TWI293628B - - Google Patents
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- TWI293628B TWI293628B TW89116495A TW89116495A TWI293628B TW I293628 B TWI293628 B TW I293628B TW 89116495 A TW89116495 A TW 89116495A TW 89116495 A TW89116495 A TW 89116495A TW I293628 B TWI293628 B TW I293628B
- Authority
- TW
- Taiwan
- Prior art keywords
- egcg
- green tea
- ecg
- gcg
- catechin
- Prior art date
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- WMBWREPUVVBILR-WIYYLYMNSA-N (-)-Epigallocatechin-3-o-gallate Chemical compound O([C@@H]1CC2=C(O)C=C(C=C2O[C@@H]1C=1C=C(O)C(O)=C(O)C=1)O)C(=O)C1=CC(O)=C(O)C(O)=C1 WMBWREPUVVBILR-WIYYLYMNSA-N 0.000 claims description 124
- WMBWREPUVVBILR-UHFFFAOYSA-N GCG Natural products C=1C(O)=C(O)C(O)=CC=1C1OC2=CC(O)=CC(O)=C2CC1OC(=O)C1=CC(O)=C(O)C(O)=C1 WMBWREPUVVBILR-UHFFFAOYSA-N 0.000 claims description 121
- 244000269722 Thea sinensis Species 0.000 claims description 93
- ADRVNXBAWSRFAJ-UHFFFAOYSA-N catechin Natural products OC1Cc2cc(O)cc(O)c2OC1c3ccc(O)c(O)c3 ADRVNXBAWSRFAJ-UHFFFAOYSA-N 0.000 claims description 84
- 235000005487 catechin Nutrition 0.000 claims description 84
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical group CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 70
- 235000013616 tea Nutrition 0.000 claims description 67
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 61
- PFTAWBLQPZVEMU-DZGCQCFKSA-N (+)-catechin Chemical compound C1([C@H]2OC3=CC(O)=CC(O)=C3C[C@@H]2O)=CC=C(O)C(O)=C1 PFTAWBLQPZVEMU-DZGCQCFKSA-N 0.000 claims description 51
- 229950001002 cianidanol Drugs 0.000 claims description 49
- 239000000203 mixture Substances 0.000 claims description 47
- RYYVLZVUVIJVGH-UHFFFAOYSA-N caffeine Chemical compound CN1C(=O)N(C)C(=O)C2=C1N=CN2C RYYVLZVUVIJVGH-UHFFFAOYSA-N 0.000 claims description 46
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 41
- 235000009569 green tea Nutrition 0.000 claims description 40
- 229920005989 resin Polymers 0.000 claims description 37
- 239000011347 resin Substances 0.000 claims description 37
- 150000001765 catechin Chemical class 0.000 claims description 36
- PFTAWBLQPZVEMU-UKRRQHHQSA-N (-)-epicatechin Chemical compound C1([C@H]2OC3=CC(O)=CC(O)=C3C[C@H]2O)=CC=C(O)C(O)=C1 PFTAWBLQPZVEMU-UKRRQHHQSA-N 0.000 claims description 31
- 238000000034 method Methods 0.000 claims description 30
- 239000002904 solvent Substances 0.000 claims description 29
- PFTAWBLQPZVEMU-ZFWWWQNUSA-N (+)-epicatechin Natural products C1([C@@H]2OC3=CC(O)=CC(O)=C3C[C@@H]2O)=CC=C(O)C(O)=C1 PFTAWBLQPZVEMU-ZFWWWQNUSA-N 0.000 claims description 27
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 27
- LPTRNLNOHUVQMS-UHFFFAOYSA-N epicatechin Natural products Cc1cc(O)cc2OC(C(O)Cc12)c1ccc(O)c(O)c1 LPTRNLNOHUVQMS-UHFFFAOYSA-N 0.000 claims description 27
- 235000012734 epicatechin Nutrition 0.000 claims description 27
- XMOCLSLCDHWDHP-IUODEOHRSA-N epi-Gallocatechin Chemical compound C1([C@H]2OC3=CC(O)=CC(O)=C3C[C@H]2O)=CC(O)=C(O)C(O)=C1 XMOCLSLCDHWDHP-IUODEOHRSA-N 0.000 claims description 24
- LPHGQDQBBGAPDZ-UHFFFAOYSA-N Isocaffeine Natural products CN1C(=O)N(C)C(=O)C2=C1N(C)C=N2 LPHGQDQBBGAPDZ-UHFFFAOYSA-N 0.000 claims description 23
- 229960001948 caffeine Drugs 0.000 claims description 23
- VJEONQKOZGKCAK-UHFFFAOYSA-N caffeine Natural products CN1C(=O)N(C)C(=O)C2=C1C=CN2C VJEONQKOZGKCAK-UHFFFAOYSA-N 0.000 claims description 23
- 235000020688 green tea extract Nutrition 0.000 claims description 22
- 229940094952 green tea extract Drugs 0.000 claims description 20
- 239000003960 organic solvent Substances 0.000 claims description 19
- 238000012360 testing method Methods 0.000 claims description 19
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims description 18
- 238000002360 preparation method Methods 0.000 claims description 15
- XMOCLSLCDHWDHP-UHFFFAOYSA-N L-Epigallocatechin Natural products OC1CC2=C(O)C=C(O)C=C2OC1C1=CC(O)=C(O)C(O)=C1 XMOCLSLCDHWDHP-UHFFFAOYSA-N 0.000 claims description 12
- DZYNKLUGCOSVKS-UHFFFAOYSA-N epigallocatechin Natural products OC1Cc2cc(O)cc(O)c2OC1c3cc(O)c(O)c(O)c3 DZYNKLUGCOSVKS-UHFFFAOYSA-N 0.000 claims description 12
- 230000036541 health Effects 0.000 claims description 11
- 239000011148 porous material Substances 0.000 claims description 11
- 229920001429 chelating resin Polymers 0.000 claims description 10
- 238000010521 absorption reaction Methods 0.000 claims description 9
- 239000002253 acid Substances 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 9
- KRKNYBCHXYNGOX-UHFFFAOYSA-K Citrate Chemical compound [O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O KRKNYBCHXYNGOX-UHFFFAOYSA-K 0.000 claims description 8
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Natural products OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 claims description 6
- 239000004952 Polyamide Substances 0.000 claims description 4
- YCIMNLLNPGFGHC-UHFFFAOYSA-N catechol Chemical compound OC1=CC=CC=C1O YCIMNLLNPGFGHC-UHFFFAOYSA-N 0.000 claims description 4
- 238000003795 desorption Methods 0.000 claims description 4
- 229920002647 polyamide Polymers 0.000 claims description 4
- 230000008929 regeneration Effects 0.000 claims description 4
- 238000011069 regeneration method Methods 0.000 claims description 4
- 238000005406 washing Methods 0.000 claims description 4
- CIWBSHSKHKDKBQ-DUZGATOHSA-N D-isoascorbic acid Chemical compound OC[C@@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-DUZGATOHSA-N 0.000 claims description 3
- 150000001298 alcohols Chemical class 0.000 claims description 3
- 235000010323 ascorbic acid Nutrition 0.000 claims description 3
- 229960005070 ascorbic acid Drugs 0.000 claims description 3
- 239000011668 ascorbic acid Substances 0.000 claims description 3
- 229960004106 citric acid Drugs 0.000 claims description 3
- 235000015165 citric acid Nutrition 0.000 claims description 3
- 235000010350 erythorbic acid Nutrition 0.000 claims description 3
- 229940026239 isoascorbic acid Drugs 0.000 claims description 3
- TYQCGQRIZGCHNB-JLAZNSOCSA-N l-ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(O)=C(O)C1=O TYQCGQRIZGCHNB-JLAZNSOCSA-N 0.000 claims description 3
- 229920000768 polyamine Polymers 0.000 claims description 3
- 239000004925 Acrylic resin Substances 0.000 claims description 2
- 150000002148 esters Chemical class 0.000 claims description 2
- 150000002576 ketones Chemical class 0.000 claims description 2
- 229920000058 polyacrylate Polymers 0.000 claims description 2
- 229920000728 polyester Polymers 0.000 claims description 2
- 229920000193 polymethacrylate Polymers 0.000 claims description 2
- 230000001172 regenerating effect Effects 0.000 claims description 2
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 claims 4
- PCTMTFRHKVHKIS-BMFZQQSSSA-N (1s,3r,4e,6e,8e,10e,12e,14e,16e,18s,19r,20r,21s,25r,27r,30r,31r,33s,35r,37s,38r)-3-[(2r,3s,4s,5s,6r)-4-amino-3,5-dihydroxy-6-methyloxan-2-yl]oxy-19,25,27,30,31,33,35,37-octahydroxy-18,20,21-trimethyl-23-oxo-22,39-dioxabicyclo[33.3.1]nonatriaconta-4,6,8,10 Chemical compound C1C=C2C[C@@H](OS(O)(=O)=O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CCCC(C)C)[C@@]1(C)CC2.O[C@H]1[C@@H](N)[C@H](O)[C@@H](C)O[C@H]1O[C@H]1/C=C/C=C/C=C/C=C/C=C/C=C/C=C/[C@H](C)[C@@H](O)[C@@H](C)[C@H](C)OC(=O)C[C@H](O)C[C@H](O)CC[C@@H](O)[C@H](O)C[C@H](O)C[C@](O)(C[C@H](O)[C@H]2C(O)=O)O[C@H]2C1 PCTMTFRHKVHKIS-BMFZQQSSSA-N 0.000 claims 2
- 241000736199 Paeonia Species 0.000 claims 2
- 235000006484 Paeonia officinalis Nutrition 0.000 claims 2
- 241000252233 Cyprinus carpio Species 0.000 claims 1
- 241000239226 Scorpiones Species 0.000 claims 1
- 238000013375 chromatographic separation Methods 0.000 claims 1
- 239000008187 granular material Substances 0.000 claims 1
- 230000000366 juvenile effect Effects 0.000 claims 1
- 239000000546 pharmaceutical excipient Substances 0.000 claims 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims 1
- HNJBEVLQSNELDL-UHFFFAOYSA-N pyrrolidin-2-one Chemical compound O=C1CCCN1 HNJBEVLQSNELDL-UHFFFAOYSA-N 0.000 claims 1
- 239000004575 stone Substances 0.000 claims 1
- 235000021419 vinegar Nutrition 0.000 claims 1
- 239000000052 vinegar Substances 0.000 claims 1
- 235000013618 yogurt Nutrition 0.000 claims 1
- 238000004128 high performance liquid chromatography Methods 0.000 description 41
- 238000000926 separation method Methods 0.000 description 28
- 239000007858 starting material Substances 0.000 description 27
- 239000000284 extract Substances 0.000 description 23
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 12
- 150000001875 compounds Chemical class 0.000 description 12
- 230000000694 effects Effects 0.000 description 12
- 239000012141 concentrate Substances 0.000 description 11
- 230000002079 cooperative effect Effects 0.000 description 11
- 239000000843 powder Substances 0.000 description 10
- 239000000243 solution Substances 0.000 description 10
- 239000003480 eluent Substances 0.000 description 9
- 238000010828 elution Methods 0.000 description 9
- 150000008442 polyphenolic compounds Chemical class 0.000 description 9
- 235000013824 polyphenols Nutrition 0.000 description 9
- 238000001704 evaporation Methods 0.000 description 8
- 238000002835 absorbance Methods 0.000 description 7
- 230000008020 evaporation Effects 0.000 description 7
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 6
- GHVNFZFCNZKVNT-UHFFFAOYSA-N Decanoic acid Natural products CCCCCCCCCC(O)=O GHVNFZFCNZKVNT-UHFFFAOYSA-N 0.000 description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 238000002474 experimental method Methods 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 229910052757 nitrogen Inorganic materials 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- 238000004587 chromatography analysis Methods 0.000 description 5
