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Integrated utilization of red radish for the efficient production of high purity of procyanidin dimers wen jiang, Xiaohua Zhou, Yang Yang, and Zhiming Zhou J. Agric. Food Chem., Just Accepted Manuscript • DOI: 10.1021/acs.jafc.8b02478 • Publication Date (Web): 03 Jul 2018 Downloaded from http://pubs.acs.org on July 7, 2018
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Journal of Agricultural and Food Chemistry
Integrated utilization of red radish for the efficient production of high purity of procyanidin dimers Wen Jiang, Xiaohua Zhou*, Yang Yang, Zhiming Zhou Department of Chemical Engineering, School of Chemistry and Chemical Engineering, Chongqing University, Chongqing 401331, PR China
*Corresponding author Xiaohua Zhou Tel: +86-65678925 Fax: (86) 23-65678925 E-mail:
[email protected] 1
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ABSTRACT
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Red radish was extracted by methanol to obtain crude radish procyanidin extracts.
3
The purity of procyanidin (PP) and procyanidin dimers (PD) of crude radish
4
procyanidin extracts under different ratio of methanol to radish was optimized to
5
achieve the best extraction performance. Then the crude radish procyanidin extracts
6
was respectively processed six macroporous resins separation to separate radish
7
procyanidin oligomers (RPO) and polymers (RPP). Depolymerization of radish
8
procyanidin polymers (RPP) into oligomers was then conducted. N-acetylneuraminate
9
lyase (NAL) was firstly used as the enzyme to depolymerize RPP. The
10
depolymerization yield (DY) under different depolymerized conditions was also
11
investigated. Results showed the DY of RPP would achieve 53.24 ±0.35% at the best
12
condition. Then high purity of procyanidin dimers was prepared by depolymerized
13
procyanidin oligomers and PRO. Additionally, the chemical structure of the
14
preparative radish procyanidin dimers was elucidated by high resolution mass
15
spectrum, one- and two-dimensional NMR.
16
Keywords : Procyanidin oligomers; Procyanidin polymers; Depolymerization;
17
N-acetylneuraminate lyase; Procyanidin dimers
18 19 20 21
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INTRODUCTION
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Red radish (Raphanus sativus L.) is an important vegetable crop belonging to the
24
Cruciferae (or Brassicaceae) family which is widely distributed in China, especially in
25
Chongqing Municipality. Radish is regarded as high medicinal and nutritional value
26
and recommended as an alternative treatment for various ailment soloplaint because
27
of the existence of various phytochemicals, especially polyphenols and flavonoids1-5.
28
However, radish is only widely underutilized as raw materials of Sichuan pickles and
29
its current applications are limited. Thus, it is desirable to take advantage of the
30
phytochemicals, especially polyphenols, of radish to expand its applications. It was
31
reported that procyanidins, oligomers and polymers of polyhydroxyflavan-3ol units,
32
are a class of polyphenols which accounted for 68% of the total phenols content in
33
radish6. Degree of polymerization (DP) was used to describe the size of
34
procyanidins7,8. Procyanidins with DP of 1–4 are oligomers, while procyanidins with
35
DP≥5 are polymers. Procyanidin oligomers were known to prevent cancers,
36
cardiovascular diseases, and other aging related conditions
37
intimate knowledge of the bioavailability of pure procyanidin oligomers is still
38
exiguous as studies have only used complex procyanidin mixtures due to a lack of
39
appropriate reference compounds12-15. Only a few procyanidin oligomers are
40
commercially available, such as procyanidin dimers which is the simplest procyanidin
41
oligomers16. Furthermore, procyanidin dimers were reported to have high biological
42
activities17. Consequently, it is of interest to prepare pure procyanidin dimers from red
43
radish. 3
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9-11
. But until now,
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However, the majority of procyanidins in nature including those in red radish are
45
polymers18 and a great deal of procyanidin polymers are left after the preparation of
46
procyanidins dimer. Procyanidin oligomers are absorbable in vivo whereas polymers
47
could not be absorbed in the gastrointestinal tract19,20. Bioavailability of procyanidin
48
polymers was relatively lower than oligomers19.
49
Depolymerization of procyanidin polymers to oligomers is expected to enhance
50
their bioavailability and make for higher bioactivity in vivo21-24. Several strategies
51
have been used for the depolymerization of procyanidin polymers. Palm procyanidin
52
polymers were depolymerized by Foo and Porter with epicatechin in ethanol-acetic
53
acid at 95 oC for 22 h and some dimers were identified25. Sorghum procyanidin
54
polymers can also be depolymerized with epicatechin under acidic conditions at 74 oC
55
for 61 min and procyanidin monomers and oligomers were recognized26. Grape seeds
56
or hazelnut skins procyanidin polymers were depolymerized into dimers with reacted
57
with flavan-3-ols under acidic conditions27. Depolymerization under acidic condition
58
was convenient and the yield of oligomers is relatively high, but the cost of the
59
depolymerization was high with flavan-3-ols as reactant and the reaction apparatus
60
would also corrode under acidic conditions. Hydrogenolysis was also applied by Foo
61
to the depolymerization of photinia glabrescens procyanidin polymers and
62
procyanidin monomers and oligomers were obtained28. It was reported by Li et al.,
63
hi-tannin sorghum bran procyanidin polymers hydrogenolyzed with 1MPa hydrogen,
64
3 mg Pd/C, at 100 oC for 1-3 h to reach the maximum oligomers yield of 38.3%29.
