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Contents lists available at ScienceDirect LWT - Food Science and Technology journal homepage: www.elsevier.com/locate/lwt Isolation, purification, identification, and stability of anthocyanins from Lycium ruthenicum Murr Pei Liua, Wanrong Lia, Zhongze Hua, Xinguang Qina,∗∗, Gang Liua,b,c,∗ aWuhan Polytechnic University, College of Food Science and Engineering, Wuhan, China b Key Laboratory for Deep Processing of Major Grain and Oil (Wuhan Polytechnic University), Ministry of Education, China cHubei Key Laboratory for Processing and Transformation of Agricultural Products (Wuhan Polytechnic University), Wuhan, China A R T I C L E I N F O Keywords: Lycium ruthenicum Murr Anthocyanins Response surface methodology HPLC-MS2 A B S T R A C T Response surface methodology was used to investigate the ultrasonic-assisted extraction of anthocyanins from Lycium ruthenicum Murr. A Box-Behnken design of three-level-three-factor was used to optimize extractive fac- tors, including ethanol concentration (A), ultrasonic extraction time (B), and liquid-solid ratio (C) and to achieve high extraction yield of the anthocyanins. The three parameters were optimized at 70% (v/v), 28min, 33: 1 (mL/ g), respectively, the best extraction yield of anthocyanins was 7.12 ± 0.093%. The AB-8 resin was further to be chosen for purification the anthocyanins. Anthocyanin composition was analyzed by HPLC-MS2, the possible structures can be speculated as petunidin-3-O-(glucosyl-p-coumaroyl)-rutinoside-5-O-glucoside, pentuidin-3-O- (caffeoyl)-rutinoside-5-O-glucoside, delphinidin-3-O-(p-coumaroyl)-rutinoside-5-O-glucoside, petunidin-3-O-(p- coumaroyl)-rutinoside-5-O-glucoside, malvidin-3-O-(p-coumaroyl)-rutinoside-5-O-glucoside, cyanidin-3-O-ruti- noside, and petunidin-3-O-(p-coumaroyl)-rutinoside. The thermal stability indicated the high purity of antho- cyanins, and purified anthocyanins combined with whey protein isolate (WPI) can enhance the thermal stability of anthocyanins. The thermal stability of the purified anthocyanins was higher than that of the unpurified anthocyanins; whereas the thermal stability of the purified anthocyanin-WPI synthesis was greater than that of the purified anthocyanins. The thermal stable anthocyanins and anthocyanin-protein synthesis has the potential application in the functional food industry. 1. Introduction Lycium ruthenicum Murr is a unique species of Lycium that belongs to the family of Solanaceae and is a functional food mainly distributed in Xinjiang, Ningxia, Tibet, and Qinghai China (Chen et al., 2018; Liu et al., 2019a). The fruits of L. ruthenicum Murr are nearly spherical, bluish violet in color when ripe, and rich in a variety of amino acids and vitamins and anthocyanins. Hence, their health value is extremely high. Anthocyanins extracted from L. ruthenicum Murr exhibit great stability, strong coloring power, and no toxic side effects and can be used in medicine, food industry, and light textile industry. L. ruthenicum Murr is abundant in anthocyanins, which hence attracted great attention be- cause of their potential therapeutic benefit (Wang et al., 2018a; Zheng et al., 2011). This research aims to explore the good extraction condi- tion of anthocyanins from L. ruthenicum Murr and identify the main components of anthocyanins. Anthocyanins are a class of flavonoids abundantly found in plant cell fluids and are widely distributed in nature, safe, and not noxious. These substances have strong antioxidant activities, mainly for anti- inflammatory, cardiovascular protection, and anti-tumor (Heinonen et al., 2016; Keppler & Humpf, 2005; Moldovan, David, Chisbora, & Cimpoiu, 2012). With the improvement of food safety requirements and the development of biology and medicine, natural pigments have gra- dually replaced artificial synthetic pigments in the development of food coloring industry (Zhao et al., 2017). Anthocyanins