- 238000007639 printing Methods 0.000 description 5
- GYSCBCSGKXNZRH-UHFFFAOYSA-N 1-benzothiophene-2-carboxamide Chemical compound C1=CC=C2SC(C(=O)N)=CC2=C1 GYSCBCSGKXNZRH-UHFFFAOYSA-N 0.000 description 4
- -1 Ethanol Compound Chemical class 0.000 description 4
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 4
- 230000008859 change Effects 0.000 description 4
- HVYWMOMLDIMFJA-DPAQBDIFSA-N cholesterol Chemical compound C1C=C2C[C@@H](O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CCCC(C)C)[C@@]1(C)CC2 HVYWMOMLDIMFJA-DPAQBDIFSA-N 0.000 description 4
- 239000011552 falling film Substances 0.000 description 4
- 235000013305 food Nutrition 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 2
- TUSDEZXZIZRFGC-UHFFFAOYSA-N 1-O-galloyl-3,6-(R)-HHDP-beta-D-glucose Natural products OC1C(O2)COC(=O)C3=CC(O)=C(O)C(O)=C3C3=C(O)C(O)=C(O)C=C3C(=O)OC1C(O)C2OC(=O)C1=CC(O)=C(O)C(O)=C1 TUSDEZXZIZRFGC-UHFFFAOYSA-N 0.000 description 2
- 244000235603 Acacia catechu Species 0.000 description 2
- 235000006226 Areca catechu Nutrition 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- 239000001263 FEMA 3042 Substances 0.000 description 2
- LRBQNJMCXXYXIU-PPKXGCFTSA-N Penta-digallate-beta-D-glucose Natural products OC1=C(O)C(O)=CC(C(=O)OC=2C(=C(O)C=C(C=2)C(=O)OC[C@@H]2[C@H]([C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)O2)OC(=O)C=2C=C(OC(=O)C=3C=C(O)C(O)=C(O)C=3)C(O)=C(O)C=2)O)=C1 LRBQNJMCXXYXIU-PPKXGCFTSA-N 0.000 description 2
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- 239000011521 glass Substances 0.000 description 2
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 2
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- BQJCRHHNABKAKU-KBQPJGBKSA-N morphine Chemical compound O([C@H]1[C@H](C=C[C@H]23)O)C4=C5[C@@]12CCN(C)[C@@H]3CC5=CC=C4O BQJCRHHNABKAKU-KBQPJGBKSA-N 0.000 description 2
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- LRBQNJMCXXYXIU-NRMVVENXSA-N tannic acid Chemical compound OC1=C(O)C(O)=CC(C(=O)OC=2C(=C(O)C=C(C=2)C(=O)OC[C@@H]2[C@H]([C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)O2)OC(=O)C=2C=C(OC(=O)C=3C=C(O)C(O)=C(O)C=3)C(O)=C(O)C=2)O)=C1 LRBQNJMCXXYXIU-NRMVVENXSA-N 0.000 description 2
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- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
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Landscapes
- Tea And Coffee (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Pyrane Compounds (AREA)
Description
經濟部智慧財產局員工消費合作社印製 1293628 A7 _B7_ 五、發明說明(1 ) 本發明係關(_)·表掊兒茶素培酸鹽(EGCG)的製法。本發 明特別敘述包含以粗孔樹脂處理自茶兒茶酸類中分離製備 EGCG之方法。 綠茶植物camellia sinensis的葉含乾重量基多達36%多驗類 ,但成分隨氣候、季節、種類及成熟狀態變化。綠茶兒茶 酸類爲綠茶多酚的主體。兒茶酸實例爲-表兒茶酸(EC) ,(-)-表掊兒茶素培酸鹽(EGCG),表掊兒茶酸(EGC)及表 兒茶素培酸鹽(ECG)。 EGCG爲上述兒茶素中最有利的化合物因其發揮強抗氧 效。且經證實EGCG具抗突變效應、殺菌效果及對血液内 膽固酸水準亦具有利影響。茶中其他兒茶素類效力遠遜。 綠茶亦含其他成分如咖啡鹼,蛋白質,果膠及/或可能不 適宜之金屬離子。 因此需要用一簡單經濟的方法高產率析離純式EGCG。 不過,多種茶兒茶素之結構相似使個別兒茶素難以分離。 而且茶内兒茶素通常伴隨咖啡鹼含量綠茶葉乾質量達4 % 。已知咖啡鹼與兒茶素結合,不易脱除。 製造茶萃提物爲技術上所週知。美國專利5,879,733號敘 述有改進澄清度與色澤的綠茶萃取物製法。在25°C至6 0 °C 範圍内溫度以一種數量之食品級陽離子交換樹脂有效脱除 萃出液内所含金屬陽離子處理綠茶得茶萃液。經過處理的 萃出液隨後接觸一奈米濾膜。但US 5,879,733内所述方法不 適合自茶兒茶酸混合物中分離EGCG。 美國專利4,613,672號説明純EGCG之製法含以下步驟:以 -4- 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) ---------U--裝------t — 訂 --------Aw (請先閱讀背面之注意事項再填寫本頁) 1293628 A7 B7 五、發明說明(2 ) 熱水或用40- 75%甲醇、40_ 75%乙醇或30- 80〇/〇丙酮的水液 萃提茶葉。所得萃液以氣仿洗過,溶解洗後萃液於一有機 溶劑。餾除有機溶劑,濃萃出組份用逆相分配塔接受高速 液體層析法用丙醇/四氫呋喃/水(〇 _ 25 : 〇 - 35 : 65-85, vol%)之展顯劑藉使㈠表兒茶素、㈠表掊兒茶素、(_)表兒 茶素掊酸鹽及㈠表掊兒茶素掊酸鹽各別析離。美國專利 4,613,672號中所述方法因使用筇貴塔填料而無法在工業规 模下經濟生產EGCG。而且美國專利4,613,672號所述方法因 使用溶劑混合物(丙酮/四氫呋喃/氯仿)非食物核准級以致 不容許生產能加入食物產品的EGCG。 技術説明生產兒茶素爲混合物,仍有需要簡單安全及經 濟方法生產純態EGCG作組成份供掺入添加物與食品。 效經發現能自茶兒茶素與/或咖啡臉混合物中離析EGCG ,當進行析離時用一粗孔極性樹脂與一適當極性洗提溶劑 而得進步選擇性。 於是本發明指導一種製造表掊兒茶素掊酸鹽(E〇CG)的方 法,包含步驟有: 經濟部智慧財產局員工消費合作社印製 ----------*--裝------* 丨訂· (請先閱讀背面之注音?事項再填寫本頁) a) 製造一綠茶萃出液; b) 將綠茶萃液於溫度範園約i〇°C至約80°C内在粗孔極性 樹脂上接受色層分離; c) 以極性洗提溶劑於約1〇X:至約80。(:範園内溫度及約0.1 巴至約50巴範圍内壓力洗提粗孔極性樹脂中EGCG ; d) 隨意濃縮c)步之洗出液; e) 隨意解吸餘留的兒茶素再生粗孔極性樹脂,·及 -5- 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 1293628 A7 B7 經濟部智慧財產局員工消費合作社印製 五、發明說明(3 ) f)隨意濃縮e)步之解吸兒茶素。 製造作始材料用的綠茶萃液爲技術上所週知者。例如, 典型以熱或冷水萃提綠茶葉作一含茶兒茶素與咖啡鹼之溶 液。此綠茶液能再濃縮作成隨意濃萃液或乾粉。萃液或粉 能含穩定劑諸如食品認可的酸類例如檸檬酸、抗壞血酸、 異抗壞血酸之類。 茶萃粉亦可購得商品例如自Guizhou Highyin Biological Product Co·,Guiyang,P.R. China,或 Zhejang Zhongke Plant Technical Co. Ltd·,Hangzhou,Zhejang,P.R. China 0 EGCG的分離典型藉使綠茶萃液接受充填粗孔極性樹月旨 塔達成。 此處所用"粗孔極性樹脂"指丙烯酸型樹脂諸如聚丙烯酸 酯如可自 Rohm & Haas,Philadelphia,Pa_ 獲得之 AMBERLITE® XAD-7或聚異丁烯酸酯如可得自Toso Haas的 AMBERCHROM® CG-71或自賓州費城三菱化學之DIAION HP 2MG ;或得自德國Darmstadt默克的聚醯胺如Polyamide 11 ; 得自瑞士 Buchs,Fluka之 Polyamide 6 與 Nylon 6,6 (分另1J 目錄 02395 及 74712號);得自瑞士Domat,EMS Chemie 的(Grilamid L 25 natur) Polyamide 12 ;或得自Sigma之聚乙晞基ρ比洛燒酮 Ρ6755 ;或者芳屬聚醯胺及聚酯等。 樹脂作業較佳經過脱氣並以洗提溶劑平衡。 根據本發明的方法係於約l〇°C至約80°C範園,較佳約40 °C至約60°C内溫度完成。能置塔於恆溫控制區例如一加熱 套管内實行恆溫控制。 -6- 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) ------------裝-------I ------- (請先閱讀背面之注意事項再填寫本頁) I293628Ministry of Economic Affairs Intellectual Property Bureau employee consumption cooperative printing 1293628 A7 _B7_ V. Description of the invention (1) The present invention relates to the production method of _ _ · 掊 catechin catechin (EGCG). The present invention specifically describes a method for separating and preparing EGCG from tea catechus by treatment with a coarse pore resin. The leaf of the green tea plant camellia sinensis contains up to 36% of the dry weight, but the composition varies with climate, season, species and maturity. Green tea catechu The acid is the main body of green tea polyphenols. Examples of catechins are - epicatechin (EC), (-)-epiphylline catechin (EGCG), epigallocatechin (EGC) and epicatechin (ECG). EGCG is the most advantageous compound of the above catechins because it exerts strong antioxidant activity. It has been confirmed that EGCG has an anti-mutation effect, a bactericidal effect and a positive effect on the level of blood cholesterol. Other catechins in tea are far less effective. Green tea also contains other ingredients such as caffeine, protein, pectin and/or metal ions that may not be suitable. Therefore, it is necessary to separate the pure EGCG in a high yield by a simple and economical method. However, the similar structure of various tea catechins makes it difficult to separate individual catechins. Moreover, tea catechins are usually accompanied by caffeine content of green tea leaves to a dry mass of 4%. It is known that caffeine is combined with catechin and is not easily removed. The manufacture of tea extracts is well known in the art. U.S. Patent No. 5,879,733 describes the preparation of green tea extracts which improve clarity and color. Effectively remove the metal cation-containing green tea extract from the metal cation exchange resin in the extract at a temperature ranging from 25 ° C to 60 ° C with a quantity of food grade cation exchange resin. The treated extract is then contacted with a nanofiltration membrane. However, the method described in U.S. Patent 5,879,733 is not suitable for the separation of EGCG from a tea catechin mixture. U.S. Patent No. 4,613,672 describes the preparation of pure EGCG with the following steps: Applying the Chinese National Standard (CNS) A4 specification (210 X 297 mm) to -4- this paper scale --------- U-- -----t — order--------Aw (please read the notes on the back and fill out this page) 1293628 A7 B7 V. Description of invention (2) Hot water or 40- 75% methanol, The tea leaves are extracted from 40_75% ethanol or 30-80 〇/〇 acetone. The resulting extract was washed with a gas imitation, and the washed extract was dissolved in an organic solvent. The organic solvent is distilled off, and the concentrated extract component is subjected to high-speed liquid chromatography using a reverse phase distribution column for propanol/tetrahydrofuran/water (〇_ 25 : 〇- 35 : 65-85, vol%). (1) Epicatechin, (1) epigallocatechin, (_) epicatechin citrate and (1) epigallocatechin catechin. The process described in U.S. Patent No. 4,613,672 is not economically capable of producing EGCG in an industrial scale due to the use of the ruthenium packing. Moreover, the method described in U.S. Patent No. 4,613,672 is not approved for use in the use of a solvent mixture (acetone/tetrahydrofuran/chloroform) to produce EGCG which can be added to food products. Technical Note The production of catechins is a mixture, and there is still a need for simple, safe and economical production of pure EGCG as a component for incorporation of additives and foods. It has been found that EGCG can be isolated from tea catechins and/or coffee face mixtures, and a coarse-pored polar resin and a suitable polar eluting solvent are used for the separation to obtain improved selectivity. Therefore, the present invention directs a method for producing epigallocatechin citrate (E〇CG), including the steps of: Ministry of Economic Affairs, Intellectual Property Bureau, Staff Consumption Cooperative, Printing ---------------- ------* 丨定· (Please read the phonetic transcription on the back? Please fill out this page again) a) Make a green tea extract; b) Place the green tea extract at a temperature of about 〇 °C to about The color layer separation is carried out on the coarse pore polar resin at 80 ° C; c) the solvent is eluted with a polarity of from about 1 〇X: to about 80. (: FFCG in the temperature of the park and the pressure in the range of about 0.1 bar to about 