65
However, hydrogenolysis requires high strength equipment and the yield of oligomers 4
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is also low.
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Meanwhile, an increasing number of attentions were drawn on enzymatic method
68
owning to its low cost and high yield. N-acetylneuraminate lyase (NAL, EC 4.1.3.3),
69
a (β/α)8-barrel protein, belongs to the dihydrodipicolinate synthase (DHDPS, EC
70
4.2.1.52) family of enzymes30. Like the much more closely studied DHDPS, NAL is a
71
homotetrameric enzyme, plays an unconnected metabolic role, catalyzing the ultimate
72
step in the biosynthesis of sialic acid—the condensation of pyruvate and
73
N-acetylmannosamine. Sialic acids, a large family of sugars, derived from the parent
74
compound N-acetylneuraminic acid31. N-acetylneuraminic acid is widely acted on the
75
surface of cells of animals, where they play important parts in a series of critical
76
biological processes, including cellular adhesion and recognition32.
77
The degradation mechanism of N-acetylneuraminic acid and procyanidin polymers
78
were shown in Figure 1. As shown in Figure 1a, the enzymatic degradation reaction
79
of N-acetylneuraminic acid by N-acetylneuraminate lyase (NAL) occurred on the C-C
80
bond of pyran ring of N-acetylneuraminic acid. And the structure of procyanidin
81
polymers was also shown in Figure 1b. The degradation site of procyanidin polymers
82
also occurred on the C-C bond of pyran ring “C” of procyanidin polymers. By
83
comparison the degradation of N-acetylneuraminic acid and procyanidin polymers,
84
the enzymatic catalytic reactions of N-acetylneuraminic acid by NAL occurred on the
85
C-C bond of pyran ring which was similar to the depolymerization of procyanidin
86
polymers. Herein, NAL is firstly used as the enzyme catalysts in the depolymerization
87
of procyanidin polymers. 5
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In this paper, red radish was firstly processed with the cleavage of radish
89
procyanidin polymers and oligomers. The radish procyanidin polymers were
90
depolymerized by NAL to yield oligomers which can be used to prepare high purity
91
of procyanidin dimers. The factors which affected the depolymerization yield were
92
investigated, including the pH, reaction temperature and the mass ratio of NAL to
93
RPP. Then the radish procyanidin oligomers were used to prepare high purity of
94
procyanidin dimers by preparative HPLC purification method. And the structure of
95
the preparative procyanidin dimers was elucidated by high resolution mass spectrum,
96
one- and two-dimensional NMR. This study presented a desirable process for efficient
97
production of high purity of procyanidin dimers from red radish.
98
MATERIAL AND METHODS
99
Reagents. Red radish (Raphanus sativus L.) was offered by Haiju Agriculture
100
Development Co. Ltd., Chongqing, China. N-acetylneuraminate lyase (35 U/mg) was
101
purchased from Xibao Biotechnology Co. Ltd., Shanghai, China. All the reagents
102
above were of biological grade. Amilan, D101, AB-8, ADS-17, NAK-7, ADS-7 and
103
XAD-4 macroporous resins were purchased from H&E Co., Ltd., Beijing, China.
104
(−)-Epicatechin was purchased from Sigma chemical CO. (St. Louis, MO), USA.
105
HPLC grade solvents were purchased from Fisher Scientific (Pittsburg, PA), China.
106
Formic acid and other chemicals were purchased from Head Chemical Factory,
107
Chongqing, China, and all of them were of analytical grade.
108
Separation of radish procyanidin oligomers (RPO) and polymers (RPP) from
109
red radish. Fresh red radish was cut into pieces (2 × 2 × 2 cm) and then extracted in a 6
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flask with methanol at 50 °C for 2 h, and the ratio of methanol to radish (v/w) was set
111
as 20: 1 to 55:1. The extracts were collected and then centrifuged at 5000 g-force for
112
10 min. Supernatants was then collected. Residual methanol in the supernatant was
113
removed on rotatory evaporation at 40 °C under vacuum by a circulating water
114
vacuum pump (SHZ-IIID, Zhixin, Shanghai, CN) to obtain the crude radish
115
procyanidin extracts. The crude radish procyanidin extracts was processed further
116
separation method, which used macroporous resins (amilan, D101, AB-8, ADS-17,
117
NAK-7 and ADS-7). The resins were required to pretreat before use and the method
118
used was as Zhang et al33 with some modification. After that, the pretreated resins
119
(10g) were dispersed in crude radish procyanidin extracts (100 mL). The mixture was
120
rocked at 60 g-force for adsorption under room temperature for 2 h. Then the resin
121
loaded radish procyanidin oligomers (RPO) were desorbed with 45% (v/v) methanol
122
solution under room temperature, and RPO eluent was collected until the eluent has
123
no color. After that, the resin loaded residual radish procyanidins were desorbed with
124
80% (v/v) methanol (containing 0.3% (v/v) formic acid) solution under room
125
temperature, and radish procyanidin polymers (RPP) eluent was collected until the
126
eluent has no color. The methanol of the eluent solutions was removed by a rotary
127
evaporator at 40 oC, and the concentrated solution was finally lyophilized by a freeze
128
drier (FD-1A-50, Tianling, Jiangsu, CN) to obtain RPO and RPP powder. RPP powder
129
could be depolymerized to low molecular weight of RPO which can provide raw
130
material for the preparation of high purity of radish procyanidins dimer.