aid in the stabili- zation of foodstuffs and increase food shelf life because of their anti- oxidation properties and antimicrobial potential (Silva, Costa, Calhau, Morais, & Pintado, 2017). These natural water-soluble pigments (Yang, Yuan, Xu, & Yu, 2015) belong to polyphenols (Zheng et al., 2011). Anthocyanins are usually obtained from flowers, fruits, and vegetables through conventional solid-liquid extraction, ultrasound-assisted ex- traction (Romero-Diez et al., 2019), enzymatic assisted extraction (Silva https://doi.org/10.1016/j.lwt.2020.109334 Received 25 October 2019; Received in revised form 23 March 2020; Accepted 24 March 2020 ∗ Corresponding author. College of Food Science and Engineering, Wuhan Polytechnic University, No. 68 Xue Fu South Road, Changqing Garden, 430023, Wuhan, China. ∗∗ Corresponding author., E-mail addresses: 76516589@qq.com (X. Qin), lg820823@163.com (G. Liu). LWT - Food Science and Technology 126 (2020) 109334 Available online 27 March 2020 0023-6438/ © 2020 Elsevier Ltd. All rights reserved. T http://www.sciencedirect.com/science/journal/00236438 https://www.elsevier.com/locate/lwt https://doi.org/10.1016/j.lwt.2020.109334 https://doi.org/10.1016/j.lwt.2020.109334 mailto:76516589@qq.com mailto:lg820823@163.com https://doi.org/10.1016/j.lwt.2020.109334 http://crossmark.crossref.org/dialog/?doi=10.1016/j.lwt.2020.109334&domain=pdf et al., 2017), and High Pressure Pulse Electric assisted extraction (Chen et al., 2018; Heinonen et al., 2016). Ultrasonic-assisted extraction is convenient and highly efficient because of the presence of cavitation bubbles during mass transfers. The use of aqueous ethanol can also increase the diffusion of compounds. Therefore, this work studied the ultrasonic-assisted extraction time and the concentration of aqueous ethanol. Response surface methodology (RSM) (Iyyappan, Bharathiraja, Baskar, & Kamalanaban, 2019; Liu, Wei, & Liao, 2013) and orthogonal test analysis (Li, Pan, Cui, & Duan, 2010) are used to optimize the conditions after completion of the single factor test. RSM has ad- vantages of achieving good extraction within few experiments and is a widely used experimental optimization method. However, the use of RSM to optimize ultrasound-assisted extraction and increase the ex- traction rate of anthocyanins in L. ruthenicum Murr has been rarely reported. Anthocyanins have potential applications in foods; however, their thermal stability remains a problem. Numerous studies combined pro- teins with biologically active ingredients to increase the stability of anthocyanins while allowing proteins to be loaded with natural active ingredients. However, few studies focused on the difference in the thermal stability of anthocyanins and anthocyanins–protein synthesis. Whey protein isolate (WPI) is a by-product in the cheese industry that has received attention because it contains all essential amino acids and has great functional properties (Liu et al., 2019b). Therefore, the combination of anthocyanins and WPI for thermal stability can serve as a basis for the experimental application of anthocyanins in foods. This study aims to: i) obtain optimum extraction conditions for anthocyanins using Box-Behnken design (BBD) that is one mode of RSM to explore different independent variables, consisting of ethanol con- centration (A), extraction time (B), liquid-solid ratio (C), and their in- teractions; ii) investigate the composition using high performance li- quid chromatography coupled with a diode array detector (HPLC-DAD) and high performance liquid chromatography equipped with a QE-Plus hybrid quadrupole orbitrap mass spectrometry (HPLC-MS2); and iii) evaluate the thermal stability of anthocyanins and anthocyanin-WPI. 2. Materials and methods 2.1. Samples, chemicals, and standard The L. ruthenicumMurr were bought in Xinjiang, China and stored in the laboratory at room temperature. The AB-8 macroporous resin was purchase from Tianjin Guangfu Fine Chemical Research Institute, China. Formic acid (Sinopharm Chemical Reagent Company Limited, China) and acetonitrile (Fisher Chemical Company Limited, USA) of chromatographic grade were used for HPLC analysis. Cyanidin-3-glucoside (94% purity) was purchased from Shanghai Yuanye Bio-technology Company Limited, China. Whey protein isolate (product 9020) was provided by Hilmar Ingredients, USA. And other chemicals were analytical reagent. Ultra-pure water was produced using Milli-Q system (Millipore Lab equipment Company Limited, USA). 