50 bar; d) arbitrarily concentrate c) the eluate of the step; e) freely desorb the remaining catechin to regenerate the coarse hole Polar resin, ··-5- This paper scale applies to China National Standard (CNS) A4 specification (210 X 297 mm) 1293628 A7 B7 Ministry of Economic Affairs Intellectual Property Bureau employee consumption cooperative printing 5, invention description (3) f) random Concentrate e) to desorb catechins. Green tea extracts for the manufacture of starting materials are well known in the art. For example, green tea leaves are typically extracted from hot or cold water as a solution containing tea catechins and caffeine. The green tea solution can be re-concentrated to form a concentrated concentrate or dry powder. The extract or powder can contain stabilizers such as food-accepted acids such as citric acid, ascorbic acid, isoascorbic acid and the like. The tea extract powder may also be purchased from a product such as Guizhou Highyin Biological Product Co., Guiyang, PR China, or Zhejang Zhongke Plant Technical Co. Ltd., Hangzhou, Zhejang, PR China 0 EGCG, and the green tea extract is filled. The rough hole polarity tree is reached. As used herein, "coarse polar resin" refers to acrylic resins such as polyacrylates such as AMBERLITE® XAD-7 or polymethacrylate available from Rohm & Haas, Philadelphia, Pa_, such as AMBERCHROM available from Toso Haas. ® CG-71 or DIAION HP 2MG from Mitsubishi Chemical, Pennsylvania; or Polyamide from Merck, Darmstadt, Germany, such as Polyamide 11; Polyamide 6 and Nylon 6, 6 from Fluka, Buchs, Switzerland (in 1J) 02395 and 74712); (Grilamid L 25 natur) Polyamide 12 from EMS Chemie, Domat, Switzerland; or polyethylidene phloprofenone 6755 from Sigma; or aromatic polyamine and polyester. The resin operation is preferably degassed and equilibrated with the elution solvent. The process according to the invention is carried out at a temperature of from about 10 ° C to about 80 ° C, preferably from about 40 ° C to about 60 ° C. The tower can be thermostatically controlled in a thermostatic control zone such as a heating jacket. -6- This paper scale applies to China National Standard (CNS) A4 specification (210 X 297 mm) ------------Installation-------I------- (Please read the notes on the back and fill out this page) I293628
五、發明說明(4 ) 經濟部智慧財產局員工消費合作社印製 流動相經過塔下之液壓能在廣限度内變化。流動相宜於 約〇·1至約50巴,較佳於約〇」至約2〇巴,尤佳在〇^至約1〇 巴的壓力泵過塔體。 流動相包含一極性洗提溶劑乃是水與一有機溶劑之混合 物。此處用辭’’有機溶劑”指醇類諸如甲醇、乙醇及異丙醇 之類,酮類如丙酮或酯類如醋酸乙酯或其混合物等。使用 食品級醇以乙醇與異丙醇爲佳。用一含約7〇至約95 v〇1%, 較佳約90 vol %的水,與約5至約3〇 vol %,較佳約1〇 v〇1% 之有機溶劑混合物的流動相時所得結果特佳。將活動相脱 氣並保持其於惰性氣氛如氮或說下有利。 塔以流動相調節。流動相經過塔柱之流速能在廣限度内 變化。流量在約0.5至約20床體積/h範圍間,宜約〇.5至約1〇 床體積/h,更佳約〇_8至約5床體積/h。〇床體積相當於i m3溶液或每m3樹脂的溶劑)。 靜止相與流動相間確立平衡後將茶萃出液引進流動相, 於是使綠茶萃液在粗孔極性樹脂上接受層析。若用綠茶萃 粉作始材料則溶解此粉於流動相中。若用水性綠茶萃液則 添加有機溶劑便利調整萃液内水對有機溶劑比流動相内之 二者比。 本發明一重要特色爲於約l〇°C至約80°C,較佳約40°C至 約60°C範圍内溫度以粗孔極性樹脂處理綠茶萃液並以極性 洗提溶劑洗提。此樹脂、洗提液與溫度三種特色的特別互 相作用形成本發明一重要情景,引導自茶兒茶素與/或咖 讲驗混合物中明確分離EGCG,洗提後遂得一 EGCG部分, 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) ------r — l! 裝·! — I f I 訂 ί------- (請先閱讀背面之注意事項再填寫本頁) 1293628 A7 B7 五、發明說明(5 ) 按萃液或濃縮液内所有兒茶素總量計含至少75%,較佳 85%以上,尤佳約90%至約97%之EGCG。 (請先閱讀背面之注意事項再填寫本頁) 粗孔極性樹脂吸收咖啡鹼、EGCG及剩餘兒茶素的能力 亦視所用洗提劑及溫度而異。對咖啡鹼之親和力遜於對 EGCG者,因此如有咖啡驗存在將先洗出而能分開。又如 合宜亦可從而回收提純式咖啡鹼,亦能係一經濟優點。其 次析離其中含EGCG部分。其餘茶兒茶素比EGCG表現較強 親和力,於是用一能解吸其餘兒茶素的溶劑再生直到樹脂 吸收其餘者。舉例,其餘兒茶素能以一純有機溶劑洗提或 者改變流動相内水對有機溶劑之比率。適宜再生溶劑係例 如一純有機溶劑或一約10-60 vo 1 %水與約40_ 90 vol%有機 溶劑的混合物,較佳約40 vol%水與約60 vol%之有機溶劑。 洗提液中EGCG的濃縮能用技術上週知方法例如蒸發完 成。EGCG洗出液能蒸乾成含高純度EGCG之粉未或濃縮至 可結晶。進行濃縮能在洗出液内添加一穩定劑諸如食品認 可的酸如擰檬酸、抗壞血酸及異抗壞血酸之類。酸添加量 以相對EGCG約0.1至約2.5 %爲宜。 經濟部智慧財產局員工消費合作社印製 含咖啡鹼的預先部分與含其餘兒茶素之e)步部分能按上 述濃縮。 製程能用單一塔或多層析塔系進行。程序亦能用技術上 稱作”模擬移動床色層分析術”或”環狀層析術”的技藝完成。 本發明方法能以簡單經濟作業實現,因此能實用於產量 與處理方面作大規模生產。 上述所製EGCG具有強抗氧化活性,故能用作各種食 -8- 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 1293628 A7 _B7_ 五、發明說明(6 ) / 、化妝品及油類等之抗氧化劑。此外,EGCG有抗致突變 效應、殺菌效果、及對血液内膽固醇水準的有利影響。因 此,濃縮或純EGCG適用於保健製劑等。 參考以下實例更詳例證本發明。V. Description of invention (4) Printed by the Consumers' Cooperative of the Intellectual Property Office of the Ministry of Economic Affairs The hydraulic energy of the mobile phase passing through the tower varies within wide limits. The flow rate is preferably from about 1 to about 50 bar, preferably from about 〇 to about 2 mbar, and particularly preferably from 〇 to about 1 Torr. The mobile phase comprises a polar eluting solvent which is a mixture of water and an organic solvent. The term "organic solvent" as used herein refers to alcohols such as methanol, ethanol and isopropanol, ketones such as acetone or esters such as ethyl acetate or mixtures thereof, etc. The use of food grade alcohols with ethanol and isopropanol is used. Preferably, the flow of a mixture of organic solvents containing from about 7 Torr to about 95 v 〇 1%, preferably about 90 vol%, and from about 5 to about 3 vol%, preferably about 1 〇v 〇 1%, is used. The results obtained are particularly good. The activity phase is degassed and maintained in an inert atmosphere such as nitrogen or in the bottom. The column is regulated by the mobile phase. The flow rate of the mobile phase through the column can vary within wide limits. The flow rate is about 0.5 to Between about 20 bed volume / h range, preferably from about 55 to about 1 〇 bed volume / h, more preferably from about 〇 8 to about 5 bed volume / h. The volume of the trampoline is equivalent to i m3 solution or per m3 resin Solvent). After the equilibrium between the stationary phase and the mobile phase is established, the tea extract is introduced into the mobile phase, and then the green tea extract is subjected to chromatography on the crude pore polar resin. If the green tea extract is used as the starting material, the powder is dissolved in the mobile phase. If the aqueous green tea extract is added, the organic solvent is added to conveniently adjust the water in the extract to the organic solvent to the mobile phase. An important feature of the present invention is that the green tea extract is treated with a coarse pore polar resin at a temperature ranging from about 10 ° C to about 80 ° C, preferably from about 40 ° C to about 60 ° C, and washed with a polar eluting solvent. The special interaction of the three characteristics of the resin, the eluent and the temperature forms an important scene of the invention, guiding the clear separation of the EGCG from the tea catechin and/or the coffee test mixture, and extracting an EGCG part after the elution. This paper scale applies to the Chinese National Standard (CNS) A4 specification (210 X 297 mm) ------r — l! Pack·! — I f I order ί------- (please read the back first) Note: Please fill out this page again) 1293628 A7 B7 V. Inventive Note (5) According to the total amount of all catechins in the extract or concentrate, at least 75%, preferably more than 85%, especially about 90% to about 97% of EGCG. (Please read the notes on the back and fill out this page.) The ability of coarse pore polar resin to absorb caffeine, EGCG and remaining catechins varies depending on the eluent used and temperature. The affinity for caffeine is inferior to that of caffeine. For EGCG, if there is a coffee test, it will be washed out first and can be separated. If it is convenient, it can be recycled. Morphine can also be an economic advantage. Secondly, it contains EGCG. The other tea catechins have stronger affinity than EGCG, so they are regenerated with a solvent that can desorb the remaining catechins until the resin absorbs the rest. For example, The remaining catechins can be eluted with a pure organic solvent or the ratio of water to organic solvent in the mobile phase. Suitable regenerating solvent is, for example, a pure organic solvent or a solvent of about 10-60 vo 1% water and about 40_90 vol% organic. A mixture of solvents, preferably about 40 vol% water and about 60 vol% organic solvent. The concentration of EGCG in the eluate can be accomplished by methods well known in the art, such as evaporation. The EGCG eluate can be evaporated to a powder containing high purity EGCG or concentrated to crystallize. Concentration can add a stabilizer such as a food-recognized acid such as citric acid, ascorbic acid, and isoascorbic acid to the eluate. The amount of acid added is preferably from about 0.1 to about 2.5% relative to EGCG. Printed by the Intellectual Property Office of the Ministry of Economic Affairs, the Consumer Cooperatives, the pre-parts containing caffeine and the e) step containing the remaining catechins can be concentrated as described above. The process can be carried out using a single column or multiple chromatography columns. The procedure can also be accomplished using techniques known in the art as "simulated moving bed chromatography" or "ring tomography". The method of the present invention can be realized in a simple and economical operation, and thus can be practically used for mass production in terms of production and processing. The above-mentioned EGCG has strong antioxidant activity, so it can be used as a variety of food--8-paper scales. It is applicable to China National Standard (CNS) A4 specification (210 X 297 mm). 1293628 A7 _B7_ V. Invention description (6) / , Antioxidants such as cosmetics and oils. In addition, EGCG has an anti-mutagenic effect, a bactericidal effect, and a beneficial effect on the level of cholesterol in the blood. Therefore, concentrated or pure EGCG is suitable for use in health care preparations and the like. The invention is illustrated in more detail with reference to the following examples.