131
Determination of the purity of procyanidins. The purity of procyanidins (PP) 7
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was measured using vanillin assay with (−)-epicatechin as standard34. The
133
absorbance of the reaction solution of vanillin and (−)-epicatechin at λ=500 nm
134
were measured by a UV spectrophotometer (UV-2600, Shimadzu, Japan) to drew
135
the standard curve. After that, the content and mass of procyanidins was measured
136
by the standard curve obtained above. And the PP was calculated as follows:
137
138
PP (%) =
M Pa M pb
× 100%
Where Mpa is the mass of procyanidins after separation (µg/mL), Mpb is the initial
139
mass of procyanidins before separation (µg/mL).
140
Depolymerization
141
N-acetylneuraminate lyase.
of
radish
procyanidin
polymers
(RPP)
by
142
Purification of N-acetylneuraminate lyase. 10 g of N-acetylneuraminate lyase
143
(NAL) was firstly poured into 1000 mL aqueous solution. Then the NAL solution was
144
purified using the purification method mentioned in the literature with some
145
modification35.
146
Depolymerization of radish procyanidin polymers by NAL. The radish
147
procyanidin polymers (RPP) powder (5 g) was poured into 100 mL distilled water to
148
prepare 50mg/mL RPP solution. 5% (w/w) NAL was then added into the above
149
solution and the reaction mixture was carried out at 50 oC, pH 8.0 for 4h under gentle
150
agitation. After the reaction finished, the pH of the solution was adjusted to 6.4 where
151
the isoelectric point of NAL to precipitate NAL. Then the solution was centrifuged for
152
10 min at the speed of 5000 g-force, and finally the depolymerization product was
153
obtained. 8
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Determination of the depolymerization yield of radish procyanidin polymers.
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The depolymerization yield (DY) of RPP means the content of procyanidin oligomers
156
after the depolymerization reaction by NAL. The HPLC-MS method was used to
157
verify the depolymerization of procyanidin polymers by NAL and measure the
158
content of procyanidin oligomers and polymers. The HPLC equipment was an Agilent
159
1200 HPLC system equipped with a high pressure pump and a UV diode array
160
detector. The analytical column was a Reverse Phase-C18 column (5 µm particle size,
161
250×4.6 mm) (HiQsil, Tokyo, Japan). The analytical HPLC analysis was performed
162
as follows: the solvent system consisted of ultra-pure water as fluid phase A and
163
methanol as fluid phase B. Gradient conditions: 0-5min, 20% B isocratic; 5-20min,
164
20-35% B linear; 20-40min, 35% B isocratic; 40-60 min, 35-55% linear; 60-80 min,
165
55% B isocratic. The eluates were detected at λ=280 nm under room temperature. The
166
flow rate was set 1.0 mL/min, and 10 µL aliquots were injected into the column. Then
167
(−)-epicatechin was used as the external standard to measure the content of
168
procyanidin oligomers in the samples according to a standard curve obtained from the
169
standard.
170
The negative electrospray ionization mode was performed using nebulizer 14 psi,
171
drying gas 11 L/min, drying temperature 355 oC, and capillary 4000 V. The full scan
172
mass spectra were measured from m/z 150 to 1500. The identification of procyanidin
173
monomers, dimers and trimers were based on mass spectra21,23,36. And the
174
depolymerization yield (DY) of RPP was determined by the following equation:
9
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Ca − Ci × 100% C0
175
DY =
176
Where Ca is the procyanidins monomer and oligomers content of depolymerization
177
product after reaction (µg/mL), Ci is the initial content of procyanidin oligomers in
178
RPP (µg/mL), C0 is the initial content of RPP (µg/mL).
179
Optimization of radish procyanidin polymers depolymerization. To achieve the
180
best depolymerization yield (DY), pH (4, 5, 6, 7, 8, 9), reaction temperature (30, 40,
181
50, 60, 70 oC) and the mass ratio of NAL to RPP (0.01, 0.03, 0.05, 0.07, 0.1) were
182
optimized.
183
Preparation of high purity of radish procyanidin dimers. Radish procyanidin
184
dimers, the simplest procyanidin oligomers in red radish, can be separated from radish
185
procyanidin oligomers (RPO). Hence, the crude radish procyanidin dimers could be
186
obtained by methanol extraction and macroporous resin adsorption. In order to
187
preparing high purity of radish procyanidin dimers, the preparative HPLC purification
188
method was used. The preparative HPLC equipment and column used agreed with the
189
equipment reported in the literature33. And the preparative HPLC separation was
190
performed as follows: the solvent system consisted of methanol as fluid phase A and
191
ultra-pure water as fluid phase B. Gradient conditions: 0-20 min, 20-35% A linear;
192
20-60min, 35% A isocratic. The flow rate was set 20 mL/ min and detected at λ=280
193
nm. The injection volume was 5 mL. The peak fraction of radish procyanidin dimers
194
was collected manually according to the chromatogram. After that, the residual
195
procyanidin oligomers were also prepared. The fraction was concentrated by a rotary
196
evaporator, and then processed using a vacuum freeze-drying machine (FD-1A-50, 10
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Tianling, Jiangsu, CN). The purity of radish procyanidin dimers was calculated using
198
the following equation.