2.2. Extraction of anthocyanins Anthocyanins of L. ruthenicum Murr were extracted by ultrasonic- assisted treatment using an ultrasonic generator (300 W, 45 kHz, SB- 5200DTS, Ningbo Scientz Biotechnology Company Limited, China). The dry L. ruthenicum Murr was powdered with a pulverizer (XL-10 B, Guangzhou Xulang Equipment Company Limited, China), subsequently make it across the 80 mesh sifter. The powder was degreased with petroleum benzin, and the L. ruthenicum Murr sample was stored at a low temperature. The powder (0.2 g) was placed in a beaker and used for each case. Three factors were selected based on the article written by Liu et al. (2013) Putting the powder in an ultrasonic generator and extracting anthocyanins at different ethanol concentrations, ultrasonic extraction times, and in individual liquid-solid ratio. 2.3. Measurement of anthocyanin yield The absorbance values of the anthocyanins were measured wave- length at 525 nm using multifunction microplate spectrophotometer (SpectraMax M2e, Molecular Devices, USA). The extraction yield of anthocyanin (using cyanidin-3-glucoside as the equivalents) (%) was calculated using = + × × ×TA A V n m[( 0.15) ]/(30.38 ),525 (1) where TA is the total anthocyanin extraction yield expressed as cya- nidin-3-glicoside equivalents (mg/g), A525 represents the absorbance at 525 nm, V means the volume of solvent (mL), n means the dilution factor, and m represents the weight of the raw material (g). 2.4. Optimization using Box-Behnken design The following test schemes and results were obtained by RSM. Based upon the preliminary results of single factor test, a Box-Behnken design of three-factor-three-level was employed to identify the great condition of the variables for anthocyanins. The following three in- dependent factors were considered: ethanol concentration (A), extrac- tion time (B), and liquid-solid ratio (C), and the level and code of in- dependent factors are displayed in Table 1. The experimental plan of extraction yield (Y) of anthocyanins is shown in Table 2. 2.5. Purification procedure by AK-8 macroporous resins Guided by the dynamic adsorption and desorption reported by Zheng et al. (2015), we slowly added 200 mL extract of anthocyanins to a pretreatment AB-8 macroporous resin column (400 mL) with a flow rate of 3–4 BV/h. The column that has absorbed anthocyanins was washed with ultrapure water at a flow rate of 3–4 BV/h to remove proteins, sugars, and polar compounds. Then, 70% (v/v) ethanol of pH 3 was used to elute at a flow rate of 1–2 BV/h to obtain an anthocyanin- rich solution. The solution was collected, used the technique of vacuum freeze-drying, and stored the purified anthocyanins at 4 °C. 2.6. The analysis of anthocyanins by HPLC-DAD The purified anthocyanins were resolved using HPLC-DAD (SSI Series 1500, Science System Incorporated, USA) equipped with Lichrospher RP-C18 column (250 mm × 4.6 mm, 5 μm particle size; Merck & Company Incorporated, Germany). The temperature of column maintained at 30 °C, injection amount was 20 μl, wavelength was set to 525 nm, and total flow rate of 0.7 mL/min. The solvent A contained water/formic acid (9:1, v/v), and the solvent B contained water/acet- onitrile/acetonitrile (6:3:1, v/v/v). Gradient elution: 10–25% B (0–10 min); 25–30% B (10–15 min); 30–90% B (15–30 min); 90% B (30–32 min); 90–30% B (32–35 min). 