WO2014081275A1 - A method for isolating shikimic acid from oil palm waste - Google Patents
A method for isolating shikimic acid from oil palm waste Download PDFInfo
- Publication number
- WO2014081275A1 WO2014081275A1 PCT/MY2013/000190 MY2013000190W WO2014081275A1 WO 2014081275 A1 WO2014081275 A1 WO 2014081275A1 MY 2013000190 W MY2013000190 W MY 2013000190W WO 2014081275 A1 WO2014081275 A1 WO 2014081275A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- acid
- oil palm
- caffeoylshikimic
- waste material
- shikimic acid
- Prior art date
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- JXOHGGNKMLTUBP-HSUXUTPPSA-N shikimic acid Chemical compound O[C@@H]1CC(C(O)=O)=C[C@@H](O)[C@H]1O JXOHGGNKMLTUBP-HSUXUTPPSA-N 0.000 title claims abstract description 88
- JXOHGGNKMLTUBP-JKUQZMGJSA-N shikimic acid Natural products O[C@@H]1CC(C(O)=O)=C[C@H](O)[C@@H]1O JXOHGGNKMLTUBP-JKUQZMGJSA-N 0.000 title claims abstract description 88
- 238000000034 method Methods 0.000 title claims abstract description 87
- 235000001950 Elaeis guineensis Nutrition 0.000 title claims abstract description 58
- 239000002699 waste material Substances 0.000 title claims abstract description 43
- 240000003133 Elaeis guineensis Species 0.000 title 1
- MRDAXWGGWWDUKL-VKJPNVGWSA-N 3-O-Caffeoylshikimic acid Chemical class O[C@H]1[C@H](O)CC(C(O)=O)=C[C@H]1OC(=O)\C=C\C1=CC=C(O)C(O)=C1 MRDAXWGGWWDUKL-VKJPNVGWSA-N 0.000 claims abstract description 79
- 241000512897 Elaeis Species 0.000 claims abstract description 58
- 239000011347 resin Substances 0.000 claims abstract description 33
- 229920005989 resin Polymers 0.000 claims abstract description 33
- 238000001179 sorption measurement Methods 0.000 claims abstract description 26
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 22
- 239000003463 adsorbent Substances 0.000 claims abstract description 20
- 230000007062 hydrolysis Effects 0.000 claims abstract description 19
- 239000012071 phase Substances 0.000 claims description 39
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 38
- 239000008346 aqueous phase Substances 0.000 claims description 32
- 239000000284 extract Substances 0.000 claims description 23
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 22
- 239000010802 sludge Substances 0.000 claims description 18
- 239000006228 supernatant Substances 0.000 claims description 18
- 239000000203 mixture Substances 0.000 claims description 15
- 239000002904 solvent Substances 0.000 claims description 15
- 239000000463 material Substances 0.000 claims description 13
- 150000001875 compounds Chemical class 0.000 claims description 12
- 239000000377 silicon dioxide Substances 0.000 claims description 11
- SHRMTKTUPUSTHH-UHFFFAOYSA-N 5-O-caffeoylshikimic acid Natural products OC1C=C(O)CC(OC(=O)C=Cc2ccc(O)c(O)c2)C1O SHRMTKTUPUSTHH-UHFFFAOYSA-N 0.000 claims description 10
- 239000007864 aqueous solution Substances 0.000 claims description 9
- 239000010808 liquid waste Substances 0.000 claims description 7
- MRDAXWGGWWDUKL-NFAWXSAZSA-N 3-O-caffeoylshikimic acid Natural products O[C@@H]1CC(=C[C@@H](OC(=O)C=Cc2ccc(O)c(O)c2)[C@H]1O)C(=O)O MRDAXWGGWWDUKL-NFAWXSAZSA-N 0.000 claims description 6
- 125000003118 aryl group Chemical group 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 6
- 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 claims description 5
- VTURJKQJEXSKNY-GDDAOPKQSA-N 4-O-Caffeoylshikimic acid Chemical compound O[C@@H]1CC(C(O)=O)=C[C@@H](O)[C@H]1OC(=O)\C=C\C1=CC=C(O)C(O)=C1 VTURJKQJEXSKNY-GDDAOPKQSA-N 0.000 claims description 5
- VTURJKQJEXSKNY-UHFFFAOYSA-N 4-trans-caffeoylshikimic acid Natural products OC1CC(C(O)=O)=CC(O)C1OC(=O)C=CC1=CC=C(O)C(O)=C1 VTURJKQJEXSKNY-UHFFFAOYSA-N 0.000 claims description 5
- 238000005516 engineering process Methods 0.000 claims description 5
- 239000003456 ion exchange resin Substances 0.000 claims description 5
- 229920003303 ion-exchange polymer Polymers 0.000 claims description 5
- 239000002910 solid waste Substances 0.000 claims description 5
- 238000004185 countercurrent chromatography Methods 0.000 claims description 3
- 230000002209 hydrophobic effect Effects 0.000 claims description 3
- 238000005406 washing Methods 0.000 claims description 3
- 239000003960 organic solvent Substances 0.000 claims description 2
- 239000007790 solid phase Substances 0.000 claims description 2
- 238000000746 purification Methods 0.000 abstract description 13
- 238000011084 recovery Methods 0.000 abstract description 6
- 235000019482 Palm oil Nutrition 0.000 description 20
- 239000002540 palm oil Substances 0.000 description 20
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 18
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 18
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 12
- 238000000926 separation method Methods 0.000 description 10
- 239000000469 ethanolic extract Substances 0.000 description 9
- 239000000243 solution Substances 0.000 description 9
- QAIPRVGONGVQAS-DUXPYHPUSA-N trans-caffeic acid Chemical compound OC(=O)\C=C\C1=CC=C(O)C(O)=C1 QAIPRVGONGVQAS-DUXPYHPUSA-N 0.000 description 9
- 239000000413 hydrolysate Substances 0.000 description 8
- GBMDVOWEEQVZKZ-UHFFFAOYSA-N methanol;hydrate Chemical compound O.OC GBMDVOWEEQVZKZ-UHFFFAOYSA-N 0.000 description 8
- 235000013824 polyphenols Nutrition 0.000 description 8
- 239000006227 byproduct Substances 0.000 description 7
- 235000013399 edible fruits Nutrition 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 7
- YQUVCSBJEUQKSH-UHFFFAOYSA-N 3,4-dihydroxybenzoic acid Chemical compound OC(=O)C1=CC=C(O)C(O)=C1 YQUVCSBJEUQKSH-UHFFFAOYSA-N 0.000 description 6
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 6
- XNEFHYFPRJBTJF-UHFFFAOYSA-N Dehydroshikimic acid Chemical compound OC1C=C(C(O)=O)CC(=O)C1O XNEFHYFPRJBTJF-UHFFFAOYSA-N 0.000 description 6
- 241000196324 Embryophyta Species 0.000 description 6
- 239000000061 acid fraction Substances 0.000 description 6
- 239000012528 membrane Substances 0.000 description 6
- 238000003801 milling Methods 0.000 description 6
- FJKROLUGYXJWQN-UHFFFAOYSA-N 4-hydroxybenzoic acid Chemical compound OC(=O)C1=CC=C(O)C=C1 FJKROLUGYXJWQN-UHFFFAOYSA-N 0.000 description 5
- 238000004811 liquid chromatography Methods 0.000 description 5
- PGZUMBJQJWIWGJ-ONAKXNSWSA-N oseltamivir phosphate Chemical compound OP(O)(O)=O.CCOC(=O)C1=C[C@@H](OC(CC)CC)[C@H](NC(C)=O)[C@@H](N)C1 PGZUMBJQJWIWGJ-ONAKXNSWSA-N 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 229940061367 tamiflu Drugs 0.000 description 5
- ACEAELOMUCBPJP-UHFFFAOYSA-N (E)-3,4,5-trihydroxycinnamic acid Natural products OC(=O)C=CC1=CC(O)=C(O)C(O)=C1 ACEAELOMUCBPJP-UHFFFAOYSA-N 0.000 description 4
- QMPHZIPNNJOWQI-GDDAOPKQSA-N 5-[(E)-caffeoyl]shikimic acid Chemical compound O[C@@H]1[C@H](O)C=C(C(O)=O)C[C@H]1OC(=O)\C=C\C1=CC=C(O)C(O)=C1 QMPHZIPNNJOWQI-GDDAOPKQSA-N 0.000 description 4
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- 240000007232 Illicium verum Species 0.000 description 4
- 235000008227 Illicium verum Nutrition 0.000 description 4
- QMPHZIPNNJOWQI-UMVBOHGHSA-N NP-000588 Natural products O[C@@H]1C=C(C[C@@H](OC(=O)C=Cc2ccc(O)c(O)c2)[C@@H]1O)C(=O)O QMPHZIPNNJOWQI-UMVBOHGHSA-N 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- 235000004883 caffeic acid Nutrition 0.000 description 4
- 229940074360 caffeic acid Drugs 0.000 description 4
- QAIPRVGONGVQAS-UHFFFAOYSA-N cis-caffeic acid Natural products OC(=O)C=CC1=CC=C(O)C(O)=C1 QAIPRVGONGVQAS-UHFFFAOYSA-N 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 238000010828 elution Methods 0.000 description 4
- 230000014759 maintenance of location Effects 0.000 description 4
- 239000002243 precursor Substances 0.000 description 4
- 238000001228 spectrum Methods 0.000 description 4
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 238000001819 mass spectrum Methods 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 150000007965 phenolic acids Chemical class 0.000 description 3
- 229940090248 4-hydroxybenzoic acid Drugs 0.000 description 2
- 241000588724 Escherichia coli Species 0.000 description 2
- 101000610640 Homo sapiens U4/U6 small nuclear ribonucleoprotein Prp3 Proteins 0.000 description 2
- JUUBCHWRXWPFFH-UHFFFAOYSA-N Hydroxytyrosol Chemical compound OCCC1=CC=C(O)C(O)=C1 JUUBCHWRXWPFFH-UHFFFAOYSA-N 0.000 description 2
- 208000002979 Influenza in Birds Diseases 0.000 description 2
- 101001110823 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) 60S ribosomal protein L6-A Proteins 0.000 description 2
- 101000712176 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) 60S ribosomal protein L6-B Proteins 0.000 description 2
- 102100040374 U4/U6 small nuclear ribonucleoprotein Prp3 Human genes 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000003957 anion exchange resin Substances 0.000 description 2
- 125000000129 anionic group Chemical group 0.000 description 2
- -1 aromatic amino acids Chemical class 0.000 description 2
- 206010064097 avian influenza Diseases 0.000 description 2
- 239000002585 base Substances 0.000 description 2
- 239000003637 basic solution Substances 0.000 description 2
- 238000010908 decantation Methods 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
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- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 238000011031 large-scale manufacturing process Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 235000009048 phenolic acids Nutrition 0.000 description 2
- 239000011877 solvent mixture Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 241000588923 Citrobacter Species 0.000 description 1
- 235000001942 Elaeis Nutrition 0.000 description 1
- 239000005562 Glyphosate Substances 0.000 description 1
- 244000188472 Ilex paraguariensis Species 0.000 description 1
- 235000003368 Ilex paraguariensis Nutrition 0.000 description 1
- COLNVLDHVKWLRT-QMMMGPOBSA-N L-phenylalanine Chemical compound OC(=O)[C@@H](N)CC1=CC=CC=C1 COLNVLDHVKWLRT-QMMMGPOBSA-N 0.000 description 1
- QIVBCDIJIAJPQS-VIFPVBQESA-N L-tryptophane Chemical compound C1=CC=C2C(C[C@H](N)C(O)=O)=CNC2=C1 QIVBCDIJIAJPQS-VIFPVBQESA-N 0.000 description 1
- OUYCCCASQSFEME-QMMMGPOBSA-N L-tyrosine Chemical compound OC(=O)[C@@H](N)CC1=CC=C(O)C=C1 OUYCCCASQSFEME-QMMMGPOBSA-N 0.000 description 1
- 240000004760 Pimpinella anisum Species 0.000 description 1
- 235000012550 Pimpinella anisum Nutrition 0.000 description 1
- QIVBCDIJIAJPQS-UHFFFAOYSA-N Tryptophan Natural products C1=CC=C2C(CC(N)C(O)=O)=CNC2=C1 QIVBCDIJIAJPQS-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 229930013930 alkaloid Natural products 0.000 description 1
- 238000005349 anion exchange Methods 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 125000002843 carboxylic acid group Chemical group 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
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- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 1
- 229930003935 flavonoid Natural products 0.000 description 1
- 150000002215 flavonoids Chemical class 0.000 description 1
- 235000017173 flavonoids Nutrition 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 210000000540 fraction c Anatomy 0.000 description 1
- 238000004108 freeze drying Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- XDDAORKBJWWYJS-UHFFFAOYSA-N glyphosate Chemical compound OC(=O)CNCP(O)(O)=O XDDAORKBJWWYJS-UHFFFAOYSA-N 0.000 description 1
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- 235000003248 hydroxytyrosol Nutrition 0.000 description 1
- 229940095066 hydroxytyrosol Drugs 0.000 description 1
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- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
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- 239000002245 particle Substances 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- COLNVLDHVKWLRT-UHFFFAOYSA-N phenylalanine Natural products OC(=O)C(N)CC1=CC=CC=C1 COLNVLDHVKWLRT-UHFFFAOYSA-N 0.000 description 1
- 229930015704 phenylpropanoid Natural products 0.000 description 1
- 125000001474 phenylpropanoid group Chemical group 0.000 description 1
- 235000017807 phytochemicals Nutrition 0.000 description 1
- 229930000223 plant secondary metabolite Natural products 0.000 description 1
- 239000002798 polar solvent Substances 0.000 description 1
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- 238000002953 preparative HPLC Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 150000003364 shikimic acids Chemical class 0.000 description 1
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- OUYCCCASQSFEME-UHFFFAOYSA-N tyrosine Natural products OC(=O)C(N)CC1=CC=C(O)C=C1 OUYCCCASQSFEME-UHFFFAOYSA-N 0.000 description 1
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/09—Preparation of carboxylic acids or their salts, halides or anhydrides from carboxylic acid esters or lactones
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
- C07C51/47—Separation; Purification; Stabilisation; Use of additives by solid-liquid treatment; by chemisorption
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2601/00—Systems containing only non-condensed rings
- C07C2601/12—Systems containing only non-condensed rings with a six-membered ring
- C07C2601/16—Systems containing only non-condensed rings with a six-membered ring the ring being unsaturated
Definitions
- the present invention relates to a method for isolating shikimic acid from oil palm waste. More particularly, the present invention relates to a method for isolating shikimic acid from oil palm waste using resin adsorption and hydrolysis techniques.
- Shikimic acid is a white crystalline compound of non-nitrogenous acid found naturally in plants. It has two kinds of functional group in the same molecule, i.e. three hydroxyl groups and a carboxylic acid group, which are optically active. In its anionic form, shikimic acid is known as shikimate. Shikimate is an important intermediate compound of the "shikimate pathway" in plants and microorganisms. Further, shikimate is the principal precursor for the synthesis of aromatic amino acids, phenylalanine, tryptophan and tyrosine and other compounds such as alkaloids, phenolics and phenyl propanoids.
- EP1092766 A1 discloses a method of using microorganism belonging to the genus Citrobacter to produce shikimic acid.
- the method includes the steps of contacting a solution containing shikimic acid with a basic anion exchange resin to adsorb the shikimic acid and eluting the shikimic acid with an aqueous basic solution to thereby purify the shikimic acid.
- CN1931823 discloses a process of extracting and separating shikimic acid from aniseed.
- the process involves water extraction to obtain an extracted solution.
- the extracted solution is then subjected to an anionic resin column and eluting with sodium hydroxide solution containing the shikimic acid.
- the solution containing the shikimic acid is desalted in a cationic resin column, concentrated and crystallized in acetone to obtain shikimic acid crystal.
- Shikimic acid can be purified using different purification methods.
- JP 2001- 026567 and WO 2001/068891 A1 both disclose a method of purifying shikimic acid by treating a solution containing shikimic acid with an alkali and adsorbing the shikimic acid by an anion exchange resin.
- Oil palm phenolics also contain numerous phenolic acids such as caffeic acid, protocatechuic acid and p-hydroxybenzoic acid.
- the major contributors to the total phenolics are caffeoylshikimic acid at 10,800 ⁇ 2400 mg/kg, followed by p-hydroxybenzoic acid at 7000 ⁇ 1000 mg/kg.
- Phenolic or caffeoylshikimic acid can be extracted from plants using various methods.
- US Patent no. 7,387,802 discloses a method for extracting phytochemical such as flavonoids, phenolic acids and hydroxyl acids from palm oil milling effluents using membrane filter.
- WO 2010/137943A1 discloses a method of extracting caffeoylshikimic acid, protocatechuic acid, hydroxytyrosol and hydroxybenzoic acid from parts of an oil palm including, but are not confined to, vegetation liquor of palm oil milling and palm oil mill effluent, using solid phase extraction approach, followed by semi-preparative high performance liquid chromatography for purification.
- WO 2011/159144 A1 discloses a method of producing shikimic acid from palm-based waste materials and by-products by purifying shikimic acid from extracts comprising oil palm phenolics, using standard purification methods.
- the extracts are obtained by pretreating the oil palm with glyphosate and subjecting the extracts to separation using different types of membranes.
- a first advantage of the method in accordance with embodiments of this invention is that the method provides good recovery of shikimic acid using resin adsorption and hydrolysis techniques in the method.
- a second advantage of the method in accordance with embodiments of this invention is that the method enabled the shikimic acid obtained by the method of the present invention to be purified using simple purification process.
- a third advantage of the method in accordance with embodiments of this invention is that the simplified purification process enables the method of the present invention to be suitable for use in large scale production of shikimic acid.
- a method for isolating shikimic acid from oil palm waste material comprises the steps of (i) providing an oil palm waste material; (ii) passing the oil palm waste material through an adsorption resin to obtain an adsorbent containing caffeoylshikimic acid isomers; (iii) washing the adsorbent containing the caffeoylshikimic acid isomers using water; (iv) eluting unwanted polar compounds adsorbed on the adsorbent using a mixture containing water and solvent; (v) recovering caffeoylshikimic acid isomers in a single fraction using a mixture containing water and solvent; (vi) subjecting the single fraction to hydrolysis to obtain shikimic acid; and (vii) purifying the shikimic acid.
- the method further comprises centrifuging the oil palm waste material to obtain a supernatant and a solid prior to the step of passing the oil palm waste material through the adsorption resin; and subjecting the supernatant to resin or solid phase adsorption to obtain an adsorbent containing caffeoylshikimic acid isomers.
- the oil palm waste material is selected from the group comprising a liquid waste material such as separator sludge and aqueous phase of post-3-phase decanter.
- the method further comprises contacting the oil palm waste material with at least one member selected from the group consisting of water, an organic solvent or a mixture thereof to obtain an extract prior to the step of passing the oil palm waste material through an adsorption resin.
- the oil palm waste material is selected from the group comprising a solid waste material such as oil palm frond, rachis and decanter cake.
- the caffeoylshikimic acid isomers are 3-O-caffeoylshikimic acid, 4-O-caffeoylshikimic acid, and 5-0- caffeoylshikimic acid.
- the single fraction is hydrolyzed using alkaline water, alkaline watersolvent mixtures or an alkaline aqueous solution. In accordance with one embodiment of this invention, the single fraction is hydrolyzed using an alkaline aqueous solution.
- the method further comprises concentrating the single fraction containing the caffeoylshikimic acid isomers prior to the step of subjecting the single fraction to hydrolysis to obtain the shikimic acid.
- the supernatant and the adsorption resin is in a ratio of 1 :1 to 10:1.
- the shikimic acid is purified using any one of the methods selected from the group consisting of ion exchange resin, reversed phase silica, simulated moving bed technology and countercurrent chromatography.
- a shikimic acid isolated from oil palm waste material by the method in accordance with the invention is provided.
- Figure 1 shows the results of a separator sludge analysed by HPLC-LTQ- Orbitrap.
- Figure 1A shows the total ion chromatogram (TIC) of the separator sludge
- Figure 1 B shows a chromatogram at m/z 335
- Figure 1C shows the spectra at 9.27 min
- Figure 1D shows the spectra at 9.73 min
- Figure 1E shows the spectra at 10.77 min.
- Figure 2 shows the results of a decanter cake analysed by HPLC-LTQ-Orbitrap.
- Figure 2A shows the TIC of the decanter cake; and
- Figure 2B shows a chromatogram at m/z 335.
- Figure 3 shows the results of an aqueous phase of post 3-phase decanter analysed by HPLC-LTQ-Orbitrap.
- Figure 3A shows the TIC of the aqueous phase of post 3-phase decanter; and
- Figure 3B shows a chromatogram at m/z 335.
- Figure 4 shows the results of ethanolic and water extracts of oil palm frond analysed by HPLC-LTQ-Orbitrap.
- Figure 4A shows the TIC of the ethanolic extract
- Figure 4B shows a chromatogram of the ethanolic extract at m/z 335
- Figure 4C shows the TIC of the water extract
- Figure 4D shows a chromatogram of the water extract at m/z 335.
- Figure 5 shows the results of an ethanolic and water extracts of oil palm rachis analysed by HPLC-LTQ-Orbitrap.
- Figure 5A shows the TIC of the ethanolic extract
- Figure 5B shows a chromatogram of the ethanolic extract at m/z 335
- Figure 5C shows the TIC of the water extract
- Figure 5D shows a chromatogram of the water extract at m/z 335.
- Figure 6 shows the HPLC-PDA chromatograms of an aqueous phase of post 3- phase decanter at wavelength 327 to 329.
- Figure 6A shows a chromatogram of Fraction C
- Figure 6B shows a chromatogram of Fraction D.
- Figure 7 shows the total amount of caffeoylshikimic acid isomers (measured in ppm) present in different fractions as compared to that of an original aqueous phase of post 3-phase decanter before separation.
- Figure 8 shows the maximum plot of HPLC-PDA of fractions D and E.
- Figure 8A is Fraction D and 8B is Fraction E.
- Figure 9 shows the amount of shikimic acid (measured in ppm) during hydrolysis reaction.
- Figure 10 shows the chromatograms of an aqueous phase of post 3-phase decanter (Figure 10A) enriched caffeoylshikimic acid isomers fraction before (Figure 10B) and after hydrolysis (Figure 10C).
- Palm oil is derived from fleshy mesocarp of the fruit of oil palm (Elaeis guinenensis). Oil palm industry has been recognized for its contribution towards economic growth and rapid development. However, it has also contributed to environmental pollution due to the production of huge quantities of by-products.
- the present invention relates to a method for isolating shikimic acid from byproducts or waste materials derived from the palm oil industry.
- the by-products or waste materials produced in the palm oil industry include, but are not limited to, oil palm trunk, oil palm fronds, empty fruit bunches, palm pressed fibres, palm kernel shells, palm kernel cake, and palm oil mill effluent.
- the by-products or waste materials derived from oil palm fruit in a palm oil mill may be obtained from any stage of the palm oil milling process and also the waste materials may be obtained from the oil palm estate itself.
- the waste materials include, but are not limited to, solid waste materials such as oil palm frond, rachis and decanter cake; and liquid waste materials such as separator sludge (centrifuged sludge) and aqueous phase of post 3-phase decanter.
- decanter cake refers to a by-product obtained from palm oil milling decantation process.
- separator sludge or “centrifuged sludge” as used herein refers to a sludge obtained directly from a centrifuging decanter, a centrifuging separator and/or a 2-phase decanter of a palm oil mill without undergoing any pretreatment or solid-liquid separation.
- aqueous phase of post 3-phase decanter refers to an aqueous phase of a by-product produced in a palm oil milling decantation process.
- the method in accordance with this invention comprises the steps of passing a waste material derivable from oil palm fruit in a palm oil mill (or an oil palm mill waste material) through an adsorption resin to obtain an adsorbent containing caffeoylshikimic acid isomers.
- the resin for use in this invention can be any hydrophobic resin, such as an aromatic or modified aromatic resin, for example, sepabeads® and diaion®, or reversed phase silica, such as C18 derivatized silica.
- the caffeoylshikimic acid isomers are 3-O-caffeoylshikimic acid, 4-O-caffeoylshikimic acid, and 5-O-caffeoylshikimic acid (dactylific acid).
- the method of the present invention can be applied to reconstituted aqueous solutions of other waste materials from oil palm mills which contain caffeoylshikimic acid isomers.
- the waste material is an aqueous phase of post 3-phase decanter.
- the waste material is a separator sludge.
- the adsorbent containing the caffeoylshikimic acid isomers is washed and eluted to remove unwanted polar compounds adsorbed on the adsorbent.
- the adsorbent can be washed and eluted with water and/or watersolvent mixture in a ratio from 100:0 to 50:50, depending on the type of adsorbent used.
- the solvent suitable for use in this invention includes, but is not limited to, any one of methanol, ethanol, acetonitrile and any other suitable water miscible solvent. Preferably, methanol or ethanol is used.
- the ratio of adsorbent to volume of liquid waste material is in the range from 1 :1 to 1 :5 (weight/volume), preferably 1 :2 to 1 :3.
- the caffeoylshikimic acid isomers on the adsorbent are recovered in a single fraction using water or a mixture of water and solvent in appropriate amount.
- the water to solvent ratio ranges from 60:40 to 0:100, more preferably, 60:40 to 30:70, and most preferably 50:50 to 40:60, depending on the type of adsorbent used.
- the solvent suitable for use includes, but is not limited to, any one of methanol, ethanol, acetonitrile or any other suitable water miscible solvent.
- methanol or ethanol is used.
- the single fraction containing the caffeoy!shikimic acid isomers may be dried before the single fraction undergoes hydrolysis, to concentrate the single fraction.
- the step of drying can be carried out using any suitable methods known in the art. Such methods include, but are not limited to, freeze-drying, evaporation under vacuum or evaporation using heat.
- the single fraction may undergo hydrolysis without going through the step of drying.
- the single fraction can be hydrolyzed using, for example, alkaline water, alkaline water.solvent mixtures or alkaline aqueous solution.
- the single fraction is hydrolyzed using alkaline aqueous solution.
- Suitable alkaline aqueous solution includes, but is not limited to, sodium hydroxide, potassium hydroxide and other alkali known by one skilled in the art.
- the single fraction is hydrolyzed using aqueous sodium hydroxide solution.
- the duration of hydrolysis may vary according to the scale of production of the shikimic acid and the concentration of. the solution used. In all cases, the single fraction is hydrolyzed until all the caffeoylshikimic acid isomers are hydrolyzed.
- the hydrolysate containing the shikimic acid obtained from the hydrolysis can be purified using any methods known in the art.
- the hydrolysate is purified using reverse phase silica, ion exchange resin, simulated moving bed technology, or countercurrent chromatography.
- the hydrolysate containing the shikimic acid is purified without having to neutralize the hydrolysate. In another embodiment, the hydrolysate is neutralized prior to subjecting the hydrolysate to acetone precipitation to recover the shikimic acid.
- the method in accordance with the invention may further comprise centrifuging the oil palm waste material prior to the step of subjecting the oil palm waste material to resin adsorption, to obtain a supernatant and a solid.
- the supernatant may then undergo resin adsorption or silica-based adsorption.
- the types of resin suitable for use in this step include, but are not limited to, hydrophobic resin, such as an aromatic or modified aromatic resin (for example, sepabeads® and diaion®), or reversed phase silica, such as C 8 derivatized silica.
- the centrifuge used in the method of the present invention can be of any type of centrifuge such as a continuous centrifuge or a batch centrifuge.
- the operating temperature of the centrifuge is preferably set in the range from 4°C to 60°C, preferably below 10°C.
- the speed of the centrifuge may vary, as long as it can prolong the operating time with slow speed.
- the ratio of supernatant to adsorption resin used in the adsorption may range from 1 :1 to 10:1 , preferably 2:1 to 3:1 (volume/weight).
- the method of the present invention uses resin adsorption and hydrolysis techniques in isolating shikimic acid from oil palm waste materials. Adsorption of the precursor compounds such as caffeoylshikimic acid isomers into a single fraction using, for example, reverse phase silica or ion exchange resin, followed by hydrolysis provide good recovery of shikimic acid from oil palm waste materials and enable the shikimic acid to be purified using simple purification process.
- the method of the present invention eliminates the need to use complicated and expensive methods for purifying caffeoylshikimic acid isomers prior to converting the caffeoylshikimic acid isomers to shikimic acid in a separate process.
- the simplified purification processes enable the method of the present invention to be used for large scale isolation of shikimic acid from caffeoylshikimic acid isomers and large scale recovery of caffeoylshikimic acid from the starting materials.
- the composition of caffeoylshikimic acid was determined using liquid chromatography coupled with photodiode array detector (HPLC-PDA) or liquid chromatography coupled with LTQ-Orbitrap mass spectrometer (HPLC-LTQ- Orbitrap).
- the composition of caffeoylshikimic, shikimic, caffeic and dehydroshikimic acids was determined using liquid chromatography coupled with triple quadruple mass spectrometer (Triple-Quad).
- Separator sludge was collected from palm oil mill and stored at -80°C. 1 mL of thawed separator sludge was filtered with 0.2 prn membrane filter. The sludge was then subjected to HPLC-LTQ-Orbitrap with ESI negative mode to determine the presence of caffeoylshikimic acid in the separator sludge.
- the total ion chromatogram (TIC) obtained is as shown in Figure 1A and the chromatogram at m/z 335 is as shown in Figure 1 B.
- a solid or cake of post 3-phase decanter was collected from palm oil mill and stored at -80°C. 1 g of thawed decanter cake was mixed with 1 ml_ of 50% methanol-water, vortex for 1 minute. The sample was then centrifuged at 12,000 rpm for 1 minute. The supernatant was filtered with 0.2 pm membrane filter and then subjected to HPLC-LTQ-Orbitrap analysis to determine the presence of caffeoylshikimic acid isomers in the cake of decanter.
- the TIC obtained is as shown in Figure 2A and the chromatogram at m/z 335 is as shown in Figure 2B.
- Example 3 An aqueous phase of post 3-phase decanter was collected from palm oil mill and stored at -80°C. 1 mL of thawed aqueous sample was filtered with 0.2 pm membrane filter. The sample was then subjected to HPLC-LTQ-Orbitrap with ESI negative mode to determine the presence of caffeoylshikimic acid in the aqueous phase of decanter. The TIC obtained is as shown in Figure 3A and the chromatogram at m/z 335 is as shown in Figure 3B.
- Oil palm frond was collected from oil palm estate and was air dried, separated from rachis, and ground to about 100 pm. 3 kg of the ground frond were extracted with hexane, followed by dichloromethane. Subsequently, the residual were extracted with ethanol, followed by water. 9 litre of solvent were used for every extraction. Each extraction was carried out for three days. Each solvent extraction was repeated twice before changing to a more polar solvent. 0.1 g of dried ethanolic extract and 0.1 g of dried water extract of oil palm frond were each dissolved in 1 mL of 50% methanol-water, respectively.
- Example 5 Ethanolic and water extracts of rachis were prepared as per Example 4 and analyzed by HPLC-LTQ-Orbitrap to determine the presence of caffeoylshikimic acid.
- the TIC of the ethanolic extract and the water extract obtained from rachis are as shown in Figures 5A and 5C respectively.
- the chromatograms at m/z 335 of the ethanolic extract and the water extract are as shown in Figures 5B and 5D respectively.
- aqueous phase of post 3-phase decanter (similar to the one used in Example 3) was subjected to about 900 g of sepabead® SP207 separation (180 mm x 80 mm i.d.) to recover the caffeoylshikimic acid isomers from the aqueous phase of post 3-phase decanter.
- a total of 4 fractions, A to D were obtained.
- the solvent system used in the separation is as shown in Table 1.
- the fractions were dried and then subjected to HPLC-PDA for analysis.
- Caffeoylshikimic acid isomers were detected in fractions C and D as shown in Figures 6A and 6B. However, elution through the column was difficult due to blockage caused by the fruits debris found in this aqueous sample.
- This example shows the concentration and recovery of caffeoylshikimic acid isomers into one sample.
- Table 1 Solvent system for separation of aqueous phase of post 3-phase decanter using sepabead® SP207.
- the fractions were analyzed by HPLC-PDA without drying.
- the total amount of caffeoylshikimic acid isomers present in each fraction was as shown in Figure 7.
- the total amount of caffeoylshikimic acid isomers was calculated based on area obtained from HPLC-PDA standard curve of caffeic acid and relative to the molecular weight of caffeic acid.
- Table 3 Preliminary indication of relative caffeoylshikimic acid isomers (CSA) present in each fraction as compared to supernatant obtained from centrifuging aqueous phase of post 3-phase decanter (namely O).
- CSA caffeoylshikimic acid isomers
- Fraction E of Example 7 (namely, the enriched caffeoylshikimic acid fraction) underwent alkali hydrolysis, followed by purification with sepabead® SP207 (180 mm x 15 mm i.d.).
- a total of about 4.6323 g of enriched caffeoylshikimic acid fraction was dissolved in 93 ml_ of 50% methanol and hydrolyzed with 4.7 ml_ of sodium hydroxide with a concentration of 3 mol/L.
- the hydrolysis reaction was monitored for 5 hours and then overnight by observing the formation of shikimic acid using HPLC-PDA.
- the results are illustrated in Table 4. Caffeoylshikimic acid was hydrolyzed and the amount of shikimic acid slowly increased throughout the hydrolysis reaction, (see Figure 9).
- Table 4 Caffeoylshikimic and shikimic acid contents determined during 5 hours and 22 hours of hydrolysis before neutralization. Zero hour represents the time point where right after sodium hydroxide was added into the CSA solution. ppm
- the shikimic acid obtained after the hydrolysis can be purified by any suitable method known in the art including, but is not limited to, sepabead® SP207, RP18, ion exchange, and simulated moving bed technology.
- a total of 95 mg of shikimic acid was recovered from 4.63 g (out of a total of 5.75g) of fraction E. This method has the potential of yielding 53 mg of shikimic acid per litre of aqueous phase of post 3-phase decanter.
- aqueous phase of post 3-phase decanter (4 L) was centrifuged to obtain a supernatant (3.25 L) and a solid.
- the supernatant obtained (3 L) was then subjected to resin adsorption using sepabead® SP207 to recover an enriched caffeoylshikimic acid fraction.
- the centrifuge used in the study was set at 4°C at 10,000 rpm.
- the aqueous phase of post 3-phase decanter was centrifuged for 10 minutes. During the adsorption, the ratio of supernatant to adsorption resin used was 3:1 (volume/weight).
- the adsorbent containing caffeoylshikimic acid was washed with water twice, followed by elution with watermethanol at a ratio of 90:10 thrice until most of the unwanted polar materials were removed. This can be monitored using HPLC- PDA.
- the amount of water and/or watermethanol used for washing can be the same as the volume of the supernatant of post 3-phase decanter loaded into the adsorption resin, at 3L each elution.
- the caffeoylshikimic acid isomers was recovered in a single fraction by eluting a watermethanol mixture (3 L) in a ratio of 50:50 until most of the caffeoylshikimic acid isomers were recovered. This can be monitored using HPLC-PDA. A total of 9 L solvent mixtures of watermethanol was used.
- the caffeoylshikimic acid enriched fraction obtained was dried and a part of caffeoylshikimic acid enriched fraction (weight in grams) was dissolved in 20 parts (volume in mL) of 50% methanol-water.
- the concentrated caffeoylshikimic acid enriched fraction was then hydrolyzed with a part of sodium hydroxide with a concentration of 3 mol/L for about 5 hours to obtain the desired shikimic acid.
- the shikimic acid obtained is then purified from the hydrolysate using method known in the art, such as anion exchange method.
- a total of 233 mg of shikimic acid was recovered from 12.35 g (out of a total of 12.48 g obtained from 3 L of centrifuged aqueous phase of post 3-phase decanter) of enriched caffeoy!shikimic acid fraction.
- the enriched caffeoylshikimic acid fraction contained more than 3.5% of caffeoylshikimic acid.
- This method has the potential of yielding 63 mg of shikimic acid per litre of aqueous phase of post 3-phase decanter, with a recovery rate of more than 98% from the total caffeoylshikimic acid in the aqueous phase of post 3-phase decanter.
- Figure 10 shows the HPLC-PDA chromatograms of aqueous phase of post 3- phase decanter (Figure 10A), enriched caffeoylshikimic acid fraction before hydrolysis ( Figure 10B) and the fraction containing the resulting shikimic acid after hydrolysis ( FigurelOC).
- This method can yield 63 mg of shikimic acid / L of aqueous phase of post 3-phase decanter via purification from the hydrolysate using method known in the art, such as ion exchange resin method, RP18, sepabead® SP207, simulated moving bed technology, etc.
- aqueous phase of post 3-phase decanter contains a relatively higher amount of caffeoylshikimic acid isomers as compared to the other oil palm waste materials.
- This aqueous solution is relatively free of solid particles and non-polar materials. It therefore presents as an optimum source for the precursors of shikimic acid to be concentrated.
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- Oil, Petroleum & Natural Gas (AREA)
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BR112015012026A BR112015012026A2 (en) | 2012-11-26 | 2013-11-07 | method for isolating shikimic acid from palm oil waste material |
IN4312DEN2015 IN2015DN04312A (en) | 2012-11-26 | 2013-11-07 | |
CR20150332A CR20150332A (en) | 2012-11-26 | 2015-06-22 | A METHOD FOR ISOLATING SHIKIMIC ACID OF WASTE FROM PALMA ACEITERA |
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Cited By (3)
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WO2014189357A1 (en) * | 2013-05-21 | 2014-11-27 | Sime Darby Malaysia Berhad | A process for extracting phenolic compound |
CN109369373A (en) * | 2018-12-18 | 2019-02-22 | 长江师范学院 | A method of shikimic acid extract is prepared from ginkgo biloba p.e chromatography waste liquid |
WO2021193565A1 (en) * | 2020-03-27 | 2021-09-30 | 住友ベークライト株式会社 | Production method for cyclic compound or derivative thereof |
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- 2013-11-07 BR BR112015012026A patent/BR112015012026A2/en not_active Application Discontinuation
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WO2014189357A1 (en) * | 2013-05-21 | 2014-11-27 | Sime Darby Malaysia Berhad | A process for extracting phenolic compound |
CN109369373A (en) * | 2018-12-18 | 2019-02-22 | 长江师范学院 | A method of shikimic acid extract is prepared from ginkgo biloba p.e chromatography waste liquid |
CN109369373B (en) * | 2018-12-18 | 2021-01-08 | 长江师范学院 | Method for preparing shikimic acid extract from ginkgo leaf extract chromatography waste liquid |
WO2021193565A1 (en) * | 2020-03-27 | 2021-09-30 | 住友ベークライト株式会社 | Production method for cyclic compound or derivative thereof |
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BR112015012026A2 (en) | 2017-07-11 |
CR20150332A (en) | 2015-09-01 |
IN2015DN04312A (en) | 2015-10-16 |
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