Mda × 100% M db
199
PD(%) =
200
Where Mda is the mass of radish procyanidin dimers after purification which can be
201
calculated according to the mentioned in HPLC analysis of radish procyanidin dimers,
202
and Mdb is the initial mass of radish procyanidin dimers before purification.
203
HPLC analysis of preparative radish procyanidin dimers. The analytical HPLC
204
method was used to analysis the concentration of the preparative radish procyanidin
205
dimers. And the analytical HPLC equipment was a LC 3000 system (Chuangxin
206
Tongheng Science and Technology Co. Ltd, Beijing, China), which equipped with a
207
high pressure pump and a UV–visible diode array detector. The analytical column was
208
a reverse phase C18 column (5 µm particle size, 250×4.6 mm) (HiQsil, Tokyo,
209
Japan).
210
The analytical HPLC analysis was performed as follows: the solvent system
211
consisted of methanol as fluid phase A and ultra-pure water as fluid phase B. Gradient
212
conditions: 0-10min, 20% A isocratic; 10-35min, 20-35% A linear; 35-50min, 35% A
213
isocratic. The eluates were detected at 280 nm at 25 °C. The flow rate was set 1.0
214
mL/min, and the injected volume was 10 µL. Then the concentration of the
215
preparative radish procyanidin dimers could be calculated according to the regression
216
line of the preparative procyanidin dimers y = 3.21571E+07 x - 3.29715E+06 (R2 =
217
0.9981), where y is the peak area and x is the concentration of procyanidin dimers 11
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(µg/mL). The working calibration curve of procyanidin dimers standard solution
219
revealed good linear correlation over the range of 0.25–2.0 µg/mL.
220
Structural elucidation of preparative radish procyanidin dimers. The structural
221
elucidation of the preparative radish procyanidin dimers was identified by high
222
resolution mass spectrum, one- and two-dimensional NMR.
223
The high resolution mass spectrum was conducted using the method as reported by
224
Christensen et al37 with some modification. The full spectrum of per- fluorkerosene
225
was used for mass calibration across the range of the spectrum collected from m/z
226
100–700.
227
The one-dimensional 1H and 1
13
C NMR, two-dimensional
1
H-1H correlated
H-1H phase-sensitive nuclear Overhauser enhancement
228
spectroscopy (COSY),
229
spectroscopy (NOESY), heteronuclear single-quantum coherence (HSQC), and
230
heteronuclear multiple-bond correlation (HMBC) experiments were performed on a
231
Agilent NMR vnmrs600 at 240 K to overcome the atropisomerism which caused
232
signal broadening, using acetone-d6 as solvent, with tetramethylsilane (TMS) as the
233
internal standard.
234
RESULTS AND DISCUSSION
235
Separation of radish procyanidin oligomers and polymers from red radish.
236
Red radish was firstly extracted with methanol to extract crude procyanidins. The
237
ratio of methanol to radish (v/m) was studied to achieve the best extraction
238
performance. And the influence was revealed in Figure 2. It was indicated that the
239
extraction yield, purity of procyanidins (PP) and purity of procyanidin dimers (PD) 12
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increased rapidly when the ratio of methanol to radish was set to be between 20:1 and
241
40:1 (v/m), but then increased slowly over 40:1 (v/m). The extraction yield, PP and
242
PD at the ratio of methanol to radish of 40:1 (v/m) would achieve 91.4 ± 0.7%, 61.8 ±
243
1.2% and 22.5 ± 0.5%, respectively. Hence, 40:1 (v/m) was selected as the best ratio
244
of methanol to radish among tested and used for the further study.
245
After that, crude procyanidin extracts was further individually processed six
246
macroporous resins (amilan, D101, AB-8, ADS-17, NAK-7 and ADS-7) separation to
247
separate procyanidin oligomers (RPO) and polymers (RPP). The results of adsorption
248
and desorption behavior of the six macroporous resins to total procyanidins and
249
procyanidin dimers were shown in Table 1 and Table 2, respectively. According to
250
the results of PP and PD, one-way ANOVA test was used to the variable. If the
251
differences are statistically significant, then a search for the reason behind the
252
significant result is performed. The results of ANOVA test of PP and PD processed
253
by different resins were given in Tables 3 and Table 4. It can be seen that the values
254
between groups calculated by Fisher–Snedecor functions are higher than the tabulated
255
values of Fisher–Snedecor functions for a significance level α= 0.01. Therefore, the
256
null hypothesis is negated. By negating the null hypothesis (the null hypothesis
257
supposes that the resins have no influence on PP and PD, having values equal to zero),
258
indicate the values of the PP and PD processed by different resins were statistically
259
different for this experiment.