2.7. Identification of anthocyanins by HPLC-MS2 A Thermo U3000 high-performance liquid chromatography Table 1 Independent variables and their levels for Box-Behnken design. Independent variables Levels −1 0 1 Ethanol concentration (A) (%, v/v) 70 75 80 Extraction time (B) (min) 20 30 40 Liquid-solid ratio (C) (mL/g) 20:1 30:1 40:1 P. Liu, et al. LWT - Food Science and Technology 126 (2020) 109334 2 equipment equipped with a QE-plus hybrid quadrupole orbitrap mass spectrometer (Thermo Fisher Scientific Incorporated, USA) and a ACQUITY HSS T3 column (100 mm × 2.1 mm, 1.8 μm particle size; Waters Corporation, USA) was used to identify the anthocyanin ex- tracted from L. ruthenicum Murr. The temperature of column main- tained at 30 °C, injection amount was set to 20 μl, and wavelength was set to 525 nm. Electrospray ionization was set to positive mode, the scan range of 80 and 1200 m/z. Nitrogen served as drying and neb- ulizing gas. The flow velocity of dry gas was 20.0 l/min, the tempera- ture of dry gas was 270 °C, and capillary voltage was 26 V. The solvent A contained water/formic acid (9:1, v/v), and the solvent B contained water/acetonitrile/acetonitrile (6:3:1, v/v/v). Gradient elution: 10–25% B (0–10 min); 25–30% B (10–15 min); 30–90% B (15–30 min); 90% B (30–32 min); 90–30% B (32–35 min). 2.8. Thermal stability studies The effect of temperature on anthocyanins was determined fol- lowing the method obtained from Swer and Chauhan (2019) and Chen et al. (2018) with minimal modifications. Combining proteins and an- thocyanins can improve the stability of some biologically active sub- stances (Liu et al., 2019b, 2020; Wang et al., 2019). This experiment aimed to explore this phenomenon. Unpurified and purified anthocya- nins were dissolved in WPI solutions (1:1, v/v). The mixed solution was stirred for 12 h at room temperature for further tests. Unpurified and purified anthocyanins-WPI samples were used for thermal stability tests. The unpurified and purified anthocyanins-WPI synthesis, un- purified and purified anthocyanins solution were individually subjected to heat treatment in water bath at 80 °C for 0, 30, 60, 90, 120, 180, 240, and 300 min to test their thermal stability and were then rapidly cooled down to room temperature. The same solvent was used as a blank. The absorbance of anthocyanins was plotted on a vertical axis, and the heating time was plotted on the horizontal axis to map the anthocya- nins thermal stability curve (Jiang et al., 2019; Wu, Yang, & Chiang, 2018). 2.9. Statistical analysis All data of this study were obtained in three times, and the results were reported as average ± standard deviation of replicates. The data was analyzed for Analysis of Variance (ANOVA). The regression ana- lysis was carried out using Design Expert software version 8.0.6. 3. Results and discussion 3.1. The standard curve of anthocyanins The different concentration of reference substance (using cyanindin- 3-glucosideas) as abscissa, the absorbance values which were measured wavelength at 525 nm as vertical axis, and then drawing the standard curve. The standard curve was shown in Fig. 1. 3.2. Influence of ethanol concentration on the extraction yield of anthocyanins The extraction was conducted at diverse ethanol concentrations of 65%, 70%, 75%, 80%, and 85% (v/v). The other arguments were set as extraction time of 30 min, and the liquid-solid ratio of 40:1 (mL/g). Fig. 2a shows that the extraction yield of anthocyanins was affected by ethanol concentration. As the ethanol concentration increased, the growth of the extraction yield was slow, reached a peak at 75% (v/v), and then decreased with the increase in ethanol concentration. Ethanol concentration of 75% was used to extract anthocyanins in L. ruthenicum Murr because it is the most suitable according to the theory that the solvent polarity and the solubility of extract is related (Liu et al., 2013). These results may be connected to the concentration of ethanol and the dissolvability of anthocyanins in L. ruthenicum Murr. Thus, an ethanol concentration of 75% was found to be favorable for anthocyanin ex- traction. 