實例1 分離EGCG 用含不同兒茶素與咖啡鹼之綠茶萃(中國大陸貴陽貴州 Highyin生物產品公司製"綠茶精,最低95%多酚類π )作始 材料。茶組份濃度用UV吸收率HPLC測定,以wt.%表示。 EGCG,咖啡鹼,其他兒茶素以及掊酸的含量表現於表1。 表1 始材料内茶組份濃度 (請先閱讀背面之注意事項再填寫本頁) 裝 經濟部智慧財產局員工消費合作社印製 化合物 茶萃 實例1 HPLC/wt.-% 茶萃 實例1 相對百分比% 掊酸 0.01 0.02 兒茶素 2.3 3.11 咖啡驗 11.0 15.10 EGCG 38.1 52.34 表兒茶素 5.2 7.11 GCG 6.6 8.99 ECG 9.7 13.35 合計 72· 8 100.00 將粒子大小 0.3 - 1.2 mm 之 AMBERLITE® XAD-7樹脂 33.5 € (26 kg)充填入内徑150 mm,長2 m及容積35.4 €的中間規格 塔中。塔柱設加熱套。樹脂以水徹底洗並以水/異丙醇(體 積比9 : 1 )之混合物平衡。所用裝置與溶劑等使用前經脱氣 並保持於惰性氮氛下。 -9- 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 1293628 A7 B7 五、發明說明(7 ) 已充填的塔保溫60°C,0.4 kg上述綠茶精(表1 )含152.5 g EGCG者溶於1.8 kg之水/異丙醇混合物(體積比9 : 1 )後加入 塔頂。EGCG藉一泵於0.5巴壓力及60X:下以水/異丙醇(體 積比9 : 1 )混合物於怪等流速50 kg/h自塔中洗提。起始洗出 (預先部分)144 kg後收集主要洗出液174 kg含112 g EGCG的 主要多酚組份。主要洗出液中EGCG濃度爲0.064%。起始自 茶精内152.5 g EGCG所分離的EGCG產率爲73.5%。 爲再生樹脂計以78.3 kg之水/異丙醇(體積比4 : 6 )洗提解 吸餘留兒茶素。第二次分離前用86 kg的水/異丙醇(體積比 9 : 1 )混合物以回洗方式於120 kg/h流量調理此塔。 表2例證分離效果由EGCG的相對百分率可見。主洗出液 内茶組份之濃度由HPLC用UV吸收率測定,以wt.-%或ppm 表示。 --------*1 ♦裝· II (請先閱讀背面之注意事項再填寫本頁) 卜丨訂· 經濟部智慧財產局員工消費合作社印製 表2 主洗出液内茶組份的濃度 化合物 主要部分 實例1 HPLC/ppm 相對百分比率% 掊酸 0 0.0 兒茶素 21 3.1 咖讲驗 1 0.2 EGCG 644 92.1 表兒茶素 29 4.2 GCG 3 0.4 ECG 1 0.2 合計 699 100.0 實例2 10- 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 1293628 A7 B7 五、發明說明(8 ) (請先閱讀背面之注意事項再填寫本頁) 用另一批貴州Highyin生物產品公司之’’綠茶精,最少 95 %多酚”重複實例1,其成份如表3所示。 表3 始材料内茶組份濃度 化合物 茶萃 實例2 HPLC/wt.-% 實例2之茶萃 實例2 相對百分比/% 掊酸 <0.1 0.05 兒茶素 1.4 1.94 咖啡驗 13.8 18.89 EGCG 35.1 47.95 表免茶素 3.3 4.47 GCG 8.2 11.20 ECG 11.4 15.49 合計 73.2 100.00 經濟部智慧財產局員工消費合作社印製 實例1洗過之塔保持恆溫60°C,用以進行分離。0.4 kg上 述綠茶萃(表3)含140.5 g純EGCG者溶解於1.8 kg的水/異丙 醇(體積比9 : 1 )混合物,加於塔頂。隨後按實例1説明洗提 。起始洗提200 kg (預先部分)後收集117 kg主要洗出液含 72.8 g之EGCG爲主要多酚組份。主要洗出液内EGCG濃度爲 0.062%。自茶萃内140.5 g EGCG起始分離的EGCG產率爲 51.8%。 爲樹脂再生,以100 kg的水/異丙醇(體積比4 : 6 )混合物 洗提解吸。次一分離步驟前用100 kg水/異丙醇(體積比 9 : 1)混合物以回洗方式於120 kg/h之流速調理此塔。 表4例證分離效果由EGCG的相對百分比表現。主要洗出 液中茶組份濃度用UV吸收率經HPLC測定,以ppm表示。與 -11 - 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 1293628 A7 B7 經濟部智慧財產局員工消費合作社印製 五、發明說明(9 ) 實例1比,獲得較高百分比之EGCG。 表4 主要洗出液内茶組份濃度 化合物 主要部分 實例2 HPLC/ppm 相對百分比/% 掊酸 <0.1 0.01 兒茶素 10 1.49 咖啡驗 1 0.17 EGCG 622 96.53 表兒茶素 2 0.27 GCG 6 0.95 ECG 4 0.57 合計 645 100.00 實例3 洗出物濃度 實例2所述重複作業製備的9008 kg吸收/解吸塔洗出液按 EGCG量計算添加2%檸檬酸使穩定。洗出液於40〇C溫度與55 毫巴壓力用不銹鋼製降膜蒸發器有熱交表面積1.1 m2者濃縮 。接受蒸發單位之進料溶液兒茶素與咖啡驗量列入表5。 表5 接受蒸發的淨化EGCG液内茶組份之濃度 化合物 進料 降膜蒸發器 HPLC/ppm 相對百分比/% 掊酸 0.1 0.01 兒茶素 10 1.30 咖讲驗 1 0.14 EGCG 712 96.20 表兒茶素 7 0.96 GCG 7 0.97 ECG 3 0.41 合計 740 100.00 -12- ---------?--裝--- (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) . 1293628 A7 B7 五、發明說明(10 ) (請先閱讀背面之注意事項再填寫本頁) 調節蒸發器進料流至120-130 kg/h範圍内於循環流速300 kg/h的流量。於是餘出流量爲123.5 kg/h,塔底產物移出率 0.52 kg/h。濃縮過程間第一部分經取樣分析,繼亦分析第 二部分。二部分EGCG濃縮物總量合計63.5 kg。 表6顯現塔底產物内茶組份之濃度。EGCG回收率爲 95.9%。分析結果明白指出溶液濃縮期間能維持分離EGCG 的高純度。 EGCG能自濃液中隨意經噴霧乾燥或藉結晶析離固態。 表6 降膜蒸發器中EGCG濃縮物内茶組份之濃度 化合物 降膜蒸發器: 成分 Ist第一部分 HPLC/wt.-% 相對百分比 t殘留產物 成分 2nd第二部分 HPLC/wt··%相對百分比/% 掊酸 0.00 0.00 0.00 0.00 兒茶素 0.17 1.55 0.14 1.59 咖嗔驗 0.01 0.12 0.02 0.28 EGCG 10.70 95.36 8.07 94.93 表兒茶素 0.16 1.39 0.11 1.24 GCG 0.13 1.14 0.13 1.52 ECG 0.05 0.44 0.04 0.44 合計 11.23 100.00 8.50 100.00 溶液的總質量 39.0 kg 24.5 kg 實例4 經濟部智慧財產局員工消費合作社印製 平均粒子直徑120微米的450 AMBERCHROM® CG-71c 充填入不銹鋼製的實驗室色層分離塔中,塔内徑2.2 cm,長 103 cm,裝有加熱套。樹脂經水/乙醇(體積比9 : 1)洗過並平 衡。 -13 - 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 1293628 A7 B7_ 五、發明說明(11 ) 溶解來自貴州Highyin生物產品公司之20 g濃兒茶素粉” 綠茶精,最少95%多酚”(始材料)於20 水/乙醇(體積比 9 : 1 )混合物。隨後將此液14 g (相當於2.99 g EGCG)加入塔 頂。藉層析泵於2_3巴壓力及60°C溫度下以水/乙醇(體積 比9 : 1 )混合物在16 /分鐘不變流量下洗提EGCG。洗提劑 經脱氣及保持於氮氛下待用。起初洗提2.48 € (預先部分) 後改變流速至25.5 m€ /分鐘,收集5.40,要洗出液含0.627 g/€濃度之EGCG。相對其他兒茶素與咖啡鹼,用HPLC測定 主要洗出液内EGCG的純度表示爲相對百分比97.13%。實驗 期間系統中壓力變動自2至3巴視所施流量而定。表7對照 洗出液與始材料内茶組份之濃度,由是説明分離效果如 EGCG的相對百分比表現。始材料及主要部分中茶組份之 濃度用UV吸收率經HPLC測定並以wt.%或ppm表示。 表7 MBERCHROM CG-71c上分離,60°C,溶劑系統:水/ ---------ΓΙΛ-裝—— (請先閱讀背面之注意事項再填寫本頁) 卜丨訂 經濟部智慧財產局員工消費合作社印製 乙醇 化合物 茶濃縮物 (始材料) 實例4 主要部分 實例4 HPLC wt.-% 相對百分比/% HPLC/ppm 相對百分比/% 掊酸 0.08 0.10 0 0.00 兒茶素 0.50 0.61 1 0.22 咖嗓驗 9.29 11.31 5 1.29 EGCG 42.23 51.41 407 97.13 表兒茶素 4.24 5.17 3 0.78 GCG 8.09 9.85 1 0.20 ECG 17.70 21.55 2 0.38 合計 82.15 100.00 419 100.00 -14- 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 1293628 A7 B7_ 五、發明說明(12) 實例5 (請先閱讀背面之注意事項再填寫本頁) 在一内徑2.4 cm,長100 cm的玻璃製實驗室層析塔中裝 填粒子直徑0.3至1.2 mm之Amberlite® XAD-7 450 ml。塔體裝 有加熱套,底上設多孔玻璃料P3。樹脂以脱離子水徹底清 洗並以水/乙醇(體積比9 : 1 )混合物平衡後使用。 溶解20 g貴州Highyin生物產品公司的濃縮兒茶素粉’’綠茶 精,最少95%多驗(始材料)於20 mf之水/乙醇(體積比9 : 1 ) 混合物。隨後加此液14 g (相當於2.91 g的EGCG)於塔頂。 用水/乙醇(體積比9 : 1 )混合物以不變流速16.9 /分鐘於 60°C溫度及0.5 _ 1巴壓力洗提EGCG。洗提劑使用前經脱氣 並保持在氮氛下。起始洗提2.48 € (預先部分)後改變流速 至23.6 分鐘,收集主要洗出液4.95 £含EGCG濃度0.470 g/,。相關其他主要兒茶素及咖啡鹼,經HPLC測定主要部 分内EGCG之純度爲86.22% (見表8 )。以EGCG基計產率爲 79.8 %。實驗期間系統中壓力變動自0.5至1巴視所用流速 而定。 經濟部智慧財產局員工消費合作社印製 爲再生樹脂起見,以1.35,的水/乙醇(體積比4 : 6 )混合 物於流速22.5 /分鐘洗提解吸餘留兒茶素。此部分亦能 用以進一步提純或分離已解吸之兒茶素。表8比較洗出液 中與始材料内茶組份的濃度,於是例證分離效果如EGCG 之相對百分比所示。始材料中及主要部分内茶組份的濃度 由HPLC用UV吸收率測定並以wt.·%或ppm表示。 -15- 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) " 1293628 A7 B7 五、發明說明(13) 表8在Amberlite® XAD-7上分離,60°C,溶劑系統:水/乙醇 化合物 茶濃縮物 (始材料) 實例5 HPLC/wt.-% 相對百分比/% 主要部分 實例5 HPLC/ppm 相對百分比/% 掊酸 0.09 0.11 0 0.00 兒茶素 0.50 0.62 2 0.32 咖#驗 9.17 11.47 7 1.22 請 先 閱 讀 背 面 之 注Example 1 Separation of EGCG A green tea extract containing different catechins and caffeine (made by Highyin Bioproducts Co., Ltd., Guiyang, China), green tea extract, minimum 95% polyphenols π was used as the starting material. The tea component concentration was determined by UV absorbance HPLC and expressed in wt.%. The contents of EGCG, caffeine, other catechins and citric acid are shown in Table 1. Table 1 Concentration of tea components in the starting materials (please read the notes on the back and then fill out this page) Installed by the Ministry of Economic Affairs, Intellectual Property Bureau, Staff and Consumers Cooperatives, printed compound tea extracts. Example 1 HPLC/wt.-% Tea extract example 1 Relative percentage % decanoic acid 0.01 0.02 catechin 2.3 3.11 Coffee test 11.0 15.10 EGCG 38.1 52.34 Epicatechin 5.2 7.11 GCG 6.6 8.99 ECG 9.7 13.35 Total 72· 8 100.00 AMBERLITE® XAD-7 resin with particle size 0.3 - 1.2 mm 33.5 € (26 kg) is filled into an intermediate specification tower with an inner diameter of 150 mm, a length of 2 m and a volume of 35.4 €. The tower is provided with a heating jacket. The resin was thoroughly washed with water and equilibrated with a mixture of water/isopropanol (volume ratio: 9:1). The device and solvent used are degassed and kept under an inert nitrogen atmosphere before use. -9- This paper scale applies to China National Standard (CNS) A4 specification (210 X 297 mm) 1293628 A7 B7 V. Invention description (7) Filled tower insulation 60 ° C, 0.4 kg of the above green tea essence (Table 1) The 152.5 g EGCG was dissolved in a 1.8 kg water/isopropanol mixture (9:1 by volume) and added to the top of the column. The EGCG was eluted from the column by a pump at a pressure of 0.5 bar and at 60X: with a water/isopropanol (volume ratio of 9:1) at a strange flow rate of 50 kg/h. After the initial washout (pre-part) 144 kg, the main eluate was collected and 174 kg of the main polyphenol component containing 112 g of EGCG. The concentration of EGCG in the main eluate was 0.064%. The EGCG yield isolated from 152.5 g EGCG in tea spirit was 73.5%. The remaining catechins were eluted with 78.3 kg of water/isopropanol (volume ratio 4:6) for the regenerated resin. Prior to the second separation, the column was conditioned at a flow rate of 120 kg/h with a mixture of 86 kg of water/isopropanol (9:1 by volume) in a backwashing manner. Table 2 illustrates that the separation effect is seen by the relative percentage of EGCG. The concentration of the inner tea component in the main eluate is determined by HPLC using UV absorbance, expressed in wt.-% or ppm. --------*1 ♦装· II (Please read the notes on the back and fill out this page) 卜丨定· Ministry of Economic Affairs Intellectual Property Bureau Staff Consumer Cooperatives Printed Table 2 Main Washing Liquid Tea Group Part of the concentration of the compound main part Example 1 HPLC / ppm relative percentage rate % citric acid 0 0.0 catechin 21 3.1 coffee test 1 0.2 EGCG 644 92.1 epicatechin 29 4.2 GCG 3 0.4 ECG 1 0.2 total 699 100.0 Example 2 10 - This paper size applies to China National Standard (CNS) A4 specification (210 X 297 mm) 1293628 A7 B7 V. Invention description (8) (Please read the back note first and then fill in this page) Use another batch of Guizhou Highyin creatures The product company's ''Green tea essence, at least 95% polyphenols' repeated Example 1, the composition of which is shown in Table 3. Table 3 Tea composition concentration in the starting material Compound tea extract Example 2 HPLC/wt.