & Krewer,
2003). Differences in Carlos seed flour myricetin levels could likely be attributed to
oxidation and thermal degradation throughout the oil extraction process that effected all
Carlos seed flours.
Summary
Our results indicate that muscadine seed flour from Noble and Carlos seeds
contain a proximate composition similar to whole-wheat flour but without gluten proteins.
In Carlos seed flour, expression of the seed at 125°C resulted in flour with the highest
amount of protein. Carlos seed flour with lower temperature expressions (85°C, 90°C,
90°C at 13% moisture, and 90°C at 16% moisture) possessed higher amounts of
carbohydrates. Fiber content showed no significant difference among flour treated with
different oil extraction treatments. However, Carlos seed flour did on average possess
more fiber than Noble seed flour. Similarly, ash content was not significantly different
63
among the various flours. Both Noble and Carlos seed flour defatted by a Soxhlet
apparatus and hexane possessed the highest total phenols. Noble seed flour showed
no significant difference in antioxidant capacity despite possessing a difference in
phenolic content. Carlos seed flour possessed significantly different antioxidant
capacities that did not correspond directly with higher phenolic contents in the flour.
Noble seed flour was shown to have a wider variety of phytochemicals possessing
multiple anthocyanins and kaempferol unlike the Carlos seed flour.
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Table 3-1. Impact of extraction method on proximate analysis (%, w/w) of Noble seed flour and Carlos seed flour.
Oil extraction method Moisture Ash Protein Lipids NDF Fiber Total Carbohydrates
Noble seed flour
Soxhlet extraction
Hexane 4.92 ± 0.13abc 6.11 ± 0.84 16.4 ± 0.1ab 0.00 ± 0.90c 44.8 ± 5.3 72.6 ± 2.0a
Screw expression
85°C 4.65 ± 0.40bc 8.09 ± 3.32 16.1 ± 0.2b 3.76 ± 1.85ab 44.8 ± 1.0 67.4 ± 0.9ab
90°C 3.93 ± 0.29bc 12.3 ± 3.5 16.6 ± 0.2a 3.58 ± 0.25b 46.3 ± 1.4 63.5 ± 3.3b
13% at 90°C 5.17 ± 0.87ab 10.2 ± 3.7 16.4 ± 0.3ab 5.51 ± 0.63ab 46.0 ± 0.3 60.3 ± 3.0b
16% at 90°C 6.03 ± 0.27a 13.4 ± 3.6 16.8 ± 0.0ab 6.04 ± 0.39a 42.0 ± 2.6 64.0 ± 3.4b
105°C 3.68 ± 0.54c 12.6 ± 1.7 16.4 ± 0.1a 5.49 ± 0.21ab 49.5 ± 0.3 64.2 ± 3.1b
125°C 3.62 ± 0.44c 9.56 ± 3.20 14.3 ± 0.1c 4.62 ± 0.22ab 48.0 ± 0.3 61.5 ± 3.5b
Carlos seed flour
Soxhlet extraction
Hexane 5.17 ± 0.60 13.8 ± 1.6 16.3 ± 0.1c 0.00 ± 0.57b 46.3 ± 0.8 64.7 ± 1.5ab
Screw expression
85°C 5.07 ± 0.20 9.43 ± 2.60 17.0 ± 0.2b 5.02 ± 0.43a 53.6 ± 1.1 64.7 ± 4.4ab
90°C 5.31 ± 0.72 4.66 ± 1.21 16.3 ± 0.2c 4.17 ± 1.01a 51.2 ± 0.6 70.1 ± 0.7a
13% at 90°C 3.73 ± 0.19 8.11 ± 0.70 17.1 ± 0.3b 3.79 ± 0.68a 51.2 ± 3.9 62.3 ± 2.5bc
16% at 90°C 5.02 ± 0.60 12.9 ± 2.2 17.8 ± 0.0a 5.90 ± 0.48a 51.7 ± 0.0 55.0 ± 3.2c
105°C 4.58 ± 0.72 12.2 ± 2.9 16.3 ± 0.1c 5.27 ± 1.52a 51.7 ± 4.5 64.7 ± 1.5ab
125°C 5.11 ± 1.15 17.22 ± 2.8 16.7 ± 0.1bc 3.70 ± 0.46a 48.6 ± 1.5 64.7 ± 1.9ab
All data represent means ± standard deviation (n=3). Different superscripts denote significant difference in each extraction method at p< 0.05 using Tukey’s test. Total carbohydrates were calculated by difference. NDF stands for neutral detergent fiber (lignin, hemicellulose, cellulose).