3.3. Influence of extraction time on the extraction yield of anthocyanins The extraction times was set to 10, 20, 30, 40, and 50 min. The other arguments were set to ethanol concentration of 75% (v/v), and liquid-solid ratio of 40:1 (mL/g). The extraction yield of anthocyanins was affected by extraction time as displayed in Fig. 2b. The value firstly increased as a function of extraction time, reached the highest at 30 min, and then decreased with prolonged extraction time. This phe- nomenon is probably caused by the extended time for ultrasonic-as- sisted extraction and the increase in the temperature of the reaction system, which leads to the destruction and decomposition of antho- cyanins (Liu et al., 2013). Therefore, 30 min was found to be favorable for anthocyanin extraction. 3.4. Influence of the liquid-solid ratio on the extraction yield of anthocyanins The extraction was conducted at an aqueous ethanol to raw material ratio of 20:1, 30:1, 40:1, 50:1, and 60:1 (mL/g). The other arguments were fixed at the ethanol concentration of 75% (v/v), the extraction time of 30 min. The extraction yield affected by the liquid–solid ratio is displayed in Fig. 2c. When the liquid-solid ratio increased, the Table 2 Box-Behnken design for independent variables and their extraction yield. Run A(ethanol concentration, %) B (extraction time, min) C (liquid- solid ratio, mL/g) Y (Extraction yield, %) 1 −1 0 1 6.4110 2 0 0 0 6.8590 3 1 −1 0 5.1625 4 0 0 0 6.9358 5 1 1 0 5.2520 6 −1 −1 0 3.6595 7 0 1 −1 5.6335 8 1 0 −1 5.2425 9 0 −1 −1 4.5840 10 0 0 0 7.3405 11 −1 1 0 6.9035 12 −1 0 −1 5.5515 13 0 0 0 6.9620 14 0 1 1 6.8425 15 0 −1 1 4.1450 16 1 0 1 6.1670 17 0 0 0 6.9390 Fig. 1. The standard curve of cyanidin-3-glucoside. P. Liu, et al. LWT - Food Science and Technology 126 (2020) 109334 3 extraction yield of anthocyanins accomplished a highest at 30:1 (mL/g). Lower liquid–solid ultrasonic energy density in the extraction solutions showed predominance and a passive effect on the extraction yield. A similar tendency for this parameter was also observed during poly- saccharide extraction from Euryale ferox seed shells (Liu et al., 2013; Wang et al., 2018b). Therefore, the aqueous ethanol to raw material ratio of 30:1 (mL/g) is appropriate for anthocyanin extraction. 3.5. Optimization of the extraction conditions for anthocyanins The experimental plans and data of 17 runs embracing five center points per block was displayed in Table 2. On the base of multiple re- gression analysis, the regression equation would be obtained: Y = 7.00–0.24A-0.39B + 0.85C + 0.17AB+0.059AC+0.14BC- 0.049A2 -1.07B2-1.18C2 (2) Using Design-Expert 8.0.6 software analyzed the data in Table 2, and the ANOVA results are displayed in Table 3. The significance of each parameter was also determined by adopting p-value and F-value. Low p-value and high F-value indicated that the relevant factors are greatly significant. If the p-value is below 0.01, then the model is sig- nificant and can promote the extraction factors (Iyyappan et al., 2019). The relationship among the above regression equation description and the response surface value was significant (p = 0.0005 < 0.05), but the lack of fit was not significant (p = 0.0595 > 0.05). R2 = 0.9589 indicated that the model was well fitted with the experimental data and thus is a suitable mathematical design for the extraction yield of an- thocyanins. Hence, regression equation can be adopted to determine the optimal extraction of anthocyanins from L. ruthenicum Murr. Two independent factors (B, C) and two quadratic terms (B2, C2) influenced the extraction yield and were significant within 95% con- fidence interval according to the following ANOVA: p-valueA = 0.0843, p-valueB = 