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Effect of drying treatments on the contents of lutein and zeaxanthin in orange- and yellow-cultivars of marigold flower and its application for lutein ester encapsulation

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IOP Conference Series: Materials Science and Engineering
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Effect of drying treatments on the contents of lutein and zeaxanthin in
orange- and yellow-cultivars of marigold flower and its application for
lutein ester encapsulation
To cite this article: Jovine Marcella Kurniawan et al 2019 IOP Conf. Ser.: Mater. Sci. Eng. 509 012060
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13th Joint Conference on Chemistry (13th JCC)
IOP Conf. Series: Materials Science and Engineering 509 (2019) 012060
IOP Publishing
doi:10.1088/1757-899X/509/1/012060
1
Effect of drying treatments on the contents of lutein and
zeaxanthin in orange- and yellow-cultivars of marigold flower
and its application for lutein ester encapsulation
Jovine Marcella Kurniawan1, Melisa Megawati Yusuf1, Sherly Salsabila Azmi1,
Katarina Purnomo Salim2, Monika Nur Utami Prihastyanti 2, Renny Indrawati
1,2, Heriyanto1,2, Yuzo Shioi 2, Leenawaty Limantara 3, Tatas Hardo Panintingjati
Brotosudarmo1,2,*
1 Department of Chemistry, Faculty of Science and Technology, Universitas Ma
Chung, Jl. Villa Puncak Tidar N-01, Malang 65151, East Java, Indonesia
2 Ma Chung Research Center for Photosynthetic Pigments (MRCPP), Universitas Ma
Chung, Jl. Villa Puncak Tidar N-01, Malang 65151, East Java, Indonesia
3 Center for Urban Studies, Universitas Pembangunan Jaya, Jl. Cendrawasih Raya
B7/P, South Tangerang-15413, Banten, Indonesia
* Corresponding author: tatas.brotosudarmo@machung.ac.id
Abstract. Marigold (Tagetes erecta L.) flower is a potential source of lutein and zeaxanthin. The
drying treatment of marigold flower is necessary during the industrial process for the preparation
of these carotenoids. However, drying treatments with high temperature led the carotenoids
undergo the isomerization reaction. Therefore, the aims of this study are to examine the effect of
several drying treatments on lutein and zeaxantin contents, and to characterize a versatility of
encapsulated lutein ester powder. Separations of the pigments were performed by high-
performance liquid chromatography (HPLC) equipped with photodiode array detector on a C30
column. All-trans isomer of lutein was identified as the major carotenoid of two different
marigold cultivars, i.e. Mega Gold (MG) and Mega Orange (MO). The contents of all-trans
isomers of lutein and zeaxanthin were 8.95 14.55 mg/g dry weight (dw) in MO and 2.56 - 3.73
mg/g dw in MG. The best drying treatment to maintain carotenoid content was freeze drying,
while the treatment with oven at 100°C decreased in carotenoids content up to 38%. The
encapsulated lutein esters by spray drying and freeze drying showed microparticle size with the
different morphological shapes. The encapsulated powders by spray drying produced uniform
particles with sperical shape and smooth as well as concave surfaces, while the broken glass of
encapsulated powders was obtained by freeze drying. MO cultivar of marigold appears to be a
potential source of lutein and zeaxanthin. Encapsulation process may increase in the solubility
of carotenoids and widen its application in food or nutraceutical products.
Keywords: drying treatments, encapsulation, lutein, marigold cultivars, zeaxanthin.
1. Introduction
Marigold (Tagetes erecta L.), belongs to Asteraceae family, has been commercially cultivated in several
countries for ornament, medicinal, religion and industrial uses. Marigold flower shows white to yellow
and orange petal colour indicating the cultivar of flavonoid, essential oil and pigments [1, 2]. These
secondary metabolite compounds act as natural insecticide, antibiotic, nematicide and fungicide [3, 4].
The yellow and orange colours of marigold petals are correlated to the presence of carotenoid pigment.
13th Joint Conference on Chemistry (13th JCC)
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Lutein is the dominant carotenoid and accounts for almost 90%, while zeaxanthin occurs about 5% from
the total carotenoids found in the ester forms [5].