65
Table 3-2. Impact of extraction method on total phenols and antioxidant capacity of Noble seed flour and Carlos seed flour.
Oil extraction methods
Noble Carlos
Total phenols (mg
Gallic acid /mL)
Antioxidant capacity (µmol
Trolox/ 100 g)
Total phenols (mg
Gallic acid /mL)
Antioxidant capacity
(µmol Trolox/ 100 g)
Soxhlet extraction
Hexane 32.8 ± 1.3a 162 ± 20 22.4 ± 1.3a 151 ± 5ab
Screw expression
85°C 25.1 ± 1.4bcd 169 ± 23 7.92 ± 0.54e 148 ± 29ab
90°C 22.9 ± 1.3d 171 ± 22 11.4 ± 1.2cd 119 ± 23b
90°C at 13% moisture 23.7 ± 0.5cd 160 ± 33 8.20 ± 1.51c 101 ± 14b
90°C at 16% moisture 23.8 ± 0.3cd 122 ± 10 9.96 ± 0.71b 113 ± 26b
105°C 27.5 ± 0.4b 114 ± 7 13.1 ± 1.6de 183 ± 31a
125°C 25.9 ± 0.1bc 168 ± 42 18.4 ± 0.6cde 129 ± 10ab
All data represent means ± standard deviation (n=3). Different superscripts denote significant difference in each extraction method at p< 0.05 using Tukey’s test.
66
Table 3-3. Impact of extraction method on phytochemical content (mg/100g) of Noble seed flour
Phytochemicals
Soxhlet Screw expression
Hexane 85°C 90°C 90°C at 13%
moisture
90°C at 16%
moisture 105°C 125°C
Anthocyanin
Delphinidin 3,5-
diglucoside 31.0 ± 0.4a 28.8 ± 0.5b 28.7 ± 0.2b 28.9 ± 0.5b 29.2 ± 0.2b 28.4 ± 0.6b 28.9 ± 0.5b
Malvidin 3,5-
diglucoside 167 ± 1a 117 ± 5c 116 ± 3c 124 ± 8c 140 ± 4b 110 ± 9c 121 ± 4c
Cyanidin 3,5-
diglucoside 76.9 ± 0.4ab 68.8 ± 1.8b 77.8 ± 4.1ab 77.0 ± 2.5ab 82.3 ± 3.5a 73.8 ± 5.6ab 74.1 ± 2.0ab
Petunidin 3,5-
diglucoside 36.0 ± 0.1a 34.7 ± 0.3c 34.9 ± 0.2bc 34.6 ± 0.2c 35.8 ± 0.3ab 34.8 ± 0.3c 35.2 ± 0.7abc
Pelargonidin 3,5-
diglucoside 17.7 ± 0.1 17.4 ± 0.1 17.4 ± 0.1 17.4 ± 0.2 17.8 ± 0.1 17.7 ± 0.3 17.4 ± 0.1
Peonidin 3,5-
diglucoside 26.8 ± 0.5a 25.3 ± 0.2bc 25.0 ± 0.2bc 24.3 ± 0.5c 24.9 ± 0.1bc 25.0 ± 0.6bc 25.6 ± 0.3b
Flavonoid
Myricetin 221 ± 46 235 ± 5 215 ± 5 214 ± 4 221 ± 7 211 ± 10 218 ± 1
Kaempferol 42.7 ± 0.2ab 39.7 ± 0.7b 43.0 ± 1.5ab 41.5 ± 2.2ab 41.6 ± 0.8ab 42.7 ± 0.9ab 44.7 ± 1.3a
Quercetin n.d. n.d. n.d. n.d. n.d. n.d. n.d.
All data represent means ± standard deviation (n=3). Different superscripts denote significant difference in each extraction method at p< 0.05 using Tukey’s test.
67
Table 3-4. Impact of extraction method on phytochemical content (mg/100g) of Carlos seed flour
Phytochemicals
Soxhlet Screw expression
Hexane 85°C 90°C 90°C at 13%
moisture
90°C at 16%
moisture 105°C 125°C
Anthocyanin
Delphinidin 3,5-diglucoside n.d. n.d. n.d. n.d. n.d. n.d. n.d.
Malvidin 3,5-diglucoside n.d. n.d. n.d. n.d. n.d. n.d. n.d.
Cyanidin 3,5-diglucoside n.d. n.d. n.d. n.d. n.d. n.d. n.d.
Petunidin 3,5-diglucoside n.d. n.d. n.d. n.d. n.d. n.d. n.d.
Pelargonidin 3,5-diglucoside n.d. n.d. n.d. n.d. n.d. n.d. n.d.
Peonidin 3,5-diglucoside n.d. n.d. n.d. n.d. n.d. n.d. n.d.
Flavonoid
Myricetin 181 ± 19 199 ± 25 234 ± 33 214 ± 44 223 ± 42 171 ± 24.3 165 ± 36
Kaempferol n.d. n.d. n.d. n.d. n.d. n.d. n.d.
Quercetin n.d. n.d. n.d. n.d. n.d. n.d. n.d.
All data represent means ± standard deviation (n=3). Different superscripts denote significant difference in each extraction method at p< 0.05 using Tukey’s test.
68
Figure 3-1. HPLC-DAD chromatogram of the anthocyanins in Noble grape seed flour at 520 nm. Peaks 1, 2, 3, 4, and 5
were delphinidin 3,5-diglucoside, cyaniding 3,5-diglucoside, petunidin 3,5-diglucoside, pelargonidin 3,5-diglucoside, and malvidin 3,5-diglucoside, respectively.
min5 10 15 20 25 30 35 40
mAU
0
10
20
30
40
50
601
2
3
4
5
6
69
Figure 3-2. HPLC-DAD chromatogram of the anthocyanins in Noble seed flour and Carlos seed flour at 360 nm. Peaks 1,
2, and 3 were myricetin, quercetin, and kaempferol, respectively.
min 10 20 30 40 50 60 70
mAU
0
10
20
30
40
50
60
1
2
3
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CHAPTER 4 CONCLUSIONS
Muscadine grape seed oil are high in polyunsaturated fatty acids primarily linoleic
(18:2) and possess vitamin E in the form of tocopherol and tocotrienol. Additionally, the
resulting defatted seed flour can possess a wide variety of phytochemicals including
anthocyanin and flavonoids. Different oil extraction methods were shown to have a
significant impact on the quality as well as quantity of oil and resulting flour. Results
suggest that muscadine grape seeds, the byproduct of the wine making industry, could
be utilized in the culinary arts or cosmetics for its high polyunsaturated fatty acids and
antioxidant properties.
The major limitation of this study is the accessibility to the grape pomace and
seeds after pressing. Carlos pomace was only able to be retrieved after pressing at
least a day later and Noble pomace after the fermentation process. Oil seeds are
typically steam treated to denature any oxidative enzymes. In attempting to dry our
seeds faster and denature oxidative enzymes, muscadine seeds were dried in
convection ovens that had no ventilation for moisture, slowing down the drying process
and causing further oxidation in the seeds.
Potential future research areas that can be explored are proper drying methods
for the seeds before extraction, to see if proper drying methods reduce oxidation and
increase vitamin E concentration. Additionally, super-critical fluid extraction could be
another extraction method to explore, as it is used in industry to extract nutraceutical
components and high quality oils.
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BIOGRAPHICAL SKETCH
Brian Wada graduated from California State University of Long Beach with a
Bachelor of Science in nutrition and dietetics in May of 2015. After taking a year off to
work Brian was offered a research assistantship to pursue his education in food science
under the advisement of Dr. Liwei Gu at the University of Florida. Brian graduated in
May 2018 with a master’s in food science and human nutrition.