260
As revealed in Table 1 and Table 2, the adsorption and desorption capacity of
261
amilan for procyanidins and procyanidin dimers in crude procyanidin extracts was 13
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highest than that of other five resins. The PP and PD would reach 84.3 ± 0.8% and
263
41.5 ± 1.6% by amilan separation, respectively. Accordingly, amilan was chosen to as
264
the resin for increasing the PP and PD. On the other word, it was also clear that the
265
crude procyanidin extracts separate by amilan macroporous resin is a desirable
266
process to enhance the purity of radish procyanidins and procyanidin dimers. After
267
that, RPP were also separated. And RPP was depolymerized to low molecular weight
268
of RPO which can provide raw material for the preparation of high purity of radish
269
procyanidins dimer.
270
Depolymerization of radish procyanidin polymers.
271
HPLC-MS analysis of the depolymerization product of radish procyanidin
272
polymers. Figure 3a was the HPLC chromatogram of radish procyanidin oligomers
273
(RPO). It was shown that our present study exhibited a good separation of RPO. The
274
separation of each compound without peak merging indicated the specificity of the
275
detection method. According to the mass spectrometry (MS) analysis, the peaks at
276
17.1 and 17.8 min had [M-H]- m/z 289 which were identified as monomer (catechin or
277
epicatechin). Peaks at 21.2, 27.6, 31.4 and 37.8 min were recognized as a procyanidin
278
dimers according to [M-H]- m/z 577. Peaks at 40.9 and 45.3 min was confirmed as
279
trimers by [M-H]- m/z of 865. Peaks at 53.3 min was also confirmed as tetramers by
280
[M-H]- m/z of 1153. In addition, a little procyanidin polymers still existed as shown in
281
the peak at 69.8 min identified by [M-H]- m/z over 1440. And the percent of
282
monomers, dimers, trimers, tetramers and polymers were 12.5%, 39.3% and 19.1%,
283
6.7% and 22.4%, respectively. 14
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Figure 3b showed the HPLC chromatogram of radish procyanidin polymers
285
extracted from red radish. Only a main peak was shown in the HPLC chromatograms
286
and the retention time was 70 min. The main peak accounted for 96.2% of the total
287
procyanidins in radish procyanidin polymers. And the percentage of monomers,
288
dimers, trimers and tetramers were 0.5%, 1.6% 1.3% and 0.4%, respectively. The
289
mass spectrometry (MS) analysis moreover demonstrated that radish procyanidins
290
polymer contained exclusively high molecular weight of polymers which identified by
291
[M-H]- m/z over 1440. As shown in Figure 3c, depolymerization resulted in an
292
obviously decrease of this polymer peak and the increase of oligomer peaks, but
293
without tetramers produced. Peak at 18.6 min had [M-H]- m/z 289 which was
294
identified as monomer (catechin or epicatechin). Peak at 25.5 and 32.4 min were
295
recognized as a procyanidin dimer according to [M-H]- m/z 577. Peaks at 41.3 and
296
44.6 min were confirmed as trimers by [M-H]- m/z of 865. The result indicated
297
N-acetylneuraminate lyase (NAL) could depolymerize the carbon-carbon bonds in
298
radish procyanidin polymers to liberate monomer and dimer of lower molecular
299
weight. And radish procyanidins polymer was successfully depolymerized by NAL.
300
Optimization of the condition parameters on the depolymerization.
301
The effect of pH on the depolymerization. Figure 4a showed that the
302
depolymerization yield (DY) of 100 mL 50 mg/mL radish procyanidin polymers (RPP)
303
solution was depolymerized by 0.25 g NAL, at different pH, 50 oC and 20 g-force for
304
4 h. It was observed that DY increased gradually with pH increased from 4.0 to 8.0.
305
However, DY decreased when the pH over 8.0. The phenomenon might be explained 15
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as follows: at the beginning, the increase of pH accelerated radish procyanidin
307
polymers depolymerized into oligomers. And the content of procyanidin oligomers
308
increased which resulted in the increase of DY. But when pH increased to 9.0, the
309
intense alkaline condition affected the enzyme activity of NAL which resulting in the
310
decrease of DY. Accordingly, the optimal pH was 8.0.
311
The effect of reaction temperature on the depolymerization. Figure 4b showed
312
the depolymerization yield (DY) of 100 mL 50 mg/mL RPP solution was
313
depolymerized by 0.25g NAL at different temperature, pH 8.0 and 20 g-force for 4 h.
314
With the reaction temperature increased from 30 to 50 oC, DY increased from 23.12%
315
to 52.34%, but then decreased over the range, which could be seen that the reaction
316
temperature affected the movement of the molecules. Therefore, the activity of the
317
reactants and the rate of reaction were promoted gradually with the increase of the
318
temperature. However, the high temperature would make enzyme inactivation and
319
resulted in the decrease of DY. In addition, the reversible reaction was also
320
accelerated because the enzyme-catalyzed reaction was an exothermic reaction38. To
321
conclude, the optimal reaction temperature was 50 oC.
322
The effect of the mass ratio of NAL to RPP on the depolymerization. Figure 4c
323
showed the depolymerization yield (DY) of 100 mL 50 mg/mL RPP solution was
324
depolymerized by different mass ratio of NAL to RPP at pH 8.0, 50 oC and 20 g-force
325
for 4 h. When the mass ratio of NAL to RPP was set between 0.01-0.05, DY increased
326
gradually. But the further increase of mass ratio of NAL to RPP did not show any
327
clear influence on DY. That might be explained as that NAL catalyzed the 16
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depolymerized of carbon-carbon bonds in RPP to liberate monomer and dimer of
329
lower molecular weight. But after the binding of enzyme and the substrate reached
330
saturation, continued to increase the content of enzyme, DY could not significantly
331
increased. In terms of the depolymerization efficiencies, the optimal mass ratio of
332
NAL to RPP was determined at 0.05.