0.0149, and p-valueC = 0.002. The sequence of the influ- ence of each element on anthocyanin yield is as follows: liquid–solid ratio > extraction time > ethanol concentration. Other factors were not significant probably because those that were selected were un- suitable. The response surface analysis diagram visually shows the in- teraction between various elements in the extraction process and ex- amines the effect of the interaction of the other two elements on the extraction rate when two factors are fixed at the central value (Liu et al., 2013). The figure of 3D response surface and the figure of 2D contour plots were plotted according to the regression equation. The interaction of some factors is shown in Fig. 3. The 3D response surface can visually reveal the influence of the interaction of all kinds of factors on anthocyanin yield. A steep 3D response surface indicates the great influence of this element on the extraction yield, and the interaction of the two factors is highly significant. In the 2D contour, an oval contour reveals that the interaction between the two factors is significant, and the circular contours indicate that the interaction is insignificant. Fig. 3e and f shows that the liquid–solid ratio exhibits the greatest in- fluence on extraction yield, and extraction time is only within seconds. The regression analysis results in Table 3 are also consistent with the above phenomenon that the p-value of the liquid-solid ratio and ex- traction time are both less than 0.05 (significant). Under the selected optimum conditions, the model equation which Fig. 2. Effect of different extraction variables on extraction yield: (a) ethanol concentration; (b) extraction time; (c) liquid-solid ratio. Table 3 Analysis of variance for fitted quadratic model of extraction of phenolic compounds. Source Sum of squares df Mean square F-value p-value (Prob > F) Model 19.01 9 2.12 18.15 0.0005 Significant A 0.48 1 0.48 4.07 0.0834 B 1.20 1 1.20 10.31 0.0149 C 5.78 1 5.78 49.41 0.0002 AB 0.12 1 0.12 1.02 0.3453 AC 0.014 1 0.014 0.12 0.7396 BC 0.081 1 0.081 0.69 0.4340 A2 0.009988 1 0.009988 0.085 0.7785 B2 4.85 1 4.85 41.52 0.0004 C2 5.85 1 5.85 50.07 0.0002 Residual 0.82 7 0.12 Lack of fit 0.67 3 0.22 5.91 0.0595 Not significant Pure error 0.15 4 0.038 Cor Total 19.92 16 R2 = 0.9589; R2adj = 0.9061; R2pred = 0.4519; C·V.% = 5.78; Adequate precisior = 13.852. P. Liu, et al. LWT - Food Science and Technology 126 (2020) 109334 4 was suitable for forecasting the optimum response values was affirmed. The most suitable experimental conditions are as below: ethanol con- centration (A), 70.00%; extraction time (B), 27.60 min; and liquid-solid ratio (C), 33.21:1 (mL/g), and the forecasted extraction yield was 7.39%. But taking into consideration the maneuverability in practical manufacture, the suitable parameters were revised as below: ethanol concentration (A), 70%; extraction time (B), 28 min; and liquid-solid ratio (C), 33:1 (mL/g). The experimental extraction yield was 7.12 ± 0.093%, which agree with the forecasted extraction yield and indicates that the model of RSM is content and precise. 3.6. Comparison of the anthocyanins content from L. ruthenicum Murr after purification The total anthocyanin extraction yield of the unpurified anthocya- nins and purified anthocyanins can be calculated from Formula (1). Cyanidin-3-glucoside (94% purity) was used as standard. According to the total anthocyanin extraction yield and purify of standard, the purity of the unpurified anthocyanins was 52.10%, and that of purified an- thocyanins was increased to 77.62% after purification by AB-8 mac- roporous resins. Fig. 3. 