Lutein and zeaxanthin are well known as macular carotenoid because both carotenoids together with
meso-zeaxanthin are accumulated in macula. Bernstein et al. [6] revealed that 25 carotenoids including
lutein have been detected in human milk, serum and tissues. The occurrence of lutein and zeaxanthin in
human is strongly related to their roles in human health. Several studies reported the beneficial health
effects of lutein and zeaxanthin, namely preventing the age-related macular degeneration disease (AMD)
because its function as blue light filter in human eyes [7], acting as antioxidant [8] and anti-inflammation
[9], preventing the skin from UV irradiation [10], and increasing the skin health [11]. Nowadays, lutein
and zeaxanthin have been reported to have important roles on brain, namely developing the brain and
increasing the brain function [12, 13].
Accumulation of lutein and zeaxanthin in the human body is influenced with the daily intake of
macular carotenoid-rich foods and lutein supplements. This fact is due to that carotenoid could not be
biosynthesized by human. Marigold flower is the potential source of lutein and zeaxanthin compared to
the other sources, such as corn, leafy vegetables, etc. [14]. However, the moisture content of fresh
marigold petals ranged from 84% to 90% [15] is very sensitive to microorganism activity causing the
flower to be rotten [16], although the petals can be stand for 3 days after picking. The drying or removing
the water from marigold petals preserved them to have extension shelf-life. Various drying methods
such as freeze drying (FD), sun drying (SD), vacuum oven drying (VOD) and conventional oven drying
(COD) are common methods in industry and have been applied for the pigment-rich plant materials. FD
is a dehydration method that allows the water contained in a frozen material to sublimate and gives the
highest quality of the final product compared with other drying methods containing heating process, but
the cost of FD is higher [17]. The other drying methods, namely SD, VOD and COD are alternative
ways, although the drying treatments with high temperature led the carotenoids undergo to the
isomerization reaction and tends to have lower bioavailability [18]. Preserving of the carotenoid quality
and lowering of the production cost are selection criteria for the suitable drying method.
However, macular carotenoid as well as carotenoids in general have an unstable tendency against
environmental factors, i.e. light irradiation, temperature, and oxidation. Their applications on the food
and drink products are also limited due to poor solubility in water. Therefore, their bioavailability is
low. Encapsulation technology is employed to improve stability and solubility and also to control release
of lutein surrounded by coating agents [19]. The most common techniques for encapsulation of bioactive
compounds, such as lutein, anthocyanin, phenolic and flavonoid, are spray drying and freeze drying [20-
22]. Fast water evaporation, low cost and powder form are the main reasons to use spray drying
technique for the food industry [23]. Nevertheless, parameters in spray drying must be optimized
especially for encapsulated heat-sensitive bioactive compounds which can be easily decomposed in high
temperature. On the other hand, freeze drying is preferably applied to minimize the compound
degradation, although the uses of freeze drying have several disadvantages compared to the spray drying.
The study of effect of several drying treatments on the carotenoid in marigold petals is necessary.
The effect of drying treatments on the content of lutein and zeaxanthin in local marigold in Indonesia
was analysed using UV-Vis spectrophotometer and high performance liquid chromatography (HPLC).
Initially, the optimization of extraction solvent was performed to have the best organic solvent for
extracting carotenoid from the powder of marigold petals. Besides that, the encapsulation of lutein esters
using a mixture of maltodextrin and gum Arabic as coating agents was prepared by spray drying and
freeze drying to characterize the morphology of encapsulated lutein ester from the SEM images.
2. Materials and Methods
2.1. Materials
Two cultivars of marigold flowers, namely Mega Orange (MO) and Mega Gold (MG) were harvested
from a traditional marigold plantation in Tabanan, Bali.
13th Joint Conference on Chemistry (13th JCC)
IOP Conf. Series: Materials Science and Engineering 509 (2019) 012060
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doi:10.1088/1757-899X/509/1/012060
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2.2. Methods
2.2.1. Sample Preparation. The fresh marigold petals of MO and MG cultivars were separated from
receptacle and then the petals were frozen (20°C) until the drying treatments. The petals were dried by
5 different drying methods, namely FD (45°C, 0.04 hPa), VOD (40°C, 24 hPa), SD (39°C), COD-40
(40°C) and COD-100 (100°C). The petals were dried until the moisture content less than 10%. The dried
petals were then ground and sieved with the particle size of 180 µm, and stored at 20°C in the dark.
2.2.2. Carotenoid Extraction and Saponification. The marigold powder (0.01 g) was extracted with
different organic solvents (1 mL), i.e. n-hexane (100%), acetone (100%), ethanol (100%) and a mixture
of ethanol and n-hexane (4:3, v/v), and then the pigment extracted with the optimum solvent was
saponified for HPLC analysis. The extraction process was carried out by vortexing and continued with
the centrifugation (14,000 rpm, 2 min, room temperature) to separate the carotenoid extract from the
residue. The extraction was repeated until the residue becomes pale and the accumulated supernatants
were dried using nitrogen gas (UHP). The saponification of crude carotenoids was performed by
dissolving the dried carotenoids in 10 mL diethyl ether (DE) and the pigment solution was added into
10 mL ethanolic solution containing 10% potassium hydroxide. The mixture was incubated at room
temperature for 2 h in the dark while. The carotenoid in DE layer was washed with water and then
carotenoid solution was dried using rotary evaporator (40°C). The dried carotenoid was kept at 30°C
in the dark.
2.2.3. Carotenoid Identification and Quantification. The identification of carotenoid from the crude
extract and saponified extract from marigold powder was performed by HPLC (Shimadzu, Kyoto,
Japan), equipped with photodiode array detector. The sample was dissolved in 1 mL of acetone, filtered
using a filter membrane (PTFE, 0.2 μm) and then injected to HPLC with 20 μL of sample loop. Pigment
separation was performed on a YMC carotenoid C30 column (150 × 4.6 mm I.D.) with gradient elution
program of methanol, methyl tert-butyl ether and water (81:15:4 (v/v/v) at 0 min and 6:90:4 (v/v/v) at
70 min), and the flow rate was 1 mL/min. The identification of the carotenoid was based on the positions
of absorption maxima (λmax), the characteristic shape of its absorption spectra and the retention time
with comparison to the literature [24]. The content of carotenoid was calculated by using standard curve
equation of lutein (y=262.27x+42.92, r2 = 0.9997) and zeaxanthin (y=225.14x-159.29, r2 = 0.9997)
between concentration of carotenoid in µg/mL and peak area at its λmax.
2.2.4. Encapsulation of Lutein Esters. Encapsulation of lutein esters was performed by the modified
method of Pal and Bhattacharjee [25]. Lutein esters were dissolved in 3 mL of virgin coconut oil and
then dispersed into 100 mL of aqueous solution containing 45 g of wall materials consisted of
maltodextrin and gum Arabic (60:40, w/w). The mixture was stirred for 30 mins (450 rpm, Heidolph
MR-Hei Standard) at room temperature (25°C) and then continued by homogenization process using
IKA Turrax (11,000 rpm, 8 mins, 25°C). The encapsulated product was kept at 4°C in the dark prior to
spray drying and freeze drying processes. The spray drying process was carried out using a mini spray
dryer (B-290, Buchi, Switzerland) to obtain the powder form of encapsulated lutein esters at following
parameters: 160170°C of the inlet temperature, 0.7 mm of diameter dispersing nozzle, and 60 hPa of
atomization pressure. In the freeze drying process, the solution of encapsulated lutein esters was initially
frozen at 30°C for 1 day and then subjected to freeze dry for 48 h at 60°C and 0.032 hPa (Alpha 1-2
LDplus, Martin Christ, Germany). The dried product was ground and then sieved to 150 μm of particle
size containing 10.5% of water content. The dried powders of encapsulated lutein esters prepared by
spray drying and freeze drying were kept at 30°C.
2.2.5. Characterization of Encapsulated Lutein Esters. The morphology of the encapsulated lutein esters
was determined by scanning electron microscope (SEM) (SU3500, Hitachi, Tokyo, Japan). Prior to SEM
analysis, the encapsulated powders were sprinkled onto double-side conductive adhesive tape attached
on an aluminium specimen stub and then the excess powder was removed by blower. The surface of
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encapsulated powders was coated with gold (Au) using an ion sputter coaster (MC1000, Hitachi) under
vacuum. The SEM analysis was operated at 5 kV with the working distance of 6.5 mm.
3. Results and Discussions
3.1. Visual Appearance of Dried Marigold Powder
The dried powders of MO and MG cultivars were shown in Fig. 1. According to the visual appearance,
the dried powders of MO cultivar were more orange than those of MG. The MO powders obtained by
VOD, COD-40 and COD-100 have dark orange colour, while FD showed the bright one. The MO dried
by SD was less orange than the others. The visual colour of MG powders obtained from drying marigold
petals with SD, COD-40 and COD-100 showed significant colour alteration compared with that of FD
which is changed from orange to pale yellow. Effect of drying treatments against marigold colour had
been reported by Siriamornpun et al. [26] and Ahluwalia et al. [27]. The colour change of marigold
powder was caused by thermal process that leads non-enzymatic browning reaction and degradation of
carotenoid inside the marigold. The colour change of marigold powders which turned darker was
occurred due to the browning reaction, i.e., MO dried by VOD and COD, MG dried by VOD, while the
changes of the powders from orange to pale yellow indicated the degradation of carotenoids [26]. FD
was found as suitable drying method for maintaining the colour of marigold compared to the colour of
the fresh petals for both cultivars. The colour of marigold powders depends on the concentration of
carotenoids, lutein and zeaxanthin. The concentration of these macula carotenoids for each marigold
powder will be discussed in the next section.
Figure 1. Visual appearance of marigold powders with different drying
methods, FD (a), VOD (b), SD (c), COD-40 (d) and COD-100 (e).
3.2. Carotenoid Extraction
The absorption spectra of crude carotenoid extracts from the marigold powders extracted with organic
solvents and aqueous solutions were shown in Fig. 2. The FD powders of MO cultivar extracted using
a mixture of ethanol and hexane (4:3, v/v) showed the highest absorbance value in 1 g dw of powders
at its λmax (158 a.u.), followed by hexane (151 a.u.) and acetone (150 a.u.), while the ethanol extract had
the lowest absorbance (116 a.u.) (Fig. 2a). The pattern of these results was in line with the results of MG
cultivar (data not shown), however the absorbance values in the absorption spectra of crude carotenoid
extracts from MG cultivar were lower compared to those of MO cultivar. The low extractability of
carotenoids from marigold powders using ethanol and water (Fig. 2b) is probably due to the occurrence
of carotenoid fatty acid esters which have high solubility in oil and non-polar solvents instead of polar
solvent and aqueous solution. The absorption around 320-400 nm in absorption spectra of carotenoid
extracted with water, ethanol, acetone and a mixture of ethanol and hexane of MO and MG cultivar were
related to the absorption of flavonoid compounds [28]. Ethanol and acetone as well as their aqueous
solution had been reported as common solvents for extracting the flavonoid from the dried marigold
[29, 30]. The absorption of flavonoid compounds may contribute to the absorption of crude carotenoid
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extract of marigold. On the other hand, there was no absorption of those compounds in the hexane
extract, therefore, the pigment extracted using hexane was chosen as the optimum extract and it will be
discussed in the section of carotenoid analysis by HPLC.
Figure 2. Absorption spectra of crude carotenoid extracts from FD-dried MO
powders extracted with a mixture of ethanol and hexane (4:3, v/v) (black),
100% ethanol (red), 100% hexane (blue) and 100% acetone (orange) (a), and
with water (black) and 100% ethanol (red) (b). The unit of absorbance was
calculated in 1 g dry weight (dw) basis.
3.3. Carotenoid Analysis by HPLC
HPLC chromatograms of saponified and unsaponified crude carotenoid extracts detected at 445 nm were
shown in Fig. 3a. In the saponified extract the dominant peak eluted at 8.2 min was identified as free
all-trans lutein, while carotenoid fatty acid esters were detected in between of 38 min and 50 min in the
unsaponified extract [5]. Bunea et al. [31] reported that carotenoid fatty acid esters had higher retention
time than their free forms when these carotenoids were separated on a reversed phase column. The
degree of saturation and length of the fatty acid chains that bind to the carotenoid affects their retention
time [31]. The lutein esters contained in the unsaponified crude carotenoid extract of marigold
represented almost 95% of total carotenoids, mainly in the forms of lutein laurate-myristate, dimyristate,
myristate-palmitate, palmitate-stearate and distearate diesters [32]. De-esterification of lutein esters to
the free lutein is performed by saponification process using alcoholic solution, ethanol containing
potassium hydroxide [33, 34]. The acylation of lutein does not affect their spectral characteristics. In
fact, the absorption spectra of free lutein and lutein esters in hexane had similar λmaxs at 423, 445 and
473 nm as well as their spectral shape (Fig. 3b). Free- and esterified-lutein could be distinguished by
chromatographic measurement instead of spectrophotometry analysis.