333
Preparative HPLC purification of radish procyanidin dimers. The high purity
334
of radish procyanidin dimers can be obtained from the radish procyanidin oligomers
335
(RPO) and the depolymerization production of RPP by the preparative HPLC system.
336
The result of preparative liquid chromatography was shown in Figure 5a. And Figure
337
5b was the analytical HPLC of the preparative radish procyanidin dimers. As shown
338
in Figure 5b, the purity of radish procyanidin dimers was 95.3 ± 0.2% in this process.
339
It was found that preparative HPLC purification would obviously improve the purity
340
of radish procyanidin dimers. In this study, every one gram of radish procyanidin
341
oligomers could get 8.12 ± 0.11 mg procyanidin dimers.
342
Structural elucidation of preparative radish procyanidin dimers. After the
343
purification of preparative HPLC, The structural elucidation of the high purity of
344
preparative radish procyanidin dimers was characterized by high resolution mass
345
spectrometry, one- and two-dimensional NMR.
346
The high resolution mass spectrometry analysis of the preparative radish
347
procyanidin dimers was shown in Figure 6a. It was observed that the characteristic
348
pseudo molecular ions [M-H]- at m/z 577 for procyanidin dimers with fragment ions
349
at m/z 577, 559, 451, 424, 289 and 150, which indicated the molecular formula of 17
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C30H25O12. Procyanidins are composed of the flavan-3-ol monomers (+)-catechin and
351
(―)-epicatechin units linked mainly through C4–C8 and/or C4–C6 (B-type). The
352
flavan-3-ols can also be doubly linked by an additional ether bond between C2 of the
353
upper unit and the oxygen at C7 or C5 of the lower unit (A-type)39. Procyanidin
354
dimers are the simplest procyanidin oligomers which polymerized by (+)-catechin or
355
(―)-epicatechin through A- or B-type as shown in Figure 6b. The postulated
356
fragmentation of the preparative radish procyanidin dimers was shown in Figure 6c
357
which taken B-type procyanidin dimers as example. The molecular weight of
358
procyanidin dimers is 578 which corresponded to the [M-H]- m/z of 577 (M Da,
359
Figure 6c)40. On the basis of the fragment ion with m/z 559 could be derived from the
360
ion with m/z 577 via the loss of water (M-H-18 Da, Figure 6c). The ion with m/z 451
361
could be formed from the ion with m/z 577 via heterocyclic ring fission (HRF) with
362
the loss of phloroglucinol of procyanidin dimers (M-126 Da, Figure 6c). The ion with
363
m/z 424 can result from retro-Diels-Alder reaction (RDA) of procyanidin dimers of
364
ring C of the lower unit and absence of m/z 150 (M-154 Da, Figure 6c). The ion with
365
m/z 289 was derived from quinone methide (QM) fission of procyanidin dimers with
366
the loss of (+)-catechin or (―)-epicatechin (M-289 Da, Figure 6c)41.
367
The spectrum of one-dimensional 1H NMR and 13C NMR of the preparative radish
368
procyanidin dimers were shown in Figure 7a and Figure 7b, respectively. In 1H
369
NMR (600 MHZ, acetone-d6, 240K), δ 2.38 (d, 1H, J = 13.8 Hz, H4t), 2.69 (d, 1H, J
370
= 13.8 Hz, H4t), 3.62 (s, 1OH, OH11u), 3.79 (s, 1OH, OH11t), 4.16 (s, 1H, H3t),
371
4.32* (d, 1H, J=67.8 Hz, H4u), 4.48 (d, 1H, J=27.6 Hz, H4u), 4.74 (s, 1H, H3u), 4.94 18
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(d, 1H, J=22.2 Hz, H2t, H2u), 5.71 (s, 1H, H6u), 5.81 (d, 1H, J=16.2, H8u, H6t), 6.52
373
(d, 1H, J=6.6 Hz, H2’t ), 6.64 (t, 1H, J=19.2 Hz, H6’t ), 6.85 (d, 1H, J=33.6 Hz, H3’u,
374
H3’t), 6.99 (s, 2H, H2’u, H6’u). (* rotamer B).
375
In
13
C NMR (600 MHZ, acetone-d6, 240K), δ 27.2* (C4t), 27.5 (C4t), 35.6 (C4u),
376
64.6* (C3t), 71.4 (C3t), 75.3* (C3u), 77.8 (C3u), 94.4 (C6t), 94.5 (C6u), 95.6 (C8u),
377
95.7* (C6u), 98.6 (C6t), 101.8 (C10u), 102.1* (C10u), 106.1 (C10t), 106.4* (C10t),
378
107.1 (C8t), 107.3* (C8t), 114.4* (C2’u, C6’u), 114.6 (C2’u, C6’u), 114.8* (C2’t,
379
C6’t), 114.8 (C2’t, C6’t), 117.7 (C3’u), 118.1 (C3’t), 130.2 (C1’t), 131.2 (C1’u), 144.0
380
(C4’t, C5’t) , 144.2* (C4’t, C5’t) , 144.5* (C4’u, C5’u), 144.5 (C4’u, C5’u), 152.8*
381
(C9t), 153.8 (C9t), 154.0* (C9u), 154.0 (C9u), 155.8* (C5t, C7t), 155.8 (C5t, C7t),
382
156.5* (C5u, C7u), 156.5 (C5u, C7u). (* rotamer B).