3D response surface plots showing interactions between (a) ethanol concentration and extraction time, (c) ethanol concentration and liquid-solid ratio, (e) extraction time and liquid-solid ratio, contour plots showing interactions between (b) ethanol concentration and extraction time, (d) ethanol concentration and liquid-solid ratio, (f) extraction time and liquid-solid ratio. P. Liu, et al. LWT - Food Science and Technology 126 (2020) 109334 5 3.7. Identification of anthocyanins from L. ruthenicum Murr The chromatographic profile of anthocyanins from L. ruthenicum Murr at 525 nm obtained using HPLC-DAD is displayed (Zheng et al., 2011) in Fig. 4. In this HPLC-DAD analysis, seven peaks were visible, and the gradient procedure was used to obtain the maximal separation. The individual anthocyanins were identified mostly by elution order, retention time, and compared the data of MS spectra according to previously reported (Wang et al., 2018a). The chromatograph obtained using HPLC-MS2 was used to de- termine the compositions of anthocyanins from L. ruthenicum Murr (Grajeda-Iglesias, Salas, Barouh, Barea, & Figueroa-Espinoza, 2017). The identification process was built by comparing the mass of mole- cular ions and fragment ions with the results that had been reported (Chen et al., 2018; Kim, Kim, Lee, Jang, & Kim, 2017; Sang et al., 2018; Wang et al., 2018a; Wu & Ronald, 2005; Zheng et al., 2011) in litera- ture. The HPLC-DAD chromatogram at 525 nm was displayed in Fig. 4, and the data obtained using the molecular ion, fragment ion, and re- tention time of the anthocyanin peaks in HPLC-MS2 analysis were shown in Table 4. The fragments determined using HPLC-MS2 revealed that only four aglycones, including cyanidin (m/z 287), delphinidin (m/z 303), pet- unidin (m/z 317), and malvidin (m/z 331) were found in L. ruthenicum Murr. The structures of individual anthocyanins from L. ruthenicum Murr were identified based on the mass fragmentation patterns of ru- tinoside (m/z 308), glucoside (m/z 162), p-coumaric acid (m/z 164), and caffeic acid (m/z 180). These anthocyanins possessed a basic structure of 3-rutinoside or 3-O-rutinoside-5-O-glucoside. The specific MS data of predicted anthocyanins are summarized in Table 4, and the mass spectrums are shown in Fig. 5. 3.8. Protection effect of WPI on the thermal stability of anthocyanins from L. ruthenicum Murr Anthocyanin and protein interact through noncovalent bonds, which mostly contain hydrogen bonds, hydrophobic interactions, and van der Waals forces (Liu et al., 2019b). Therefore protein often be used to load anthocyanins, and usually anthocyanins-protein synthesis ap- plied to food industry. Thermal sterilization is a common treatment in the food industry, and thermal stability of substance is important. Fig. 6 shows that the thermal stability of the unpurified anthocyanins is in- ferior to that of the purified anthocyanins-WPI synthesis. The thermal stability of the synthesis and anthocyanins greatly differs before heating at 60 min. With prolonged heating time of 60–120 min, the thermal stability increases, but the thermal stability curve is relatively flat. This phenomenon indicates that the thermal stability of anthocyanins is stable during this period. When heated for 120–300 min, the antho- cyanins show a steep thermal stability curve, whereas that of the an- thocyanin-WPI synthesis has improved. The thermal stability curve of the unpurified anthocyanin-WPI synthesis decreases sharply within 0–60 min, and the thermal stability of the unpurified anthocyanins is slower than that of the unpurified anthocyanins-WPI synthesis. The purified anthocyanins and antho- cyanin-WPI synthesis exhibit a similar stationary phase at 60–120 min, and the thermal stability of the unpurified anthocyanins is slower than that of the unpurified anthocyanins-WPI synthesis at 120–300 min. The results show that the thermal stability of the purified antho- cyanins is higher than that of the unpurified anthocyanins; whereas the thermal stability of the purified anthocyanin-WPI synthesis is greater than that of the purified anthocyanins. These facts indicate that high- purity anthocyanins can achieve a high degree of thermal stability, and the stability of purified anthocyanins-WPI is improved. The anthocya- nins-WPI synthesis and the improvement of their thermal stability are consistent with the previous research (Qin et al., 2018). Therefore, the present experiment can serve as a basis for the application for antho- cyanin-protein synthesis in the food industry. 4. Conclusions This article explores the L. ruthenicum Murr extract conditions for anthocyanins optimized by RSM. Comparing the results from RSM and single factor test can obtain an optimum extract condition. Purification of anthocyanins using AB-8 resin produced a purified anthocyanin with purity of 77.62%. Many kinds of anthocyanins are found in L. ruthe- nicum Murr by HPLC. The seven possible structures can be speculated through HPLC-MS2. The thermal stability indicated the high purity of anthocyanins, and purified anthocyanins combined with WPI can en- hance the thermal stability of anthocyanins. CRediT authorship contribution statement Pei Liu: Formal analysis, Writing - original draft. Wanrong Li: Methodology, Validation. Zhongze Hu: Supervision. Xinguang Qin: Conceptualization, Methodology, Validation. Gang Liu: Conceptualization, Writing - review & editing. Fig. 4. HPLC chromatograms at 525 nm of anthocyanins from L. ruthenicum Murr. Table 4 Anthocyanins identified in the extract of L. ruthenicum Murr. Peak No. RT (min) M+ (m/z) Fragment (m/z) Anthocyanin 1 22.933 1095 933, 479, 317 Petunidin-3-O-(glucosyl-p-coumaroyl)-rutinoside-5-O-glucoside 2 23.383 949 787, 479, 317 Pentuidin-3-O-(caffeoyl)-rutinoside-5-O-glucoside 3 24.410 919 757, 465, 303 Delphinidin-3-O-(p-coumaroyl)-rutinoside-5-O-glucoside 4 25.128 933 771, 479, 317 Petunidin-3-O-(p-coumaroyl)- rutinoside-5-O-glucoside 5 26.158 947 785, 493, 331 Malvidin-3-O-(p-coumaroyl)-rutinoside-5-O-glucoside 6 26.675 595 287 Cyanidin-3-O-rutinoside 7 28.243 771 317 Petunidin-3-O-(p-coumaroyl)-rutinoside P. Liu, et al. LWT - Food Science and Technology 126 (2020) 109334 6 Fig. 5. MS spectra of anthocyanins in L. ruthenicum Murr. The number of each spectrum corresponds to the peak number in Table 4 and Fig. 4. P. Liu, et al. LWT - Food Science and Technology 126 (2020) 109334 7 Fig. 5. (continued) P. Liu, et al. LWT - Food Science and Technology 126 (2020) 109334 8 Declaration of competing interest The authors declare that there are no conflicts of interest. Acknowledgment This research received funding from the Chinese National Natural Science Foundation of China[grant number 31771925]. Also, it was supported by the Research and Innovation Initiatives of Wuhan Polytechnic University [grant number 2020J01]. References Chen, S., Zeng, Z., Hu, N., Bai, B., Wang, H., & Suo, Y. (2018). Simultaneous optimization of the ultrasound-assisted extraction for phenolic compounds content and antioxidant activity of Lycium ruthenicum Murr. fruit using response surface methodology. Food Chemistry, 242, 1–8. 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anthocyanin yield Optimization using Box-Behnken design Purification procedure by AK-8 macroporous resins The analysis of anthocyanins by HPLC-DAD Identification of anthocyanins by HPLC-MS2 Thermal stability studies Statistical analysis Results and discussion The standard curve of anthocyanins Influence of ethanol concentration on the extraction yield of anthocyanins Influence of extraction time on the extraction yield of anthocyanins Influence of the liquid-solid ratio on the extraction yield of anthocyanins Optimization of the extraction conditions for anthocyanins Comparison of the anthocyanins content from L. ruthenicum Murr after purification Identification of anthocyanins from L. ruthenicum Murr Protection effect of WPI on the thermal stability of anthocyanins from L. ruthenicum Murr Conclusions CRediT authorship contribution statement Declaration of competing interest Acknowledgment References
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