-% Example 2 tea Example 2 Relative Percentage/% Tannic Acid <0.1 0.05 Catechin 1.4 1.94 Coffee Test 13.8 18.89 EGCG 35.1 47.95 Table Free Tea 3.3 4.47 GCG 8.2 11.20 ECG 11.4 15.49 Total 73.2 100.00 Ministry of Economic Affairs Intellectual Property Bureau Staff Consumer Cooperative Printed Example 1 wash The tower is kept at a constant temperature of 60 ° C for separation. 0.4 kg of the above green tea extract (Table 3) containing 140.5 g of pure EGCG dissolved in 1.8 kg of water / isopropanol (9:1 by volume) mixture, added to the tower Top. The elution was then carried out as described in Example 1. After initial elution of 200 kg (pre-part), 117 kg of main eluate was collected containing 72.8 g of EGCG as the main polyphenol component. The concentration of EGCG in the main eluate was 0.062%. The yield of EGCG isolated from the initial extraction of 140.5 g EGCG from the tea extract was 51.8%. For resin regeneration, stripping with 100 kg of water/isopropanol (volume ratio 4:6). Desorption before the next separation step 100 kg of water/isopropanol (9:1 by volume) mixture was conditioned at a flow rate of 120 kg/h in a backwashing manner. Table 4 illustrates the separation effect as a function of the relative percentage of EGCG. The main component of the tea in the eluate The concentration is measured by HPLC using UV absorption, expressed in ppm. -11 - This paper scale applies Chinese National Standard (CNS) A4 specification (210 X 297 mm) 1293628 A7 B7 Ministry of Economic Affairs Intellectual Property Bureau employee consumption cooperative printed five , Invention Description (9) Example 1 ratio, obtaining a higher percentage of EGCG. Table 4 Main tea extract concentration in the main eluate. Example 2 HPLC/ppm Relative percentage/% decanoic acid <0.1 0.01 catechin 10 1.49 Coffee test 1 0.17 EGCG 622 96.53 Epicatechin 2 0.27 GCG 6 0.95 ECG 4 0.57 Total 645 100.00 Example 3 Eluate Concentration The 9008 kg absorption/desorption column eluate prepared by the repeated operation described in Example 2 was stabilized by adding 2% citric acid as calculated by the amount of EGCG. The eluate was concentrated at a temperature of 40 ° C and a pressure of 55 mbar using a stainless steel falling film evaporator with a heat exchange surface area of 1.1 m2. The catechin and coffee samples of the feed solution receiving the evaporation unit are listed in Table 5. Table 5 Concentration of Tea Components in Evaporated Purified EGCG Liquid Compound Feed Falling Film Evaporator HPLC/ppm Relative Percentage/% Tannic Acid 0.1 0.01 Catechin 10 1.30 Coffee Test 1 0.14 EGCG 712 96.20 Epicatechin 7 0.96 GCG 7 0.97 ECG 3 0.41 Total 740 100.00 -12- ---------?----- (Please read the notes on the back and fill out this page) This paper scale applies to Chinese national standards ( CNS)A4 size (210 X 297 mm) . 1293628 A7 B7 V. Description of invention (10) (Please read the note on the back and fill out this page) Adjust the evaporator feed flow to the range of 120-130 kg/h Flow at a circulating flow rate of 300 kg/h. The remaining flow rate is 123.5 kg/h and the bottom product removal rate is 0.52 kg/h. The first part of the concentration process was sampled and analyzed, followed by the second part. The total amount of the two parts of EGCG concentrate is 63.5 kg. Table 6 shows the concentration of the tea component in the bottom product. The EGCG recovery was 95.9%. The results of the analysis clearly indicate that the high purity of the separated EGCG can be maintained during concentration of the solution. EGCG can be spray dried or concentrated by solid state from the dope. Table 6 Concentration of Tea Components in EGCG Concentrate in Falling Film Evaporator Compound Falling Film Evaporator: Composition Ist Part I HPLC/wt.-% Relative Percentage t Residual Product Composition 2nd Part II HPLC/wt··% Relative Percentage /% 掊酸0.00 0.00 0.00 0.00 catechin 0.17 1.55 0.14 1.59 咖嗔0.01 0.12 0.02 0.28 EGCG 10.70 95.36 8.07 94.93 Epicatechin 0.16 1.39 0.11 1.24 GCG 0.13 1.14 0.13 1.52 ECG 0.05 0.44 0.04 0.44 Total 11.23 100.00 8.50 100.00 The total mass of the solution is 39.0 kg 24.5 kg. Example 4 Ministry of Economic Affairs Intellectual Property Office Staff Consumer Cooperatives Printed 450 AMBERCHROM® CG-71c with an average particle diameter of 120 μm Filled into a stainless steel laboratory chromatography column with an inner diameter of 2.2 cm It is 103 cm long and is equipped with a heating jacket. The resin was washed and equilibrated with water/ethanol (9:1 by volume). -13 - This paper size is applicable to China National Standard (CNS) A4 specification (210 X 297 mm) 1293628 A7 B7_ V. Invention description (11) Dissolving 20 g concentrated catechin powder from Guizhou Highyin Bioproducts Co., Ltd. , a mixture of at least 95% polyphenols (starting material) in 20 water/ethanol (9:1 by volume). This solution was then added to the top of the column with 14 g (equivalent to 2.99 g EGCG). The EGCG was eluted by a toluene pump at a pressure of 2_3 bar and at a temperature of 60 ° C with a water/ethanol (9:1 by volume) mixture at a constant flow rate of 16 /min. The eluent is degassed and kept in a nitrogen atmosphere for use. Initially, 2.48 € (pre-part) was added and the flow rate was changed to 25.5 m€ /min, and 5.40 was collected. The eluate had an EGCG concentration of 0.627 g/€. The purity of EGCG in the main eluate was determined by HPLC as a relative percentage of 97.13% relative to other catechins and caffeine. During the experiment, the pressure variation in the system was determined by the flow rate from 2 to 3 Bar. Table 7 compares the concentration of the eluate with the tea component in the starting material, which is a representation of the relative percentage of separation effect such as EGCG. The concentration of the tea component in the starting material and the main portion was determined by HPLC using UV absorption and expressed in wt.% or ppm. Table 7 MBERCHROM CG-71c separation, 60 ° C, solvent system: water / --------- ΓΙΛ - installed - (Please read the back of the note before you fill out this page) Intellectual Property Bureau Staff Consumer Cooperative Printed Ethanol Compound Tea Concentrate (Starting Material) Example 4 Main Section Example 4 HPLC wt.-% Relative Percentage/% HPLC/ppm Relative Percentage/% Niobic Acid 0.08 0.10 0 0.00 Catechin 0.50 0.61 1 0.22 咖嗓9.29 11.31 5 1.29 EGCG 42.23 51.41 407 97.13 Epicatechin 4.24 5.17 3 0.78 GCG 8.09 9.85 1 0.20 ECG 17.70 21.55 2 0.38 Total 82.15 100.00 419 100.00 -14- This paper scale applies to Chinese National Standard (CNS) A4 size (210 X 297 mm) 1293628 A7 B7_ V. Description of invention (12) Example 5 (Please read the note on the back and fill out this page) In a glass laboratory layer with an inner diameter of 2.4 cm and a length of 100 cm The column was filled with Amberlite® XAD-7 450 ml with a particle diameter of 0.3 to 1.2 mm. The tower body is provided with a heating jacket, and a porous frit P3 is arranged on the bottom. The resin was thoroughly washed with deionized water and equilibrated with a water/ethanol (volume ratio of 9:1) mixture. Dissolve 20 g of concentrated catechin powder '' green tea extract of Guizhou Highyin Bioproducts Co., Ltd., at least 95% of the mixture (starting material) in a mixture of 20 mf water/ethanol (9:1 by volume). This solution was then added to 14 g (equivalent to 2.91 g of EGCG) at the top of the column. The EGCG was eluted with a water/ethanol (volume ratio of 9:1) mixture at a constant flow rate of 16.9 / min at a temperature of 60 ° C and a pressure of 0.5 _ 1 bar. The eluent is degassed and kept under nitrogen before use. After the initial elution of 2.48 € (pre-part), the flow rate was changed to 23.6 minutes, and the main eluate was collected at 4.95 £ with an EGCG concentration of 0.470 g/. For other major catechins and caffeine, the purity of EGCG in the main part was determined by HPLC to be 86.22% (see Table 8). The yield based on the EGCG basis was 79.8 %. The pressure variation in the system during the experiment was determined by the flow rate used from 0.5 to 1 bar. Printed by the Intellectual Property Office of the Ministry of Economic Affairs, the Consumer Cooperatives. For the purpose of recycled resin, the remaining catechins were desorbed at a flow rate of 22.5 / min at a water/ethanol (volume ratio of 4:6) of 1.35. This part can also be used to further purify or isolate desorbed catechins. Table 8 compares the concentration of the tea component in the eluate with the starting material, thus exemplifying the separation effect as indicated by the relative percentage of EGCG. The concentration of the tea component in the starting material and in the main portion was determined by HPLC using UV absorbance and expressed in wt.