1 An integrated approach for the valorization of mango seed kernel: efficient extraction
2 solvent selection, phytochemical profiling and antiproliferative activity assessment.
3
4 Diego Ballesteros-Vivas1,2a, Gerardo Alvarez-Rivera2a, Sandra Johanna Morantes Medina3
5 Andrea del Pilar Sánchez Camargo1, Elena Ibánez2, Fabián Parada-Alfonso1, Alejandro
6 Cifuentes2*
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8 1 High Pressure Laboratory, Department of Chemistry, Faculty of Science, Universidad
9 Nacional de Colombia, Carrera 30 #45-03, Bogotá D.C., 111321, Colombia.
10 2 Laboratory of Foodomics, Institute of Food Science Research, CIAL, CSIC, Nicolás Cabrera
11 9, 28049 Madrid, Spain.
12 3 Unit of Basic Oral Investigation (UIBO), School of Dentistry, Universidad El Bosque, Av.
13 Carrera 9 #131 A-02, Bogotá D.C., 110121, Colombia.
14 15 a These two authors contributed equally to this work.
16
17 *Corresponding author:
18 Prof. Dr. Alejandro Cifuentes, Laboratory of Foodomics, Institute of Food Science Research,
19 CIAL (CSIC), Nicolás Cabrera 9, 28049 Madrid, Spain, e-mail: [email protected], Tel.: +34
20 910017955; fax: +34 910017905.
21
22 Keywords:
23 Mangifera indica L.; fruit by-products; Hansen solubility parameters; Pressurized-liquid
24 extraction; LC-Q-TOF; GC-Q-TOF; High-resolution mass spectrometry; antiproliferative
25 activity; HT-29 cell line; CCD-18Co cell line.
26
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27 ABSTRACT
28 A novel valorization strategy is proposed in this work for the sustainable utilization of a major
29 mango processing waste (i.e. mango seed kernel, MSK), integrating green pressurized-liquid
30 extraction (PLE), bioactive assays and comprehensive HRMS-based phytochemical
31 characterization to obtain bioactive-rich fractions with high antioxidant capacity and
32 antiproliferative activity against human colon cancer cells. Thus, a two steps PLE procedure
33 was proposed to recover first the non-polar fraction (fatty acids and lipids) and second the polar
34 fraction (polyphenols). Efficient selection of the most suitable solvent for the second PLE step
35 (ethanol/ethyl acetate mixture) was based on the Hansen solubility parameters (HSP) approach.
36 A comprehensive GC- and LC-Q-TOF-MS/MS profiling analysis allowed the complete
37 characterization of the lipidic and phenolic fractions obtained under optimal condition (100%
38 EtOH at 150°C), demonstrating the abundance of oleic and stearic acids, as well as bioactive
39 xanthones, phenolic acids, flavonoids, gallate derivatives and gallotannins. The obtained MSK-
40 extract exhibited higher antiproliferative activity against human colon adenocarcinoma cell line
41 HT-29 compared to traditional extraction procedures described in literature for MSK utilization
42 (e.g. Soxhlet), demonstrating the great potential of the proposed valorization strategy as a
43 valuable opportunity for mango processing industry to deliver a value-added product to the
44 market with health promoting properties.
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52 1. INTRODUCTION
53 Mango (Mangifera indica L.) is one of the most important tropical fruit crops, with an annual
54 production of more than 38 million tonnes (Mitra, 2016). The commercial importance of mango
55 fruit is due, among other reasons, to its sensorial quality attributes, high nutritional value and
56 functional compounds content (Ediriweera, Tennekoon, & Samarakoon, 2017; Gentile et al.,
57 2019; Ribeiro & Schieber, 2010). Colombia plays an increasing role in world mango
58 production with cultivars such as ‘Sugar mango’, recognized by its sensorial qualities
59 (Corrales-Bernal, Maldonado, Urango, Franco, & Rojano, 2014). The industrial mango
60 processing generates about 40–60% of fruit wastes (12–15% of peels and 15–20% of kernels
61 seeds); none of them currently used for commercial purposes (Nawab, Alam, Haq, & Hasnain,
62 2016). Recently, several researches about the chemical composition and bioactive potential of
63 mango seed kernel (MSK) have been reviewed (Jahurul et al., 2015; Torres-León et al., 2016).