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Figure 3. HPLC chromatograms detected at 445 nm of unsaponified (red) and saponified
(black) crude carotenoid extracts from MO cultivar dried by FD (a) and absorption spectra
of the free lutein (black) and lutein esters (red) in hexane (b). Intensity of HPLC
chromatograms was calculated in 1 g dw basis, while absorbance value of absorption
spectra was normalized at 1.
The separation of free carotenoids from marigold powder could be done less than 11 min using RP-
HPLC on C30 column with the gradient elution program of H2O, MeOH and MTBE mixture. Fig. 4a
shows HPLC chromatograms of saponified crude carotenoid extracts from MO-FD and MG-FD. These
two cultivars of marigold have similar elution profiles with the same peaks such as peaks 1, and 4-8,
indicating that those cultivars have the same carotenoid composition. The identification of each peak
was according to the chromatographic and spectrophotometric properties as well as the result of co-
chromatography analysis with the carotenoid standards. Table 1 summarizes the identification of
carotenoids for each peak. Peak 7 was identified as all-trans isomer of lutein which has λmaxs at 424,
445, and 472 nm and the largest peak area (65 - 85%) compared to other carotenoid peaks. The studies
of Hadden et al. [18] and Pratheesh et al. [35] proved that lutein was the dominant carotenoid in marigold
flower, while zeaxanthin was one of other minor carotenoids. Peak 8 had λmaxs at 428, 450, and 476 nm
which belong to zeaxanthin. The identification of lutein and zeaxanthin was supported with the results
of co-chromatography between saponified carotenoid extract and lutein or zeaxanthin standard (data not
shown). Peaks 1 and 4 were confirmed to be violaxanthin and antheraxanthin, respectively, [36]. Peaks
5, 6, and 9 were identified as the cis-isomers of lutein which show the additional cis absorption band at
330-331 nm in their absorption spectra.
HPLC chromatogram of saponified carotenoid extract from MO-COD-100 (Fig. 4b, red colour)
showed the additional two peaks, 2 and 3, which can be identified as cis-isomers of carotenoid due to
the presence of cis absorption band. In addition, Fig. 4 left (insert) indicated that cis-isomer peaks, 2, 3,
5, and 6, were formed and significantly increased after the drying treatment with the COD at 100°C. On
the contrary, the peak area of all-trans isomers of carotenoids decreased especially for the peak of all-
trans isomer of lutein. The isomerization mechanism of all-trans isomer of lutein into its cis-isomers
was proposed by Updike and Schwartz [37]. In addition, the isomerization or degradation of carotenoid
is known to be caused by the thermal oxidation. The drying with COD-100 on the marigold flower
totally degrades the violaxanthin and antheraxanthin. It is reported that violaxanthin and antheraxanthin
as the epoxy-carotenoid group degraded faster due to the formation of furanoid caused by epoxide
isomerization [38]. The ester forms of hydroxyl-carotenoids, lutein and zeaxanthin contained in
marigold flower were more stable in the heat treatment compared to the free from of carotenoids.
13th Joint Conference on Chemistry (13th JCC)
IOP Conf. Series: Materials Science and Engineering 509 (2019) 012060
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Figure 4. HPLC chromatograms detected at 445 nm of saponified carotenoid extracts of
MO (black) and MG (red) cultivars of marigold dried by FD (a), and MO-FD (orange)
and MO-COD-100 (blue) (b). The intensity unit was calculated in 1 g dw.
Table 1. Identification of carotenoids from saponified carotenoid extracts of MO and MG
based on the retention time and λmaxs in HPLC solvent.
Peak number
Retention time [min]
λmaxs [nm]
1
4.4
- , 416, 439, 469
2
5.2
- , - , 432, 454
3
5.6
- , - , 433, 456
4
6.5
- , 421, 444, 470
5
6.9
331, 421, 439, 466
6
7.6
330, 422, 438, 464
7
8.3
- , 424, 445, 472
8
9.7
- , 428, 450, 476
9
10.5
330, - , 441, 468
Note: * refer to Gupta et al. [36] and Updike and Schwartz [37].