383
To further elucidate the structural of the preparative radish procyanidin dimers, the
384
two-dimensional homonuclear (1H-1H COSY),
385
Overhauser enhancement spectroscopy (NOESY), and heteronuclear (HSQC, HMBC)
386
were also employed. The results were shown in Figure 8.
387
1
1
H−1H phasesensitive nuclear
H-1H COSY spectrum afforded the assignment of the B- and C-rings protons.
388
From the H2’t and H3’t protons it was possible to determine the H2’ and H3’ protons
389
of the B-ring of the terminal unit. From the correlation of H2/H3 and H3/H4 of the
390
terminal unit it was possible to determine the H2, H3 and H4 protons of the C-ring of
391
the terminal unit. The addition correlations of H2’t/H6’t in the 1H-1H NOESY
392
spectrum and C2’/H2’, C3’/H3’and C6’/H6’ of the terminal unit in the HSQC-spectra
393
further verify the configuration of B-ring. Similarly, the configuration of A-ring was 19
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also identified by the correlation of C6/H6 and C8/H8 of the terminal unit in the
395
HSQC spectra and C8t/C6t in the HMBC spectrum. The correlations of C2/H2,
396
C3/H3 and C4/H4 of the terminal unit further verify the configuration of C-ring from
397
the HSQC-spectra. NOE correlations between H2’t and H6’t (B-ring) as well as H2t
398
(C-ring) allowed the identification of B- and C-rings of both units. The correlations of
399
C1’t/H2t and C10t/H4t in the HMBC-spectra further determine that the configuration
400
of preparative radish procyanidin dimers was flavan-3-ol unit. In addition, due to the
401
absence of NOE correlation of H2t and H4t with H3t, the terminal unit of flavan-3-ol
402
unit is identified as (―)-epicatechin (2, 3-cis configuration). Due to the absence of
403
these correlations, the upper unit was determined readily. The configuration of the
404
upper unit was also flavan-3-ol (2, 3-cis configuration). In the spectrum of HMBC,
405
the correlation of C8 of the terminal unit with H4 of the upper unit was characteristic
406
of a 4 → 8 interflavanoid linkages. In other words, this compound are linked C4 →
407
C8. Accordingly, the preparative radish procyanidin dimers was composed of
408
(―)-epicatechin units which were linked via a C4 → C8 bond (B-type), and this
409
preparative radish procyanidin dimers was (―)-epicatechin-4β → 8-(―)-epicatechin
410
(procyanidin B2).
411
In Conclusions, the present study showed that red radish was successively treated
412
with methanol extraction and macroporous resins separation to separate radish
413
procyanidin oligomers (RPO) and polymers (RPP). After that, the purity of
414
procyanidins (PP) and procyanidin dimers (PD) would achieve 41.5 ± 1.6% and 84.3
415
± 0.8% by 40:1 (v/m) methanol extraction and amilan macroporous resins separation. 20
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Depolymerization of radish procyanidin polymers (RPP) into oligomers was then
417
conducted by N-acetylneuraminate lyase (NAL). The HPLC-MS analysis of the
418
depolymerization product indicated that procyanidin polymers were successfully
419
depolymerized by NAL. Then high purity of procyanidin dimers was prepared by the
420
depolymerized procyanidin oligomers and PRO. The high purity of procyanidin
421
dimers (95.3 ± 0.2%) was prepared by preparative high performance liquid
422
chromatography. The complete structures of the preparative radish procyanidin dimers
423
were elucidated using high resolution mass spectrum, one- and two-dimensional
424
NMR.
425
(―)-epicatechin-4β → 8-(―)-epicatechin (procyanidin B2). This study presented a
426
desirable process for efficient production of high purity of procyanidin dimers from
427
red radish.
428
ACKONWLEDGEMENT
This
preparative
radish
procyanidin
dimers
was
identified
as
429
I would like to express my gratitude to all those who have helped me during the
430
writing of this manuscript. I gratefully acknowledge the help of my supervisor
431
professor Zhou Xiaohua. I do appreciate his patience, encouragement and professional
432
instruction for my manuscript. And I also appreciate the help of Dr. Yang Yang and
433
professional Zhou Zhiming. All authors approved the final manuscript.
434
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FUNDING SOURCES
549
This work was supported by the National Natural Science Foundation of China
550
(21206175 and 315014682), the Industrial Biotechnology Program of Tianjin
551
Municipal
552
Fundamental
553
106112017CDJXFLX0014), and the Henan Provincial Science and technology Open
554
cooperation projects (162106000014). This work is also partially supported by Open
555
Funding Project of the State Key Laboratory of Bioreactor Engineering, Shanghai,
556
China.
Science
and
Research
Technology Funds
for
Commission the
Central
(14ZCZDSY00066), Universities
27
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the No.