64 MSK contains important families of health-promoting compounds including fatty acids and
65 triacylglycerols (Lieb et al., 2018), gallotanins (Luo et al., 2014), xanthones (e.g. mangiferin)
66 (Barreto et al., 2008), flavonoids and phenolic acids, among others (Dorta, González, Lobo,
67 Sánchez-Moreno, & de Ancos, 2014; Lopez-Cobo et al., 2017). Polyphenolic compounds from
68 mango have been reported to have a strong antioxidant activity (Barreto et al., 2008; Soong &
69 Barlow, 2006; Sultana, Hussain, Asif, & Munir, 2012), and exhibit bioactivity in cancer cell
70 line models, including breast, liver, leukemia, cervix, prostate, lung and colon (Abdullah,
71 Mohammed, Rasedee, & Mirghani, 2015; Abdullah, Mohammed, Rasedee, Mirghani, & Al-
72 Qubaisi, 2015; Luo et al., 2014; Timsina & Nadumane, 2015). In particular, mangiferin (2-β-
73 D-glucopyranosyl-1,3,6,7-tetrahydroxy-9H-xanthen-9-one) has been reported as one of the
74 most bioactive phytochemicals in mango; in both in vitro and in vivo models (Imran et al.,
75 2017).
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76 Considering the bioactive potential of MSK, the development of green valorization strategies
77 to obtain polyphenolic-rich extracts from this valuable biowaste, pose a great challenge and a
78 unique opportunity for mango processing industry to deliver a value-added product to the
79 market with health promoting properties. Thus, strategies based on efficient extraction solvent
80 selection and use of new green extraction processes can help fulfilling the goals of the green
81 extraction of natural products (Chemat, Vian, & Cravotto, 2012). Hansen solubility parameters
82 (HSP) was shown to be a useful predictive model to ascertain the solubility of solutes, such as
83 secondary metabolites, in different solvents through their affinity and miscibility estimation.
84 In terms of new green extraction processes, Pressurized Liquid Extraction (PLE) is a
85 recognized environmentally friendly technique due to its higher extraction efficiency, lower
86 solvent consumption, short extraction time and the possibility of using green solvents (Ameer,
87 Shahbaz, & Kwon, 2017; Herrero, Castro-Puyana, Mendiola, & Ibañez, 2013). Several
88 research works have been conducted employing the joint strategy involving HSP+PLE to
89 target bioactive compounds recovery from natural sources (Ballesteros-Vivas et al., 2019;
90 Damergi et al., 2017; Sánchez-Camargo et al., 2017; Srinivas, King, Monrad, Howard, &
91 Hansen, 2009).
92 In this context, the present research aimed to develop an integrated valorization strategy,
93 involving HSP approach and sequential PLE procedure, in vitro antioxidant assays and
94 comprehensive characterization with advanced analytical techniques (liquid chromatography
95 and gas chromatography coupled to high resolution mass spectrometry) to obtain mangiferin
96 and other phenolic compounds from ‘sugar MSK’ with selective antiproliferative activity
97 against human colon adenocarcinoma cell line HT-29. An integrated process scheme of the
98 proposed MSK valorization strategy is shown in Figure 1.
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101 2. MATERIAL AND METHODS
102 2.1 Samples and reagents
103 Sugar mango fruits were purchased from a local market in Bogotá D.C., Colombia in February
104 2018. Mango fruit by-products were obtained after mechanical pulping process. Seeds were
105 split into coat and kernel (endosperm). ‘Sugar MSK’ (5.3% moisture content) was dried at
106 room temperature in the darkness during 48 h, subsequently ground to fine powder and stored
107 at -20 °C until its use.