The contents of lutein and zeaxanthin were calculated using the equations of standard curves (r2 =
0.9997) for lutein and zeaxanthin which are expressed as mg of carotenoid in 1 g dw. The contents of
lutein and zeaxanthin in MO and MG cultivars obtained by several drying methods are shown in Table
2 and Fig. 5. The contents of lutein and zeaxanthin of MO cultivar dried by FD from crude carotenoid
extract prepared by extraction with 100% hexane were 13.94 mg/ g dw and 0.61 mg/g dw, respectively.
These carotenoid contents were higher compared to the same sample extracted with a mixture of ethanol
and hexane (4:3, v/v) which was having 9.68 mg/g dw of lutein and 0.40 mg/g dw of zeaxanthin. Hexane
had been used as extraction solvent of carotenoids from the powder of marigold petals [39]. Recently,
Boonnoun et al. [34] evaluated the extraction conditions on the yield of lutein esters from the dried
marigold using extractions of hexane, liquefied DME and SC-CO2. The hexane extraction had higher
yield of lutein esters compared to that of SC-CO2, although DME extraction produced the highest yield.
The lutein content in MO and MG cultivars were 25 and 15 times higher than those of zeaxanthin,
respectively. Moreover, the total carotenoids, contents of lutein and zeaxanthin, in MO cultivar was
almost four times higher than those of MG. This result was in line with experimental report of Piccaglia
et al. [40] dealing with the colour of marigold flower depends on the carotenoid content. Lin et al. [41]
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also identified the sub species of Tagetes erecta by the colour, namely yellow, orange or brown which
is indicated with the different amounts of lutein. Lutein content increases as the marigold colour
intensifies becoming more orange. Li et al. [42] and Ingkasupart et al. [2] reported about the lutein and
lutein ester contents in 11 marigold cultivars grown in Thailand and in China ranging from 8.31 to 20.59
mg of lutein/g dw and 1.61 to 6.11 mg of lutein esters/g dw, respectively. The lutein content of marigold
from Thailand is in the range to that of MO cultivar of local marigold from Indonesia (8.61 13.94 mg/g
dw; Table 2), while the content of lutein esters of marigold cultivars from China was lower 1.4 to 8.7
times. Thus, MO cultivar of Indonesian local marigold has high potency as the source of lutein.
Table 2. Lutein and zeaxanthin contents in MO and MG cultivars of marigold
flower dried by several drying methods.
Drying Method
Carotenoid Content [mg/g d.w. ± SE]
Lutein
Zeaxanthin
Mega Orange
Mega Gold
Mega Orange
Mega Gold
FD
13.94 ± 0.62
3.51 ± 0.21
0.61 ± 0.06
0.22 ± 0.01
VOD
13.23 ± 0.12
3.24 ± 0.21
0.60 ± 0.05
0.22 ± 0.02
COD-40
12.46 ± 0.21
3.15 ± 0.14
0.44 ± 0.01
0.20 ± 0.01
SD
10.46 ± 0.60
2.55 ± 0.23
0.40 ± 0.02
0.16 ± 0.02
COD-100
8.61 ± 0.33
2.42 ± 0.21
0.34 ± 0.02
0.14 ± 0.01
Figure 5. Bar charts of lutein (a) and zeaxanthin (b) contents (mg/g dw) from MO cultivar (red) and
MG cultivar (orange) of marigold flower dried by FD, VOD, COD-40, SD and COD-100. Carotenoid
contents are averaged of 3 replications and bars represent standard error.
Fig. 5 shows the comparison of lutein and zeaxanthin contents from MO cultivar and MG cultivar of
marigold after drying by different methods. The dried marigolds by FD and VOD had higher lutein and
zeaxanthin contents compared to other drying methods. There was no significant difference on the
contents of lutein and zeaxanthin between both methods, indicating that FD and VOD were suitable
method for maintaining the colour of dried marigolds as well as the carotenoid content. This result is in
agreement with previous results of Siriamornpun et al. [26] and Ahluwalia et al. [27] that showed less
colour alteration and higher bioactive compounds contained after drying the marigold with FD and VOD
method. As drying method, COD-40 and SD can be used as alternative methods because of the economic
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reasons, but these drying methods required longer time to reach the water content less than 10%. The
least drying method, COD-100, decreased the lutein and zeaxanthin contents up to 38% for MO and
30% for MG. In addition, thermal processing of marigold by COD-100 lead the carotenoid
isomerization. Therefore, COD-100 was not suitable for drying the marigold flowers
3.4. Characterization of Encapsulated Lutein Ester
SEM micrographs of the encapsulated lutein esters obtained by spray drying and freeze drying with
magnification of 1000 and 100, respectively, are shown in Fig. 6. Fig. 6a shows that particles of
encapsulated lutein ester resulted by spray drying were formed in the heterogeneous forms. The particles
with different sizes including large particles are correlated to agglomeration [43] and produced using
maltodextrin as coating agent [44], while Ferrari et al. [44] revealed that small particles of encapsulated
powders were obtained with gum arabic. Particle sizes of the encapsulated powders were in the range
of 1.1224.80 µm (mean of particle diameter = 9.56 µm). The morphology of encapsulated powder
showed spherical shape and smooth outer surface, although there was a concavity as the result of
shrinkage during rapid water removal process, related to the temperature of gas inlet that is a parameter
used in the spray drying. The result by morphological observation was similar with Pal and
Bhattacharjee [25] and Ferrari et al. [44] which reported the spray drying of encapsulated lutein and
anthocyanin, respectively, using maltodextrin and gum arabic as wall materials. The usage of different
wall materials, such as maltodextrin and β-cyclodextrin, for spray drying also showed the same
morphology with concave surface, i.e., without cracks or pores Papoutsis et al. [22]. Encapsulation of
lutein with copovidone at 100120°C as the temperature inlet produced smooth and spherical micro-
particles [19]. Therefore, the formation of concavities in the particle surface is not associated with the
type of wall material used, but depends on the spray-drying parameters. In contrast, the encapsulated
powders obtained by freeze drying process showed a broken glass or flakes-like form, where the
maximum size of the particles was less than 150 µm due to the sieving process (Fig. 6b). This structure
is related to the process of sublimation of the water contained under low temperature, so there is no force
to produce the droplet [22].
Figure 6. SEM micrographs of encapsulated lutein ester containing maltodextrin and gum arabic
prepared by spray drying with magnification of 1000 (a) and freeze drying with magnification of
100 (b).
4. Conclusions
The effect of drying treatments for marigold flower on the lutein and zeaxanthin contents was varied.
The FD and VOC have the highest content of both carotenoids followed by COD-40 > SD > COD-100.
MO and MG cultivars of marigold flower have the same pattern on carotenoid contents against drying
13th Joint Conference on Chemistry (13th JCC)
IOP Conf. Series: Materials Science and Engineering 509 (2019) 012060
IOP Publishing
doi:10.1088/1757-899X/509/1/012060
10
treatment. Lutein was the dominant carotenoid in MO cultivar dried by FD containing 13.94 mg/g dw
which was extracted with 100% hexane, while the zeaxanthin content is almost 22.128.3 times and
14.717.3 times lower compared to those of lutein in MO cultivar and in MG cultivar, respectively.
SEM analysis of encapsulated lutein esters by spray draying showed that the powders had spherical
shape with uniform sizes of micro particles (1.1224.80 μm), while the encapsulated powders prepared
by freeze drying showed the broken glass shape with the particle sizes less than 150 μm.
Acknowledgement
This study was supported by National Innovation System Research Grant provided by Ministry of
Research, Technology, and Higher Education of the Republic of Indonesia (No. 25/INS-
2/PPK/E4/2018).
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... However, spray drying conditions must be improved, particularly for heat-sensitive bioactive chemicals encapsulated and readily broken at high tempera-tures. However, compared to spray drying, freeze-drying has several drawbacks that make it less desirable for minimizing compound degradation [30]. The most widely utilized drying process in the food industry right now is spray drying. ...
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Extraction of xanthophylls from marigold flowers using liquefied dimethyl ether (DME) was investigated. The most suitable DME extraction condition was found to be 33:0.5 (w/w) DME to dried marigold flowers ratio and at 35 °C, giving 20.65 mg of total xanthophylls/g of dried marigold flowers. Following extraction, the suitable de-esterification conditions to convert the extracted lutein fatty acid ester (the major compound in xanthophylls) to free lutein, a more bio-available form, were determined to be 2.5%w/v KOH–EtOH, at 35 °C for 4 h. While employing the most suitable conditions in each of the two steps gave favorable free lutein yield (16.65 mg free lutein/g dried marigold flowers), a one-step process in which simultaneous extraction and de-esterification carried out at the most suitable condition: the DME to dried marigold flowers ratio 33:0.5 (w/w), EtOH to dried marigold flowers ratio 10:0.5, 5% KOH–EtOH concentration, at 35 °C for 1 h, could lead to about 20% improvement (20.71 mg free lutein/g dried marigold flowers). Furthermore, the results from this study suggested that wet marigold samples could possibly be used both in the DME extraction for xanthophylls and in the simultaneous process to obtain free lutein.
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Background and aims: Many coronary artery disease (CAD) patients exhibit chronic low-grade inflammation. Carotenoids are anti-oxidants with potential anti-inflammatory properties. Here, we first assessed relationships between interleukin (IL)-6 and individual carotenoids in plasma from CAD patients. Based on the results, we proceeded to assess anti-inflammatory effects of one carotenoid, lutein, in peripheral blood mononuclear cells (PBMCs) from CAD patients. Methods: Lutein + zeaxanthin (isomers with lutein being dominant), β-cryptoxanthin, lycopene, α- and β-carotene and IL-6 were measured in plasma from 134 patients with stable angina (SA) and 59 patients with acute coronary syndrome. In 42 patients, plasma measurements were also performed 3 months after coronary intervention. PBMCs from SA patients were pre-treated with lutein (1, 5 and 25 μM) for 24 h followed by 24 h incubation ± lipopolysaccharide (LPS). Cell pellets were collected for IL-6, IL-1β and TNF mRNA and intracellular lutein. Cytokine secretion was measured in cell media. Results: Only lutein + zeaxanthin were inversely correlated with IL-6 in SA patients at baseline (r = -0.366, p < 0.001) and follow-up (r = -0.546, p < 0.001). Ex vivo, lutein was taken up by PBMCs from SA patients in a dose- and time-dependent manner. Pre-treatment with lutein dose-dependently lowered LPS-induced secretion of IL-6, IL-1β (p < 0.01) and TNF (p < 0.05), and also reduced IL-6, IL-1β and TNF mRNA expression (p < 0.05). Conclusions: Clinical findings highlighted the inverse association between lutein and IL-6 in CAD patients. Anti-inflammatory effects of lutein in PBMCs from CAD patients were consolidated in ex vivo experiments. Taken together, these results show that lutein has the potential to play a role in resolution of chronic inflammation in CAD patients.
Article
Lutein (LUT), is one of the most important carotenoids having prominent antioxidant activity. However, its use is limited due to poor solubility and instability under adverse conditions. LUT was microencapsulated with soluble polymers using spray drying to improve its solubility and bioavailability. Maltodextrin (polysaccharide base) and copovidone (polyvinyl pyrrolidone vinyl acetate based copolymer) were evaluated as hydrophilic carriers for encapsulation of LUT. Design of Experiments (DOE) was utilized and microencapsulation process was optimized using full factorial design. Copovidone proved to be better carrier compared to maltodextrin and showed enhanced dissolution and antioxidant characteristics of LUT. Microencapsulated LUT powder was characterized by dissolution study, DSC, XRD and SEM. This study can be used as a guideline for optimization of microencapsulation of similar bio-actives with hydrophilic carriers to improve solubility and subsequent bioavailability.
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Drying is an important process parameter for preservation of food components and it is widely applicable in food sectors. Nowadays, encapsulation by drying technology is of growing interest to provide many useful effects in food industry. Encapsulation of several drying techniques (spray drying, freeze drying, fluidized bed coating) is a challenge to incorporate food component, antioxidant, colorant, cells and enzymes in powder form in food products. By drying, encapsulation achieves excellent properties of protection, stabilization, solubility and controlled release of the bioactive compounds. There are many reasons to apply encapsulation technology by drying, so recent developments of encapsulation are discussed in this review. Controlled release of food component at the right place at right time is a key functionality that can be provided by encapsulation. Drying improves effectiveness of food additives, broadens the application range of food ingredients, enhances shelf life of the food and lowers cost of the food products.