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FIGURE CAPTIONS Figure 1. Degradation mechanism of N-acetylneuraminic acid and procyanidin polymers. Figure 2. Influence of the ratio of methanol to radish on extraction yield, purity of procyanidin and purity of procyanidin dimers. Extraction temperature 50
o
C,
extraction time=2 h. Figure 3. HPLC chromatograms of (a) RPO, (b) RPP and (c) the depolymerization product of RPP at λ 280 nm. Figure 4. The effects of the condition parameters on the radish procyanidin polymers depolymerization (a. pH, t=50 oC, NAL/RPP=0.05, depolymerization reaction time=4 h; b. Reaction temperature, pH=8.0, NAL/RPP=0.05, depolymerization reaction time=4 h; c. The mass ratio of NAL to RPP, pH=8.0, t=50 oC, depolymerization reaction time=4 h). Figure 5. Preparative HPLC purification of radish procyanidin dimers (a. Preparative HPLC analysis of radish procyanidin dimers; b. HPLC analysis of the preparative radish procyanidin dimers). Figure 6. High resolution mass spectrum (a), structure of A-type and B-type (u: upper unit; t: terminal unit) (b) and postulated fragmentation (c) of the preparative radish procyanidin dimers. Figure 7. One-dimensional 1H NMR (a) and 13C NMR (b) spectra of the preparative radish procyanidin dimers. Figure 8. The two-dimensional NMR of 1H-1H COSY (a), 1H−1H NOESY (b), HSQC 28
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(c) and HMBC (d) spectra of the preparative radish procyanidin dimers.
29
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Table 1. The Adsorption and Desorption Behavior of The Resins to Total Procyanidins.
Resins
Adsorption capacity(mg/g)
Adsorption ratio(%)
Amilan
7.43 ± 0.07
93.3 ± 0.9
6.84 ± 0.06
92.1 ± 0.9
83.5
84.3
85.1
D-101
4.47 ± 0.05
53.8 ±0.6
4.13 ± 0.07
92.4 ± 1.4
68.4
69.5
70.7
AB-8
4.63 ± 0.10
57.6 ± 1.2
4.24 ± 0.07
91.6 ± 0.7
67.4
68.1
68.8
ADS-17
5.01 ± 0.09
62.1 ± 0.5
4.67 ± 0.09
93.2 ± 1.0
70.5
71.9
73.3
NKA-9
5.46 ± 0.12
67.8 ± 0.8
4.63 ± 0.10
84.8 ± 0.8
72.4
74.1
72.4
ADS-7
5.29 ± 0.09
64.5 ± 1.2
4.35 ± 0.07
82.2 ± 0.7
78.4
79.7
81.1
Desorption capacity(mg/g) Desorption ratio(%)
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Purity of procyanidins(%)
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Table 2. The Adsorption and Desorption Behavior of The Resins to Procyanidin Dimers.
Resins
Adsorption capacity(mg/g)
Adsorption ratio(%)
Amilan
3.79 ± 0.05
94.7 ± 1.3
3.46 ± 0.04
91.3 ± 1.1
39.9
41.5
43.1
D-101
1.31 ± 0.01
32.8 ±0.3
1.25 ± 0.02
95.4 ± 1.5
28.6
29.3
30.1
AB-8
1.32 ± 0.03
33.0 ± 0.7
1.22 ± 0.02
92.5 ± 1.5
27.3
28.5
29.7
ADS-17
1.68 ± 0.03
42.1 ± 0.7
1.58 ± 0.03
94.0 ± 1.7
30.1
31.5
32.9
NKA-9
2.23 ± 0.05
55.8 ± 1.3
1.91 ± 0.04
85.6 ± 1.7
30.7
32.8
34.9
ADS-7
2.42 ± 0.04
60.5 ± 1.0
2.03 ± 0.03
83.9 ± 1.1
34.2
35.7
37.2
Desorption capacity(mg/g) Desorption ratio(%) Purity of procyanidin dimer(%)
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Table 3. One-way ANOVA Result of The Purity of Procyanidins Processed By Different Resins.
Variation source
Freedom degrees number
Sum of Squares
Mean Square
F function calculated
F0.05
F0.01
Between Groups
2
16.8
8.40
59.31
4.10
7.56
Within Groups
5
587.7
117.54
829.69
3.33
5.64
Error
10
1.42
0.14
Total
17
605.92
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Table 4. One-way ANOVA Result of The Purity of Procyanidin Dimers Processed By Different Resins.
Variation source
Freedom degrees number
Sum of Squares
Mean Square
F function calculated
F0.05
F0.01
Between Groups
2
24.65
12.33
57.42
4.10
7.56
Within Groups
5
346.46
69.29
322.79
3.33
5.64
Error
10
2.15
0.21
Total
17
373.26
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Figure 1
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Figure 2
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Figure 3
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Figure 4
60
b
50
40
40
30 20 10
30 20
4
6
8
10
10
pH
c
60
50 DY (%)
DY (%)
a
30
40
50 DY (%)
60
Reaction temperature (oC)
60
40 30 20 10 0.00
50
0.02 0.04 0.06 0.08 0.10 The mass ratio of NAL to PPC
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Figure 5
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Figure 6
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Figure 7
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Figure 8
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TOC Graphic
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