% or ppm. -15- This paper size is applicable to China National Standard (CNS) A4 specification (210 X 297 mm) " 1293628 A7 B7 V. Inventive Note (13) Table 8 is separated on Amberlite® XAD-7, 60 ° C, solvent System: water/ethanol compound tea concentrate (starting material) Example 5 HPLC/wt.-% relative percentage/% Main part Example 5 HPLC/ppm Relative percentage/% decanoic acid 0.09 0.11 0 0.00 catechin 0.50 0.62 2 0.32 Coffee #验9.17 11.47 7 1.22 Please read the note on the back first
EGCG 41.16 51.46 470 86.22 表兒茶素 4.16 5.20 5 0.98EGCG 41.16 51.46 470 86.22 Epicatechin 4.16 5.20 5 0.98
GCG 7.75 9.69 22 3.97GCG 7.75 9.69 22 3.97
ECG 17.16 21.46 40 7.28 合計 79.99 100.00 545 100.00 項赢 再W 填 I裝 頁 實例6 實例5之用生樹脂在實例5内所述實驗室塔中泵汲一水/ 乙醇(體體比9 : 1 )混合物通過樹脂使其平衡。 溶解20 g貴州Highyin生物產品公司的濃兒茶素粉"綠茶 精,最少95%多酚π (始材料)於20 之水/乙醇(體積比 9 : 1 )混合物。隨後將14 g此溶液(相當於3.04 g EGCG)加進 塔頂。洗提EGCG用水/乙醇混合物(體積比9 : 1 )以22.5 / 分鐘不變流速於40°C塔溫及1 - 2巴壓力進行。洗提劑使用 前經脱氣並保持於氮氛下。起始3.60 €洗提(預先部分)後 改變流速至26.3 /分鐘流量,收集主洗提液4.73,。主洗 出液内EGCG濃度爲0.278 g/f。有關其他主兒茶素與咖啡鹼 方面主洗出液内表掊兒茶素掊酸鹽純度經HPLC檢定爲 93.2%。以EGCG基礎計產率爲42.8%。實驗期間系統中壓力 變化自1至2巴視流量而定。 爲再生樹脂計以1.98,水/乙醇(體積比4 : 6 )於流速26.3 -16- 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 訂 經濟部智慧財產局員工消費合作社印製 1293628 A7 B7 五、發明說明(14) /分鐘及40°C溫度洗提解吸。此部分亦能用以進一步提 純或分離解吸之兒茶素。表9比較洗出液中及始材料内茶 組份的濃度,於是説明分離效果如相對百比EGCG所示。 始材料中及主要部分内茶組份濃度係由HPLC用UV吸收率 測定並以wt._%或ppm表示。 表9在Amberlite® XAD-7上分離,40°C,溶劑系統:水/乙醇 茶濃縮物 (始材料) 實例6 請 先 閱 讀 背 面 之 注 意 事 項▲ 再W 填 i j裝 頁 實例6之 主要部分 化合物 HPLC/ppm HPLC/wt.-% 相對百分比/% 相對百分比/% 掊酸 0.08 0.10 0 0.00 兒茶素 0.51 0.61 1.00 9.48 11.33 1.43 訂ECG 17.16 21.46 40 7.28 Total 79.99 100.00 545 100.00 Wins and then W Fills I. Example 6 Raw resin for Example 5 Pumped in a laboratory tower as described in Example 5 Water/Ethanol (body ratio 9:1) The mixture is equilibrated by a resin. Dissolve 20 g of high-quality catechin powder from Guizhou Highyin Bioproducts Co., Ltd., green tea extract, a mixture of at least 95% polyphenol π (starting material) in 20 water/ethanol (9:1 by volume). 14 g of this solution (equivalent to 3.04 g EGCG) was then added to the top of the column. The eluted EGCG water/ethanol mixture (volume ratio 9:1) was carried out at a constant flow rate of 22.5 / min at a column temperature of 40 ° C and a pressure of 1-2 bar. The eluent is degassed and kept under nitrogen before use. After the initial 3.60 € elution (pre-part), change the flow rate to 26.3 / min flow and collect the main eluate 4.73. The concentration of EGCG in the main wash was 0.278 g/f. Regarding other main catechins and caffeine, the purity of the catechin catechol in the main eluate was determined by HPLC to be 93.2%. The yield based on EGCG was 42.8%. The pressure change in the system during the experiment depends on the flow rate of 1 to 2 Bar. For regenerated resin, 1.98, water/ethanol (volume ratio 4:6) at a flow rate of 26.3 -16- This paper scale applies Chinese National Standard (CNS) A4 specification (210 X 297 mm). Co-operative printing 1293628 A7 B7 V. Description of invention (14) / min and 40 ° C temperature elution and desorption. This section can also be used to further purify or separate desorbed catechins. Table 9 compares the concentrations of the tea components in the eluate and in the starting material, thus indicating that the separation effect is as shown by the relative EMIG. The concentration of the tea component in the starting material and in the main portion was determined by HPLC using UV absorbance and expressed in wt.% or ppm. Table 9 Separated on Amberlite® XAD-7, 40 ° C, Solvent System: Water/Ethanol Tea Concentrate (Starting Material) Example 6 Please read the notes on the back ▲ then fill in the main part of the sample of Example 6 HPLC/ppm HPLC/wt.-% Relative Percentage/% Relative Percentage/% Niobic Acid 0.08 0.10 0 0.00 Catechin 0.51 0.61 1.00 9.48 11.33 1.43
EGCG 43.01 51.40 276 93.24 表兒茶素 4.34 5.18 9 3.15EGCG 43.01 51.40 276 93.24 Epicatechin 4.34 5.18 9 3.15
GCG 8.23 9.83 2 0.51GCG 8.23 9.83 2 0.51
ECG 18.03 21.54 2 0.66 合計 83.68 100.00 296 100.00 經濟部智慧財產局員工消費合作社印製 實例7 實例6之再生樹脂以水/異丙醇(體積比9 : 1 )混合物平衡。 溶解20 g貴州Highyin生物產品公司的濃縮兒茶素粉”綠茶 精,最少95%多酚”(始材料)於20 水/異丙醇(體積比 9 : 1 )混合物。隨後加此液14 g(相當於3.21 g EGCG)於塔頂 ,用水/異丙醇(體積比9 : 1 )混合物以不變流速18 /分鐘 於60°C塔溫洗提。使用前將洗提劑脱氣並保持於氮氛下。 起始洗出液1.35,(預先部分)後改變流速至16.5 m/ /分鐘, -17- 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 1293628 A7 B7 五、發明說明(15) 收集主要洗出液2.30 €。主要洗出液内EGCG濃度爲0.998 。相關其他主要兒茶素與咖啡鹼言,主洗出液中表掊兒 茶素掊酸鹽之純度經HPLC測定爲85.7%。以EGCG基礎計產 率爲62.8%。實驗期間系統内壓力變動自1至2巴視所用流 量而定。 爲再生樹脂起見餘留兒茶素用2.03 €的水/異丙醇(體積比 4 : 6 )混合物以16.5 /分鐘流速及40°C溫度洗提解吸。此 部分亦能供解吸的兒茶素作進一步提純或分離用。表10比 較洗出液内與始材料中茶組份濃度,於是説明分離效果如 相對EGCG百分比所示。始材料内及主要部分中茶組份之 濃度由HPLC用UV吸收率測定,並以wt·-%或ppm表示。 表10在Amberlite® XAD-7上分離,60°C,溶劑系統:水/異 丙醇 --------*—#-裝! (請先閱讀背面之注意事項再填寫本頁) 訂 經濟部智慧財產局員工消費合作社印製 化合物 茶濃i (始相 實令 HPLC/wt.-% 德物 -料) V 相對百分比/% 實合丨 主要 HPLC/ppm 17之 部分 相對百分比/% 掊酸 0.05 0.06 0 0.01 兒茶素 0.38 0.44 8 0.69 咖啡驗 9.48 10.82 28 2.39 EGCG 45.42 51.83 998 85.68 表兒茶素 4.38 5.00 16 1.38 GCG 8.80 10.04 35 3.02 ECG 19.12 21.81 80 6.84 合計 87.63 100.00 1165 100.00 癰 -18- 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 1293628 經濟部智慧財產局員工消費合作社印製 A7 B7_ 五、發明說明(16) 實例8 實例7的再生樹脂以水/異丙醇(體積比9 : 1 )混合物平衡。 溶解20 g貴州Highyin生物產品公司的濃縮兒茶素粉”綠 茶精,最少95%多驗”(始材料)於20 水/異丙醇(體積比 9 : 1 )混合物。隨後加此液14 g (相當於3.10 g EGCG)於塔頂 。用水/異丙醇(體積比9 : 1 )混合物以16.9 m€/分鐘之怪流 於40°C塔溫洗提。使用前將洗提劑脱氣並保持於氮氛下。 起始洗出液2.48 /(預先部分)後改變流速至23.66 m€ /分鐘 ,收集主要洗出液4.95,。主要洗出液内EGCG濃度爲0.370 g/,。相關其他主要兒茶素與咖啡鹼言,主要部分内EGCG 之純度經HPLC測定爲86.6%。以EGCG基計產率爲59.2%。 實驗中系統壓力變動自1至2巴視所用流速而定。 爲再生樹脂起見餘留兒茶素用2.03 ^的水/異丙醇(體積 比4 : 6)混合物以16.5 /分鐘流速及40°C溫度洗提解吸。 此部分亦能供解吸之兒茶素作進一步提純或分離用。 表11比較洗出液内與始材料中茶組份濃度,於是説明分 離效果如相對EGCG百分比所示。始材料内及主要部分中 茶組份之濃度由HPLC用UV吸收率測定,並以wt.-%或ppm 表示。 -19- 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) ---------*—I·裝·II (請先閱讀背面之注意事項再填寫本頁) 訂·“ 1293628 A7 B7 五、發明說明(17) 表11 在Amberlite XAD-7上分離,40°C,溶劑系統:水/異丙醇 化合物 茶濃縮物 主要部分 (始材料) 實例8 實例8 HPLC/wt.-% 相對百分比/% HPLC/ppm 相對百分比 掊酸 0.20 0.23 0 0.00 兒茶素 0.49 0.57 4 0.83 咖徘驗 9.21 10.85 6 1.50 EGCG 43.74 51.52 370 86.62 表兒茶素 4.23 4.99 14 3.21 GCG 8.50 10.02 11 2.49 ECG 18.52 21.82 23 5.35 合計 84.91 100.00 428 100.00 請 先 閱 讀 背 之 注ECG 18.03 21.54 2 0.66 Total 83.68 100.00 296 100.00 Ministry of Economic Affairs Intellectual Property Office Staff Consumer Cooperative Printed Example 7 The regenerated resin of Example 6 was equilibrated with a mixture of water/isopropanol (9:1 by volume). Dissolve 20 g of high-concentration catechin powder from Guizhou Highyin Bioproducts, a blend of green tea extract, at least 95% polyphenol (starting material) in 20 water/isopropanol (9:1 by volume). Subsequently, 14 g of this solution (corresponding to 3.21 g of EGCG) was added to the top of the column, and the mixture with water/isopropanol (volume ratio of 9:1) was eluted at a constant flow rate of 18 /min at 60 ° C. The eluent was degassed and kept under nitrogen before use. Start the eluate 1.35, (pre-part) and change the flow rate to 16.5 m / / min, -17- This paper scale applies to the Chinese National Standard (CNS) A4 specification (210 X 297 mm) 1293628 A7 B7 V. Description of the invention (15) Collect the main eluate for 2.30 €. The concentration of EGCG in the main eluate was 0.998. Related to other major catechins and caffeine, the purity of the epicatechin in the main eluate was determined by HPLC to be 85.7%. The yield based on EGCG is 62.8%. The pressure variation in the system during the experiment was determined by the flow rate used by 1 to 2 Bax. For the regenerated resin, the remaining catechins were desorbed with a mixture of 2.03 € water/isopropanol (volume ratio 4:6) at a flow rate of 16.5 /min and a temperature of 40 °C. This part can also be used for further purification or separation of desorbed catechins. Table 10 compares the tea component concentrations in the eluate and in the starting material, thus indicating the separation effect as indicated by the relative EGCG percentage. The concentration of the tea component in the starting material and in the main portion was determined by HPLC using UV absorbance and expressed in wt·-% or ppm. Table 10 Separated on Amberlite® XAD-7, 60 ° C, Solvent System: Water / Isopropyl Alcohol - - * * - # - Pack! (Please read the notes on the back and fill out this page) Ministry of Economic Affairs, Intellectual Property Office, Staff and Consumer Cooperatives, Printing Compound Tea Concentrate i (Initial Phase HPLC/wt.-% German-Material) V Percentage/% Real-time 丨 Major HPLC/ppm 17% relative percentage/% Capric acid 0.05 0.06 0 0.01 catechin 0.38 0.44 8 0.69 Coffee test 9.48 10.82 28 2.39 EGCG 45.42 51.83 998 85.68 Epicatechin 4.38 5.00 16 1.38 GCG 8.80 10.04 35 3.02 ECG 19.12 21.81 80 6.84 Total 87.63 100.00 1165 100.00 痈-18 - This paper scale applies to China National Standard (CNS) A4 specification (210 X 297 mm) 1293628 Ministry of Economic Affairs Intellectual Property Office Staff Consumer Cooperative Printed A7 B7_ V. Invention Description (16) Example 8 Recycled resin of Example 7 in water/ The mixture of isopropanol (9:1 by volume) was equilibrated. Dissolve 20 g of concentrated catechin powder from Guizhou Highyin Bioproducts Co., Ltd. "Green tea essence, at least 95% multiple test" (starting material) in a mixture of 20 water / isopropanol (9:1 by volume). This solution was then added to the top of the column at 14 g (equivalent to 3.10 g EGCG). The water/isopropyl alcohol (volume ratio of 9:1) mixture was eluted at a temperature of 40 ° C in a strange flow of 16.9 m € / min. The eluent was degassed and kept under nitrogen before use. After the initial eluate 2.48 / (pre-part), change the flow rate to 23.66 m € / min and collect the main eluate 4.95. The concentration of EGCG in the main eluate was 0.370 g/. Related to other major catechins and caffeine, the purity of EGCG in the main part was determined by HPLC to be 86.6%. The yield based on the EGCG basis was 59.2%. The system pressure variation during the experiment was determined by the flow rate used from 1 to 2 Bar. For the regenerated resin, the remaining catechin was desorbed with a mixture of 2.03 mmol of water/isopropanol (volume ratio of 4:6) at a flow rate of 16.5 /min and a temperature of 40 °C. This part can also be used for further purification or separation of desorbed catechins. Table 11 compares the tea component concentrations in the eluate with the starting material, thus indicating the separation effect as indicated by the relative EGCG percentage. The concentration of the tea component in the starting material and in the main portion is determined by HPLC using UV absorbance and expressed in wt.-% or ppm. -19- This paper size is applicable to China National Standard (CNS) A4 specification (210 X 297 mm) ---------*—I·Install·II (Please read the notes on the back and fill out this page. )·1293628 A7 B7 V. INSTRUCTIONS (17) Table 11 Separation on Amberlite XAD-7, 40 ° C, Solvent System: Water/Isopropanol Compound Tea Concentrate Main Part (Starting Material) Example 8 Example 8 HPLC/wt.-% Relative Percentage/% HPLC/ppm Relative Percentage Citrate 0.20 0.23 0 0.00 Catechin 0.49 0.57 4 0.83 Curry Verification 9.21 10.85 6 1.50 EGCG 43.74 51.52 370 86.62 Epicatechin 4.23 4.99 14 3.21 GCG 8.50 10.02 11 2.49 ECG 18.52 21.82 23 5.35 Total 84.91 100.00 428 100.00 Please read the back note first
實例9 用有機溶劑在聚醯胺上11分離EGCG 訂 用商品可得之綠茶萃(’’綠茶精,最少95%多酚”中國大陸 貴陽貴州Highyin生物產品公司批號960328)含兒茶素與咖啡 鹼如表12内所示量者作始材料。茶組份的濃度由HPLC用 UV吸收率測定。 經濟部智慧財產局員工消費合作社印製 表12 始材料中茶組份之濃度 化合物 茶萃 HPLC/wt.-% 茶萃 相對百分比/% 掊酸 0.1 0.01 EGC 2.02 2.99 兒茶素 0.78 1.15 咖啡驗 8.48 12.54 EGCG 36.87 54.52 表兒茶素 4.48 6.62 GCG 4.77 7.05 ECG 10.22 15.11 合計 67.63 100.00 -20- 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 1293628 A7 B7 五、發明說明(18 ) 250 g商品可得的聚醯胺11(來源德國Darmstadt默克,目錄 1.07435.0100號)粒子大小5 - 40微米者懸浮在300 醋酸乙 酉旨中,轉移入一内徑5 cm、長3 6 cm之塔内。塔有加熱套裝 置定溫於40°C。溶解3 g起始綠茶精,具表12中特徵,含 1.11 g純EGCG者153 醋酸乙酯,加入塔頂。一醋酸乙酯/ 乙醇梯度洗提〔500 醋酸乙酯,1000 mi醋酸乙酯/乙醇 (8.5 : 1·5 v/v),1000 m 彳醋酸乙酯 / 乙醇(7:3 v/v),2000 m 彳 醋酸乙酯/乙醇(1 : 1 v/v)〕於0.3巴壓力下產生550 的主 要部分,蒸發溶劑後得1.12 g固體含0.87 g EGCG作主要兒 茶素組份。主要洗出液内EGCG濃度爲0.186%。自起始兒茶 素所含1.106§£0€0計算分離£000產率爲76%。 爲樹脂再生計用500 乙醇洗提解吸餘留兒茶素。下次 分離前,以500 醋酸乙酯調整塔。 表13説明分離效果。主要洗出液内組份濃度由HPLC用 UV吸收率測定。 ------- —.—裝— (請先閱讀背面之注意事項再填寫本頁) 纛 經濟部智慧財產局員工消費合作社印製 表13 主要洗出物(蒸發溶劑後)餘留物内茶組份濃度 化合物 主要部分之餘留 HPLC/wt.-% 主要部分之餘留 相對百分比/% 掊酸 0 0 EGC 0 0 兒茶素 0 0 咖#驗 0 0 EGCG 77.4 96.50 表兒茶素 0.05 0.06 GCG 0.74 0.92 ECG 2.07 2.58 合計 80.21 100.00 -21 - 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 8 2 6 3 912 A7B7 五、發明說明(19)Example 9 Separation of EGCG from Polyamide with Organic Solvent 11 Commercial Green Tea Extract (''Green Tea Extract, Minimum 95% Polyphenols') Guiyang Guizhou Highyin Bioproducts Co., Ltd. Batch No. 960328) Contains catechins and caffeine The starting materials are as shown in Table 12. The concentration of the tea components is determined by the UV absorption rate of HPLC. Ministry of Economic Affairs, Intellectual Property Bureau, Staff Consumer Cooperatives, Table 12, Concentration of tea components in the starting materials, compound tea extract HPLC/ Wt.-% relative percentage of tea extract /% decanoic acid 0.1 0.01 EGC 2.02 2.99 catechin 0.78 1.15 coffee test 8.48 12.54 EGCG 36.87 54.52 epicatechin 4.48 6.62 GCG 4.77 7.05 ECG 10.22 15.11 total 67.63 100.00 -20- paper scale Applicable to China National Standard (CNS) A4 specification (210 X 297 mm) 1293628 A7 B7 V. Description of invention (18) 250 g of commercially available polyamido 11 (source German Dermstadt Merck, catalogue 1.07435.0100) particles The size of 5 - 40 microns is suspended in 300 acetic acid, transferred into a tower with an inner diameter of 5 cm and a length of 3 6 cm. The tower has a heating device and a temperature of 40 ° C. Dissolve 3 g of starting green tea. Table 12 characteristics, containing 1.11 g of pure EGCG 153 ethyl acetate, added to the top of the column. Ethyl acetate / ethanol gradient elution [500 ethyl acetate, 1000 mi ethyl acetate / ethanol (8.5: 1 · 5 v / v ), 1000 m 彳 ethyl acetate / ethanol (7:3 v / v), 2000 m 彳 ethyl acetate / ethanol (1 : 1 v / v)] produced a major part of 550 at a pressure of 0.3 bar, after evaporation of the solvent 1.12 g of solids containing 0.87 g of EGCG as the main catechin component. The concentration of EGCG in the main eluate was 0.186%. The calculation of the separation of £000 from the initial catechin was 1.106§£0€0. Desorb the remaining catechins with 500 ethanol for the resin regeneration meter. Adjust the column with 500 ethyl acetate before the next separation. Table 13 shows the separation effect. The concentration of the components in the main eluate is the UV absorption rate by HPLC. ------- -. - Installation - (Please read the notes on the back and fill out this page) 纛 Ministry of Economic Affairs Intellectual Property Bureau Staff Consumer Cooperatives Printed Table 13 Main Eluates (after evaporation of solvents) The main part of the tea component concentration in the residue remains HPLC/wt.-% The remaining part of the main part is relative percentage /% 掊酸0 0 EGC 0 0 Tea 0 0 咖# 验 0 0 EGCG 77.4 96.50 Epicatechin 0.05 0.06 GCG 0.74 0.92 ECG 2.07 2.58 Total 80.21 100.00 -21 - This paper scale applies to Chinese National Standard (CNS) A4 specification (210 X 297 mm) 8 2 6 3 912 A7B7 V. Description of invention (19)
ί^Μ_0在聚醯胺11上用含水混合溶劑分離EGCG 用表1 4所示數量之含兒茶素與咖讲驗的綠茶精水液作始 材料。茶組份之濃度用UV吸收率經HPLC測定,以wt.-%表 7JT 〇 轰J土起始茶精液餘留物内(蒸發溶劑後)茶組份的濃度 化合物 茶萃 HPLC/wt.-% 茶萃 相對百分比/% 掊酸 1.36 4.77 EGC 3.61 12.65 兒茶素 1.45 5.08 咖啡驗 6.89 24.14 EGCG 10.14 35.53 表兒茶素 1.59 5.57 GCG 0.99 3.47 ECG 2.51 8.79 合計 28.54 100.00 懸浮粒子大小5 40微米的聚醯胺11(來源德國Darnstadt默 克,目錄1.07435.0100號)於100 水中,調節pH至6.5。轉 移此懸浮液入一内徑3 cm及長8 cm之塔内。加上述(表14) 含0.078 g純EGCG的綠茶精於塔頂。一水/乙醇梯度洗提〔 500 水,600 水 / 乙醇(7 : 3 v/v),350 水 / 乙醇(6 : 4 v/v),500 水/乙醇(1 : 1 v/v)〕以5 m/ /分鐘之流速產生 110 (0.072 g)的主要部分含0.046 g EGCG。主洗出液中 EGCG濃度爲0.06 %。自茶精内0.078 g EGCG起始分出EGCG 之產率爲59%。 爲再生樹脂計,以500 m,乙醇洗提解吸餘留兒茶素。下 -22- -------- — ΙΓΙ·-裝—— (請先閱讀背面之注意事項再填寫本頁) . 鐮 經濟部智慧財產局員工消費合作社印製 適 度 尺 張 紙 本 21 /V 格 規 A4 S) N (C 準 標 家 釐 公 97 1293628 A7 B7 五、發明說明(2Q ) 次分離前以500 水調理塔。 表15説明分離效果。主洗出液中茶組份濃度經用玎v 吸收率測定。 表11主要部分(蒸發溶劑後)餘留物内茶組份之濃度 化合物 主要部分之餘留 HPLC/wt.-% 主要部分之餘留 相對百分比/% 掊酸 1.10 1.59 EGC 0.00 0.00 兒茶素 1.29 1.86 咖啡驗 0.00 0.00 EGCG 63.53 91.70 表兒茶素 0.00 0.00 GCG 0.16 0.23 ECG 3.20 4.62 合計 69.28 100.00 11 在Amberlite XAD-7上分離EGCG,溶劑系統··水/ 乙醇 將一粒子直徑在〇·3與1.2 mm間之Amberlite XAD-7樹脂416 填充入實驗室色層分離塔内,塔係玻璃製(ECO 25/999 M3V-K,瑞士 Wallisellen,Stagroma AG製),有内徑 2.5 cm及 經濟部智慧財產局員工消費合作社印製 ------裝------ί訂· (請先閱讀背面之注意事項再填寫本頁) 長度100 cm。塔設備加熱套,定溫60°c。樹脂以水/乙醇( 體積比9 : 1 )混合物清洗並平衡。 用購得商品綠茶精(中國大陸浙江杭州浙江中國植物技 術社的π茶多驗TP- 80π含兒茶素及咖啡驗量如表16所示者 作始材料。茶組份濃度經HPLC用UV吸收率測定,以wt··% 表示。 -23- 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 1293628 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明說明(21 ) 表16始材料中茶組份濃度 化合物 實例13之茶萃 HPLC/wt.-% 實例13之茶萃 相對百分比/% 掊酸 0.1 0.1 EGC 8.6 10.1 兒茶素 1.9 2.2 咖啡驗 6.2 7.3 EGCG 40.3 47.4 表兒茶素 10.4 12.2 GCG 0.9 1.1 ECG 16.6 19.5 合計 85.0 100.00 溶解11.2 g表16内所示特徵含4.5 g純EGCG的起始綠茶精 於112.5 脱離子水,加入塔頂。兒茶素用水/乙醇混合物 (體積比9 : 1 )以恆定流速0.6 ^ /小時於60°C塔溫洗提。使用 前洗提劑經脱氣並保持於氮氛下。 起初洗提1.2 €後更改洗提劑成分爲水/乙醇體積比8 : 2。 此洗提總量1.5,產生900 主要部分含2.115 gEGCG。主要 部分中EGCG濃度爲0.245%。起始自茶精内4.5 g EGCG分離 之EGCG產率爲47%。實驗期間系統中壓力變化自0.8至1.5 巴。 爲再生樹脂計繼續以水/乙醇4 : 6體積比混合物洗提,於 是乙醇解吸餘留兒茶素。下次分離前塔以水/乙醇體積比 9 : 1處理。 表17説明分離效果。主要部分的餘留物(蒸發溶劑後)内 茶組份濃度以HPLC用UV吸收率測定,表示爲wt.-%。 -24- 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -------—.--I 裝-------^—訂------- (請先閱讀背面之注意事項再填寫本頁) 1293628 經濟部智慧財產局員工消費合作社印製 A7 B7 五、發明說明(22 ) 表17 主要部分(蒸發溶劑後)餘留物内茶組份濃度 化合物 實例13之主要部分餘留 HPLC/wt.-% 實例13之主要部分餘留 相對百分比/% 掊酸 0 0 EGC 0 0 兒茶素 0.6 0.7 咖啡驗 0.3 0.3 EGCG 81.4 94.5 表兒茶素 1.7 2.0 GCG 0.2 0.2 ECG 1.9 2.2 合計 86.1 100.00 -25- ---------,---裝-------- 丨訂------- (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐)ί^Μ_0 Separation of EGCG from a polyamine 11 using an aqueous mixed solvent The starting amount of the catechin-containing and green tea aqueous solution shown in Table 14 was used. The concentration of the tea component was determined by HPLC using UV absorption rate, and the concentration of the tea component in the residue of the tea semen (after evaporation of the solvent) was determined by wt.-% Table 7JT 〇 J J soil compound tea extract HPLC/wt.- % Percentage of tea extract /% Citrate 1.36 4.77 EGC 3.61 12.65 Catechin 1.45 5.08 Coffee test 6.89 24.14 EGCG 10.14 35.53 Epicatechin 1.59 5.57 GCG 0.99 3.47 ECG 2.51 8.79 Total 28.54 100.00 Suspended particle size 5 40 μm polyp Amine 11 (sourced from Dernstadt, Germany, catalogue 1.07435.0100) was adjusted to pH 6.5 in 100 water. Transfer the suspension into a tower with an inner diameter of 3 cm and a length of 8 cm. Add the above (Table 14) green tea extract containing 0.078 g of pure EGCG to the top of the column. One water / ethanol gradient elution [500 water, 600 water / ethanol (7: 3 v / v), 350 water / ethanol (6: 4 v / v), 500 water / ethanol (1: 1 v / v)] A major fraction of 110 (0.072 g) was produced at a flow rate of 5 m/min with 0.046 g EGCG. The concentration of EGCG in the main eluate was 0.06%. The yield of EGCG from the start of 0.078 g of EGCG in the tea extract was 59%. For the regenerated resin, the remaining catechins were desorbed by washing with 500 m of ethanol.下-22- -------- — ΙΓΙ·-装- (Please read the notes on the back and fill out this page). 镰Ministry of Economic Affairs, Intellectual Property Bureau, Staff and Consumer Cooperatives, Print a Moderate Ruler Paper 21 /V Grid A4 S) N (C standard standard PCT 97 1293628 A7 B7 V. Invention description (2Q) 500 water conditioning tower before separation. Table 15 shows the separation effect. The concentration of tea component in the main washing liquid It is determined by the absorption rate of 玎v. Table 11 The main part (after evaporating the solvent) The concentration of the tea component in the residue The remainder of the main part of the compound remains HPLC/wt.-% The remaining percentage of the main part is %/% 掊酸1.10 1.59 EGC 0.00 0.00 catechin 1.29 1.86 Coffee test 0.00 0.00 EGCG 63.53 91.70 Epicatechin 0.00 0.00 GCG 0.16 0.23 ECG 3.20 4.62 Total 69.28 100.00 11 Separate EGCG from Amberlite XAD-7, solvent system · water / ethanol will Amberlite XAD-7 resin 416 with a particle diameter between 〇·3 and 1.2 mm is packed into a laboratory chromatography column, made of glass (ECO 25/999 M3V-K, manufactured by Wallisellen, Switzerland, Stagroma AG). 2.5 cm in diameter and the Intellectual Property Officer of the Ministry of Economic Affairs Printed by consumer cooperatives ------Package ------ 订 · · (Please read the note on the back and fill in this page) Length 100 cm. Tower heating set, constant temperature 60 ° C. Resin The water/ethanol (9:1 by volume) mixture was washed and balanced. The commercially available green tea extract (Chinese Phyto-Zhejiang-Zhejiang-Zhejiang-Zhejiang Chinese Plant Technology Co., Ltd. π-tea multi-test TP-80π-containing catechin and coffee test as shown in Table 16 The materials shown are the starting materials. The tea component concentration is determined by UV absorption rate by HPLC and expressed in wt··%. -23- The paper scale is applicable to China National Standard (CNS) A4 specification (210 X 297 mm) 1293628 Economy Ministry of Intellectual Property Bureau Staff Consumer Cooperative Printed A7 B7 V. Invention Description (21) Table 16 Tea Composition Concentration Compound Example 13 Tea Extract HPLC/wt.-% Example 13 Tea Extract Relative Percentage /% Tannin 0.1 0.1 EGC 8.6 10.1 catechin 1.9 2.2 Coffee 6.2 7.3 EGCG 40.3 47.4 Epicatechin 10.4 12.2 GCG 0.9 1.1 ECG 16.6 19.5 Total 85.0 100.00 Dissolved 11.2 g The characteristics shown in Table 16 contain 4.5 g of pure EGCG starting green tea Finer than 112.5, from the water, join the top of the tower. The catechin water/ethanol mixture (volume ratio 9:1) was eluted at a constant flow rate of 0.6 ^ / hr at 60 ° C. The eluent is degassed and kept under nitrogen before use. After the initial stripping of 1.2 €, the composition of the eluent was changed to a water/ethanol volume ratio of 8:2. The total amount of this elution was 1.5, resulting in a major portion of 900 containing 2.15 g of EGCG. The concentration of EGCG in the main part was 0.245%. The EGCG yield starting from 4.5 g of EGCG in tea spirit was 47%. The pressure in the system varied from 0.8 to 1.5 bar during the experiment. The mixture was again eluted with a water/ethanol 4:6 volume ratio mixture for the regenerated resin, and the ethanol was then desorbed from the remaining catechins. The tower was treated with a water/ethanol volume ratio of 9:1 before the next separation. Table 17 illustrates the separation effect. The concentration of the tea component in the remainder of the main portion (after evaporation of the solvent) was determined by HPLC using UV absorbance and expressed as wt.-%. -24- This paper size is applicable to China National Standard (CNS) A4 specification (210 X 297 mm) --------.--I--------^------ -- (Please read the notes on the back and fill out this page) 1293628 Ministry of Economic Affairs Intellectual Property Office Staff Consumer Cooperatives Print A7 B7 V. Inventions (22) Table 17 Main part (after evaporation of solvent) Residual tea group Part of the concentration of the compound Example 13 Remaining HPLC/wt.-% The main part of Example 13 Residual relative percentage /% Citrate 0 0 EGC 0 0 Catechin 0.6 0.7 Coffee test 0.3 0.3 EGCG 81.4 94.5 Epicatechin 1.7 2.0 GCG 0.2 0.2 ECG 1.9 2.2 Total 86.1 100.00 -25- ---------,---装-------- -定------- (Please read the back first Note on this page. This paper size applies to the Chinese National Standard (CNS) A4 specification (210 X 297 mm).
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