108 Gallic acid, quercetin, trolox, 2,2'-azino-bis(3-ethylbenzothiazoline-6-sulphonic acid) (ABTS),
109 2,2-diphenyl-1-picrylhydrazyl (DPPH), 3-(4,5-dimethylthiazol-2-yl)-2,5-diphenyltetrazolium
110 bromide (MTT), RPMI-1640 cell culture medium, streptomycin (0.1 mg/mL), penicillin (100
111 U/mL) potassium acetate, ammonium acetate, sodium carbonate, formic acid, potassium
112 persulfate, aluminum chloride, were purchased from Sigma-Aldrich (Madrid, Spain). Fetal
113 bovine serum (Gibco) and 0.05% trypsin-EDTA (Gibco) were purchased from Thermo Fisher
114 Scientific (Rockford, IL). Merck (Darmstadt, Germany) provided the Folin-Ciocalteu phenol
115 reagent. Solvents employed were HPLC-grade. Acetonitrile, chloroform, ethanol and methanol
116 were acquired from VWR Chemicals (Barcelona, Spain), whereas ethyl acetate by Scharlau
117 (Barcelona, Spain). Ultrapure water was obtained from a Millipore system (Billerica, MA,
118 USA). For the UPLC-q-TOF-MS analyses, MS grade ACN and water from LabScan (Dublin,
119 Ireland) were employed.
120
121 2.2 Hansen Solubility Parameters estimation
122 HSP for mangiferin and green solvents, including ethanol, ethyl acetate, ethyl lactate and (+)-
123 limonene, were estimated using HSPiP® software v 5.0 at normal conditions, following the
124 methodology previously reported by Sánchez-Camargo et al (Sánchez-Camargo et al., 2017).
125 Briefly, the SMILES (Simplified molecular input line syntax) of mangiferin
5
126 [C1=C2C(=CC(=C1O)O)OC3=CC(=C(C(=C3C2=O)O)C4C(C(C(C(O4)CO)O)O)O)O] was
127 break into corresponding functional groups using Yamamoto-molecular break (Y-MB) method
128 and then HSP parameters were estimated by “Do It Yourself” tool. Subsequently, the affinity
129 between the mangiferin and the green solvents was measured by Ra or “distance” term using
130 their HSPs values through “Solvent optimizer” tool (the smaller Ra corresponding to the greater
131 affinity between solvent and solute). The variation of Ra at different temperatures (25-150 °C)
132 was also studied. For this purpose, the temperature dependence of mangiferin solubility
133 parameters was estimated by Jayasri and Yaseen method (Jayasri & Yaseen, 1980), employing
134 the critical data obtained by Marrero & Gani group contribution method (Marrero & Gani,
135 2001). The temperature effect on HSPs of green solvents was evaluated by the Gunn-Yamada
136 (Pereira, Silva, & Rodrigues, 2011) and Williams et al. (Williams, Rubin, & Edwars, 2004)
137 methods. Finally, Ra between mangiferin and green solvents were estimated at different
138 temperatures.
139
140 2.3 Pressurized liquid extraction (PLE)
141 A commercial ASE 200 device (11 mL stainless steel cells) was used for PLE process in two
142 steps. For each extraction, ‘sugar MSK’ samples and sea sand were mixed in a 1:2 w/w
143 proportion. The mixture was extracted on static mode at 100 bar. After the extraction, the
144 solvent was removed by evaporation with continuous stream of gaseous nitrogen. Extraction
145 yield was expressed as g of extract/100 g dry weight basis of sample (mean of duplicate).
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147 2.3.1. PLE- first step evaluation
148 Due to ‘sugar MSK’ fat content, a first defatting step was required in order to recover the fat
149 while cleaning the sample for polyphenolics’ extraction. Three “alternative and usable”
150 solvents were tested to avoid the use of n-hexane: n-heptane, cyclohexane and (+)-limonene.
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151 n-Hexane was used as reference nonpolar solvent. In order to achieve the maximum defatting
152 of ‘sugar MSK’, kinetics extraction curves for each nonpolar solvent were studied at 100 °C
153 and 100 bar for 90 min.
154
155 2.3.2. PLE-second step optimization
156 The polyphenolic compounds recovery, including mangiferin, from ‘sugar MSK’ after the
157 defatting process was optimized using a three-level face-centered central composite design
158 (CCD). The effect of temperature (50-150 °C) and green solvent composition (according to
159 HSP results) were investigated on mangiferin content, extraction yield, total phenolic content,
160 total flavonoid content and antioxidant activity. Experimental data was fitted with the following
161 second order polynomial equation: