US20160340271A1 - Methods for preparation of lycopenes from c15-wittig salts and methods for purification of high all-e containing and high 6z containing c15-wittig salts - Google Patents
Methods for preparation of lycopenes from c15-wittig salts and methods for purification of high all-e containing and high 6z containing c15-wittig salts Download PDFInfo
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- US20160340271A1 US20160340271A1 US15/227,343 US201615227343A US2016340271A1 US 20160340271 A1 US20160340271 A1 US 20160340271A1 US 201615227343 A US201615227343 A US 201615227343A US 2016340271 A1 US2016340271 A1 US 2016340271A1
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- lycopene
- wittig
- isomer
- salts
- lycopenes
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- 150000003839 salts Chemical class 0.000 title abstract description 69
- 238000000034 method Methods 0.000 title abstract description 20
- 150000002664 lycopenes Chemical class 0.000 title abstract description 12
- 238000002360 preparation method Methods 0.000 title abstract description 6
- 238000000746 purification Methods 0.000 title description 16
- 238000003786 synthesis reaction Methods 0.000 claims abstract description 27
- 239000001751 lycopene Substances 0.000 claims description 72
- 229960004999 lycopene Drugs 0.000 claims description 71
- OAIJSZIZWZSQBC-GYZMGTAESA-N lycopene Chemical compound CC(C)=CCC\C(C)=C\C=C\C(\C)=C\C=C\C(\C)=C\C=C\C=C(/C)\C=C\C=C(/C)\C=C\C=C(/C)CCC=C(C)C OAIJSZIZWZSQBC-GYZMGTAESA-N 0.000 claims description 48
- UPYKUZBSLRQECL-UKMVMLAPSA-N Lycopene Natural products CC(=C/C=C/C=C(C)/C=C/C=C(C)/C=C/C1C(=C)CCCC1(C)C)C=CC=C(/C)C=CC2C(=C)CCCC2(C)C UPYKUZBSLRQECL-UKMVMLAPSA-N 0.000 claims description 45
- JEVVKJMRZMXFBT-XWDZUXABSA-N Lycophyll Natural products OC/C(=C/CC/C(=C\C=C\C(=C/C=C/C(=C\C=C\C=C(/C=C/C=C(\C=C\C=C(/CC/C=C(/CO)\C)\C)/C)\C)/C)\C)/C)/C JEVVKJMRZMXFBT-XWDZUXABSA-N 0.000 claims description 44
- ZCIHMQAPACOQHT-ZGMPDRQDSA-N trans-isorenieratene Natural products CC(=C/C=C/C=C(C)/C=C/C=C(C)/C=C/c1c(C)ccc(C)c1C)C=CC=C(/C)C=Cc2c(C)ccc(C)c2C ZCIHMQAPACOQHT-ZGMPDRQDSA-N 0.000 claims description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 239000013078 crystal Substances 0.000 claims description 8
- 238000004128 high performance liquid chromatography Methods 0.000 claims description 8
- 239000002775 capsule Substances 0.000 claims 2
- 239000000839 emulsion Substances 0.000 claims 2
- 239000000203 mixture Substances 0.000 abstract description 37
- 230000015572 biosynthetic process Effects 0.000 abstract description 21
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 57
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 53
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 27
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 27
- 239000000010 aprotic solvent Substances 0.000 description 19
- 238000001914 filtration Methods 0.000 description 19
- 150000004714 phosphonium salts Chemical class 0.000 description 14
- 239000000843 powder Substances 0.000 description 14
- 239000000047 product Substances 0.000 description 13
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 10
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical compound CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 description 9
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 description 9
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 9
- 238000000605 extraction Methods 0.000 description 9
- 239000000243 solution Substances 0.000 description 9
- 241000235553 Blakeslea trispora Species 0.000 description 8
- 238000001035 drying Methods 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 7
- 239000000706 filtrate Substances 0.000 description 7
- HNZUNIKWNYHEJJ-UHFFFAOYSA-N geranyl acetone Natural products CC(C)=CCCC(C)=CCCC(C)=O HNZUNIKWNYHEJJ-UHFFFAOYSA-N 0.000 description 7
- JXJIQCXXJGRKRJ-KOOBJXAQSA-N pseudoionone Chemical compound CC(C)=CCC\C(C)=C\C=C\C(C)=O JXJIQCXXJGRKRJ-KOOBJXAQSA-N 0.000 description 7
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 6
- 239000002244 precipitate Substances 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- 238000003556 assay Methods 0.000 description 5
- 239000012266 salt solution Substances 0.000 description 5
- 239000011877 solvent mixture Substances 0.000 description 5
- 238000005292 vacuum distillation Methods 0.000 description 5
- AYODHZHFDRRQEZ-UHFFFAOYSA-N 2,7-dimethylocta-2,4,6-trienedial Chemical compound O=CC(C)=CC=CC=C(C)C=O AYODHZHFDRRQEZ-UHFFFAOYSA-N 0.000 description 4
- 241000227653 Lycopersicon Species 0.000 description 4
- 235000007688 Lycopersicon esculentum Nutrition 0.000 description 4
- 238000007239 Wittig reaction Methods 0.000 description 4
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- 239000000376 reactant Substances 0.000 description 4
- 238000011282 treatment Methods 0.000 description 4
- RIOQSEWOXXDEQQ-UHFFFAOYSA-N triphenylphosphine Chemical compound C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 RIOQSEWOXXDEQQ-UHFFFAOYSA-N 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 235000021466 carotenoid Nutrition 0.000 description 3
- 150000001747 carotenoids Chemical class 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000006317 isomerization reaction Methods 0.000 description 3
- 150000007524 organic acids Chemical class 0.000 description 3
- 239000003960 organic solvent Substances 0.000 description 3
- 229910000027 potassium carbonate Inorganic materials 0.000 description 3
- TYJJADVDDVDEDZ-UHFFFAOYSA-M potassium hydrogencarbonate Chemical compound [K+].OC([O-])=O TYJJADVDDVDEDZ-UHFFFAOYSA-M 0.000 description 3
- QSGIPTUSRASGRK-UHFFFAOYSA-M triphenyl(3,7,11-trimethyldodeca-2,4,6,10-tetraenyl)phosphanium;chloride Chemical compound [Cl-].C=1C=CC=CC=1[P+](C=1C=CC=CC=1)(CC=C(C)C=CC=C(C)CCC=C(C)C)C1=CC=CC=C1 QSGIPTUSRASGRK-UHFFFAOYSA-M 0.000 description 3
- UIMSQVVHHIUQOZ-UHFFFAOYSA-N 3,7,11-trimethyldodeca-1,4,6,10-tetraen-3-ol Chemical compound CC(C)=CCCC(C)=CC=CC(C)(O)C=C UIMSQVVHHIUQOZ-UHFFFAOYSA-N 0.000 description 2
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- 235000012828 Citrullus lanatus var citroides Nutrition 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- OAIJSZIZWZSQBC-OUUYXACASA-N cis-lycopene Natural products CC(=CCCC(=CC=CC(=C/C=C/C(=C/C=C/C=C(C)/C=C/C=C(C)/C=C/C=C(C)/CCC=C(C)C)/C)C)C)C OAIJSZIZWZSQBC-OUUYXACASA-N 0.000 description 2
- 208000029078 coronary artery disease Diseases 0.000 description 2
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- BMYNFMYTOJXKLE-UHFFFAOYSA-N 3-azaniumyl-2-hydroxypropanoate Chemical compound NCC(O)C(O)=O BMYNFMYTOJXKLE-UHFFFAOYSA-N 0.000 description 1
- HRQKOYFGHJYEFS-UHFFFAOYSA-N Beta psi-carotene Chemical compound CC(C)=CCCC(C)=CC=CC(C)=CC=CC(C)=CC=CC=C(C)C=CC=C(C)C=CC1=C(C)CCCC1(C)C HRQKOYFGHJYEFS-UHFFFAOYSA-N 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- 240000000560 Citrus x paradisi Species 0.000 description 1
- 206010028980 Neoplasm Diseases 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
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- 235000006708 antioxidants Nutrition 0.000 description 1
- 235000013734 beta-carotene Nutrition 0.000 description 1
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- 208000024348 heart neoplasm Diseases 0.000 description 1
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- 238000004519 manufacturing process Methods 0.000 description 1
- SYSQUGFVNFXIIT-UHFFFAOYSA-N n-[4-(1,3-benzoxazol-2-yl)phenyl]-4-nitrobenzenesulfonamide Chemical class C1=CC([N+](=O)[O-])=CC=C1S(=O)(=O)NC1=CC=C(C=2OC3=CC=CC=C3N=2)C=C1 SYSQUGFVNFXIIT-UHFFFAOYSA-N 0.000 description 1
- 230000019612 pigmentation Effects 0.000 description 1
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/32—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from compounds containing hetero-atoms other than or in addition to oxygen or halogen
- C07C1/34—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from compounds containing hetero-atoms other than or in addition to oxygen or halogen reacting phosphines with aldehydes or ketones, e.g. Wittig reaction
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/21—Alkatrienes; Alkatetraenes; Other alkapolyenes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
- C07F9/02—Phosphorus compounds
- C07F9/28—Phosphorus compounds with one or more P—C bonds
- C07F9/54—Quaternary phosphonium compounds
- C07F9/5442—Aromatic phosphonium compounds (P-C aromatic linkage)
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
- C07B2200/00—Indexing scheme relating to specific properties of organic compounds
- C07B2200/09—Geometrical isomers
Definitions
- the present invention relates to methods for preparation of lycopenes, especially to lycopenes with high all-E contents or high 6Z contents from C15-Wittig slats mixtures.
- methods for extraction and purification of desired E/Z ratios in C15-Wittig salts are also disclosed.
- Lycopene (also referred to as ⁇ , ⁇ -carotene) is one of the many carotenoids that exist in nature. Lycopene can be easily found in ripe tomato fruits, watermelons and pink grapefruits, giving them a characteristic red pigmentation. Lycopene obtained from raw tomatoes contains approximately 5% or more of cis-lycopene. According Schierle et al. 1997, lycopene obtained from raw tomatoes contains 94-96% of all-E-lycopene, 3-5% of 5Z-lycopene and a minor quantity of Z-isomers. Recent epidemiological studies show that lycopene as antioxidant may alleviate coronary heart disease and cancers of prostate, bladder, skin, digestive tract, breast and cervix.
- Lycopene can be produced in two ways: extraction and synthesis. Biological lycopene is extracted either from fruits (such as tomatoes or watermelons) or from fungal biomass (such as Blakeslea trispora ). Synthetic lycopene is manufactured through chemical synthesis. Lycopene produced by using synthesis process has lower all-E content than that extracted from B. trispora.
- the joint FAO (Food and Agriculture Organization of the United Nations)/WHO (World Health Organization) expert committee has established specifications for both synthetic lycopene and lycopene extracted from B. trispora at the 67th meeting of JECFA (2006).
- total lycopene content shall be higher than 96%, in which at least 70% must be all-E-lycopene and the remains are 5Z-lycopene and a minor quantity of Z-isomers.
- the total lycopene content shall be higher than 95%, in which at least 90% must be all-E-lycopene and the remains are other carotenoids ( ⁇ - and ⁇ -carotene) for not more than 5%.
- Pseudoionone is one of the starting materials for lycopene syntheses. It is a mixture of cis and trans isomers (also referred to as the cis/trans mixture). In general, pseudoionone cis/trans mixtures containing about 20% to 50% of all-trans-isomer and the remains of other cis-isomers are available in the market. A cis-pseudoionone will result in a cis-lycopene and an all-trans-pseudoionone will result in an all-E-lycopene, after the syntheses. In order to obtain higher all-E containing lycopene, a pseudoionone with higher all-trans content shall be used.
- the all-trans-pseudoionone must first be separated from the pseudoionone cis/trans mixture before the syntheses.
- all-trans-pseudoionone is isolated from the cis/trans mixture by a fractional distillation operation. This purified all-trans-pseudoionone so obtained is then used to synthesize a C15 phosphonium salt to produce lycopene.
- the other method for producing synthetic all-E-lycopenes uses thermal isomerization process that converts Z-isomers of lycopene into all-E-lycopene.
- This process increases the all-E content of the obtained lycopene from 53% to 73.4%-87.8%.
- the obtained all-E content may even satisfy the all-E content specification for biological lycopenes.
- a synthetic lycopene with a 5Z-content of up to 97% is also obtained.
- new methods for the preparation of all-E-lycopenes and 5Z-lycopenes are disclosed.
- the methods generally include the steps of purification of all-E-C15-Wittig salts and synthesis of all-E-Lycopene and 5Z-Lycopene using the purified all-E-C15-Wittig salts.
- C15-Witting salts of a variety of E isomer/Z isomer ratio may be obtained.
- the invented methods may further comprise synthesis of C15-OH, to be used as material for the all-E-C15-Wittig salts.
- a C15 Wittig salt cis/trans mixture preferably a C15 phosphonium salt cis/trans mixture, containing about 40% of all-E content is first obtained.
- the C15 Wittig salt cis/trans mixture is preferably a product of synthesis of all-E-C15-Witting salts, whereby it contains both cis and trans forms of isomers.
- the C15 Wittig salt cis/trans mixture is concentrated under vacuum to remove methanol and H 2 O contained therein, whereby a C15-Wittig salt precipitate is obtained. An aprotic solvent is added to the precipitate for further concentration.
- the aprotic solvent may be ethyl acetate, chloroform, acetone, methyl ethyl ketone or methyl isobutyl ketone, or any combination thereof, and is preferably ethyl acetate.
- the concentration takes place at around 30° C. for a relatively long period of time, such as 16 hours.
- a crystalized C15-Wittig salt precipitate is obtained.
- An aprotic solvent is later added to the precipitate for extraction of 6Z-C15-Wittig salts.
- the aprotic solvent may be ethyl acetate, chloroform, acetone, methyl ethyl ketone or methyl isobutyl ketone, or any combination thereof, and is preferably acetone.
- the extraction operation takes place at between 0° C. to 55° C., preferably 40° C. to 50° C., for about 2 hours.
- a wet cake of 6Z-C15-Wittig salt is obtained.
- the 6Z-C15-Wittig salt wet cake is removed and the filtrate is concentrated again, to obtain C15-Wittig salts with an E isomer/Z isomer ratio of greater than 3:1.
- an aprotic solvent in either a pure solvent form or a solvent mixture form is added to the C15-Wittig salts, i.e, the filtrate after the wet cake of 6Z-C15-Wittig salt is removed after the filtration step, for crystallization.
- the aprotic solvent may be ethyl acetate, chloroform, acetone, methyl ethyl ketone or methyl isobutyl ketone, or any combination thereof, and is preferably an ethyl acetate/acetone mixture.
- the crystallization operation takes place at between 25° C. to ⁇ 30° C. for a relatively long time, preferably 0° C. to ⁇ 20° C. for about 16 hours. After filtration and drying, C15-Wittig salts with an E isomer/Z isomer ratio of greater than 15:1 are obtained.
- the wet cake of 6Z-C15-Wittig salts obtained in the previous filtration step is rinsed in an aprotic solvent.
- the aprotic solvent may be acetone, methyl ethyl ketone or methyl isobutyl ketone, or any combination thereof, and is preferably acetone.
- the rinsing operation takes place at between 0° C. to 55° C., preferably 40° C. to 50° C., for about 2 hours.
- C15-Wittig salts with an E isomer/Z isomer ratio of less than 1:30 are obtained.
- lycopenes i.e., all-E-lycopene and 5Z-lycopene
- products obtained from the purification step are reacted with C10-dialdehyde in a double Wittig reaction.
- a base reactant may be added to proceed the reaction.
- a lycopene wet cake is collected.
- the product is washed, rinsed, filtered and dried to obtain all-E-lycopene powders with an all-E content of up to 95%, or 5Z-lycopene powders with a 5Z content of up to 97%.
- the C15 phosphonium salt cis/trans mixtures may be prepared by reacting vinyl-pseudoionol and triphenylphosphine with an inorganic or organic acid, preferably a strong inorganic or organic acid.
- the strong acid may be a hydrohalic acid such as hydrochloric acid and hydrobromic acid, sulfuric acid, phosphoric acid, sulfonic acid and other inorganic or any organic acid with a comparable degree of dissociation.
- the present invention discloses novel methods for the preparation of all-E-lycopenes and 5Z-lycopenes.
- the invented methods feature in their capability of producing C15-Wittig salts with controllable E isomer/Z isomer ratios and synthesis of all-E-lycopenes and 5Z-lycopenes using the particular C15-Wittig salts.
- All-E-lycopenes with an all-E content of up to 95% or 5Z-lycopenes with a 5Z content of up to 97% are obtained by using the method of this invention.
- the invented methods generally include the steps of purification of C15-Wittig salts and synthesis of all-E-lycopenes and 5Z-lycopenes using the purified C15-Wittig salts.
- a C15 phosphonium salt cis/trans mixture is first obtained.
- the mixture is preferably a product from the synthesis of C15-Wittig salts, using the conventional synthesis methods.
- the mixture is first concentrated under vacuum to remove as much methanol/H 2 O as possible, if it is produced in a previous synthesis step. After enough quantity of methanol/H 2 O is removed, a C15-Wittig salt precipitate is emerged. The concentration takes place at around 30° C. for a relatively long period of time, such as 16 hours.
- C15-Witting salts of desired E isomer/Z isomer ratio may be obtained.
- both all-E-C15-Wittig salts and 6Z-C15-Wittig salts have poorer solubility than 2Z-C15-Wittig salts in ethyl acetate.
- both 2Z-C15-Wittig salts and all-E-C15-Wittig salts have much better solubility than 6Z-C15-Wittig salts in either acetone, methyl ethyl ketone or methyl isobutyl ketone.
- An aprotic solvent is later added to the precipitate for extraction of 6Z-C15-Wittig salts.
- the aprotic solvent may be ethyl acetate, chloroform, acetone, methyl ethyl ketone or methyl isobutyl ketone, or any combination thereof, and is preferably acetone.
- the extraction operation takes place at between 0° C. to 55° C., preferably 40° C. to 50° C., for about 2 hours. After filtration, a wet cake of 6Z-C15-Wittig salt is obtained. The 6Z-C15-Wittig salt wet cake is removed.
- the filtrate is again concentrated in an aprotic solvent, preferably ethyl acetate, to obtain C15-Wittig salts having an E isomer/Z isomer ratio of greater than 3:1.
- the E isomer content in the product is relatively low but the product is useful in direct reaction with a C10-dialdehyde without further purification, to produce a qualified (high all-E content) synthetic lycopene.
- an aprotic solvent in either a pure solvent form or a solvent mixture form is added to the C15-Wittig salts obtained in the previous extraction step for crystallization.
- the aprotic solvent is preferably ethyl acetate.
- the crystallization operation may take place under the temperature of between 25° C. to ⁇ 30° C. for a predetermined period of time, preferably under 0° C. to ⁇ 20° C. for, for example, 16 hours.
- the produced wet cake may be further purified in an ethyl acetate/acetone solvent.
- the products are filtered and dried to obtain high all-E content of C15-Wittig salts with an E isomer/Z isomer ratio of greater than 15:1.
- the wet cake of 6Z-C15-Wittig salts obtained in the above-mentioned extraction step is subjected to further purification.
- An aprotic solvent is added to the wet cake.
- Aprotic solvents applicable in this purification step include acetone, methyl ethyl ketone and methyl isobutyl ketone and any of their combinations.
- the purification is operated under the temperature of 0° C. to 55° C., preferably 40° C. to 50° C., for a period of time such as 2 hours.
- the products are filtered and dried to obtain a high 6Z content of C15-Wittig salts with an E isomer/Z isomer ratio of less than 1:30.
- C10-dialdehyde is reacting with products of the purification steps.
- the high all-E content or high 6Z content of C15-Wittig salts obtained in the purification process is reacted with the C10-dialdehyde in a double Wittig reaction.
- a base reactant may be added to proceed the reaction.
- the product is then processed by thermal isomerization and filtration, to obtain a lycopene wet cake. Acetone and water are added separately for washing and rinsing treatments. After filtration and drying, all-E-lycopene powders with all-E content of up to 95% or 5Z-lycopene powders with 5Z content of up to 97% are obtained.
- the invented methods may include optionally synthesis of C15-OH, to be used as the C15-Wittig salts.
- the resulted C15 phosphonium salt is also a cis/trans mixture, containing about 40% of all-E content.
- methods that produce C15-Wittig salts with almost any desirable E isomer/Z isomer ratio are provided.
- lycopenes with almost any desirable E isomer/Z isomer ratio of lycopene may also be prepared, using the C15-Wittig salts, purified according to this invention, as material.
- the present invention provides new methods of producing desirable synthetic lycopene.
- a 3,7,11-trimethyldodeca-2E,4E,6E,10E-tetraen-1-yl-triphenylphosphonium chloride salt wet cake was obtained by filtration. 167 ml of ethyl acetate and 33 ml of acetone were added to the obtained wet cake. The mixture was stirred at 25° C. for 30 minutes then cooled to 5° C. and stirred for 16 hours. After filtration and drying, 30 g of 3,7,11-trimethyl-dodeca-2E,4E,6E,10E-tetraen-1-yl-triphenyl phosphonium chloride (All E-C15TPPCl) salt powder were obtained. HPLC analysis revealed that the powder contains 94.8% of all-E isomer, 3.3% of 6Z isomer, and 1.9% of 2Z isomer. The E isomer/Z isomer ratio is accordingly 18.2:1.
- 1,534.0 g of a 3,7,11-trimethyldodeca-2,4,6,10-tetraen-1-yl-triphenylphosphonium chloride salt solution purity 38.6% in methanol
- 42.6% of all-E isomer 39.6% of 6Z and 2Z isomers
- the solution mixture was heated to 60° C. and stirred for 3 hours. Thereafter, the temperature of the solution mixture was raised to 100° C. to remove as much organic solvents as possible, then cooled to 80° C. and stirred for 16 hours.
- 95.9 g of lycopene wet cake were obtained by filtration. Acetone and water were added to the wet cake separately for washing and rinsing treatments. After filtration and drying, 24.6 g of synthetic lycopene crystal were obtained.
- Lycopene is one of the many carotenoids that may alleviate coronary heart disease and prevent from several kinds of cancers. It can be produced by way of either extraction or synthesis. Current synthesis processes can produce synthetic lycopenes with all-E content of merely 87%, which is much lower than that of the biological lycopene extracted from B. trispora /natural source. This invention makes the synthetic lycopene to meet the all-E content standard for biological lycopene extracted from B.
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Abstract
The present invention relates to methods for preparation of lycopenes, especially to lycopenes with high all-E contents or high 6Z contents from C15-Wittig slats mixtures.(with high all-E-contents and high 6Z-contents, respectively). C15-Wittig slats mixtures are purified and 6Z-C15-Wittig salts are extracted from the mixtures. The extracted 6Z-C15-Wittig salts are,used in the synthesis of lycopenes with high 6Z contents and the residues are used in the synthesis of lycopenes with high All-E contents.
Description
- The present invention relates to methods for preparation of lycopenes, especially to lycopenes with high all-E contents or high 6Z contents from C15-Wittig slats mixtures. In this invention, methods for extraction and purification of desired E/Z ratios in C15-Wittig salts are also disclosed.
- Lycopene (also referred to as Ψ, Ψ-carotene) is one of the many carotenoids that exist in nature. Lycopene can be easily found in ripe tomato fruits, watermelons and pink grapefruits, giving them a characteristic red pigmentation. Lycopene obtained from raw tomatoes contains approximately 5% or more of cis-lycopene. According Schierle et al. 1997, lycopene obtained from raw tomatoes contains 94-96% of all-E-lycopene, 3-5% of 5Z-lycopene and a minor quantity of Z-isomers. Recent epidemiological studies show that lycopene as antioxidant may alleviate coronary heart disease and cancers of prostate, bladder, skin, digestive tract, breast and cervix.
- Lycopene can be produced in two ways: extraction and synthesis. Biological lycopene is extracted either from fruits (such as tomatoes or watermelons) or from fungal biomass (such as Blakeslea trispora). Synthetic lycopene is manufactured through chemical synthesis. Lycopene produced by using synthesis process has lower all-E content than that extracted from B. trispora. The joint FAO (Food and Agriculture Organization of the United Nations)/WHO (World Health Organization) expert committee has established specifications for both synthetic lycopene and lycopene extracted from B. trispora at the 67th meeting of JECFA (2006). For synthetic lycopene, total lycopene content shall be higher than 96%, in which at least 70% must be all-E-lycopene and the remains are 5Z-lycopene and a minor quantity of Z-isomers. For lycopene extracted from B. trispora, the total lycopene content shall be higher than 95%, in which at least 90% must be all-E-lycopene and the remains are other carotenoids (β- and γ-carotene) for not more than 5%. These specifications indicate that lycopene extracted from B. trispora consists mainly of all-E-form, which no synthetic lycopene prepared using the nowadays technology may reach.
- Pseudoionone is one of the starting materials for lycopene syntheses. It is a mixture of cis and trans isomers (also referred to as the cis/trans mixture). In general, pseudoionone cis/trans mixtures containing about 20% to 50% of all-trans-isomer and the remains of other cis-isomers are available in the market. A cis-pseudoionone will result in a cis-lycopene and an all-trans-pseudoionone will result in an all-E-lycopene, after the syntheses. In order to obtain higher all-E containing lycopene, a pseudoionone with higher all-trans content shall be used. Therefore, the all-trans-pseudoionone must first be separated from the pseudoionone cis/trans mixture before the syntheses. In the conventional technology, all-trans-pseudoionone is isolated from the cis/trans mixture by a fractional distillation operation. This purified all-trans-pseudoionone so obtained is then used to synthesize a C15 phosphonium salt to produce lycopene.
- Unfortunately, the conventional synthesis process in producing the C15 phosphonium salts will cause a part of the all-trans-form to convert to cis-forms during the reaction. With the current technology, even the high all-E containing (90% to 95%) C15-OH (also referred to as 3,7,11-trimethyl-dodeca-1,4,6,10-tetraen-3-ol or vinyl-pseudoionol) is used, a product with only 65.2% to 71.1% of all-E-C15-Wittig salts, as well as 9.8% to 10.3% of 6Z and 8.2% to 10.8% of 2Z isomers, would be obtained. Clearly, the resulted products have lower E isomer/Z isomer ratios, which are about 3.4:1 to 3.8:1. Reference may be made to, for example, U.S. Pat. No. 6,603,045, U.S. Pat. No. 6,433,226, U.S. Pat. No. 6,187,959 and U.S. Pat. No. 2002/0,128,516. Such poor E/Z selectivity of C15 phosphonium salts is a challenge in producing a synthetic all-E-lycopene, with all-E content competitive to that of biological lycopenes extracted from natural sources such as B. trispora.
- The other method for producing synthetic all-E-lycopenes uses thermal isomerization process that converts Z-isomers of lycopene into all-E-lycopene. Reference may be made to U.S. Pat. No. 7,126,036 and U.S. Pat. No. 2004/0049082. This process increases the all-E content of the obtained lycopene from 53% to 73.4%-87.8%.
- It has been found that all-E-C15-Wittig salts can be separated from the C15 phosphonium salt obtained from the reaction of cis/trans mixture, using a series of purification steps in aprotic solvents. According to the present invention, significantly high E/Z selectivity in the C15 phosphonium salts, with an E isomer/Z isomer ratio of greater than 15:1, may be realized. By reacting a C10-dialdehyde (also referred to as 2,7-dimethyl-2,4,6-octatriene-1,8-dial) with such high all-E content of C15-Wittig salts through a double Wittig reaction, a synthetic lycopene with all-E content for up to 95% may be produced. The obtained all-E content may even satisfy the all-E content specification for biological lycopenes. By switching the reactants from high all-E content of C15-Wittig salts to high 6Z content of C15 phosphonium salts, a synthetic lycopene with a 5Z-content of up to 97% is also obtained.
- According to the present invention, new methods for the preparation of all-E-lycopenes and 5Z-lycopenes are disclosed. The methods generally include the steps of purification of all-E-C15-Wittig salts and synthesis of all-E-Lycopene and 5Z-Lycopene using the purified all-E-C15-Wittig salts. According to this invention, by changing the combination of solvents used and the reaction temperature, C15-Witting salts of a variety of E isomer/Z isomer ratio may be obtained. The invented methods may further comprise synthesis of C15-OH, to be used as material for the all-E-C15-Wittig salts.
- In the purification of all-E-C15-Wittig salts, a C15 Wittig salt cis/trans mixture, preferably a C15 phosphonium salt cis/trans mixture, containing about 40% of all-E content is first obtained. The C15 Wittig salt cis/trans mixture is preferably a product of synthesis of all-E-C15-Witting salts, whereby it contains both cis and trans forms of isomers. The C15 Wittig salt cis/trans mixture is concentrated under vacuum to remove methanol and H2O contained therein, whereby a C15-Wittig salt precipitate is obtained. An aprotic solvent is added to the precipitate for further concentration. The aprotic solvent may be ethyl acetate, chloroform, acetone, methyl ethyl ketone or methyl isobutyl ketone, or any combination thereof, and is preferably ethyl acetate. The concentration takes place at around 30° C. for a relatively long period of time, such as 16 hours. A crystalized C15-Wittig salt precipitate is obtained. An aprotic solvent is later added to the precipitate for extraction of 6Z-C15-Wittig salts. The aprotic solvent may be ethyl acetate, chloroform, acetone, methyl ethyl ketone or methyl isobutyl ketone, or any combination thereof, and is preferably acetone. The extraction operation takes place at between 0° C. to 55° C., preferably 40° C. to 50° C., for about 2 hours. After filtration, a wet cake of 6Z-C15-Wittig salt is obtained. The 6Z-C15-Wittig salt wet cake is removed and the filtrate is concentrated again, to obtain C15-Wittig salts with an E isomer/Z isomer ratio of greater than 3:1.
- In order to obtain C15-Wittig salts with high all-E contents, an aprotic solvent in either a pure solvent form or a solvent mixture form is added to the C15-Wittig salts, i.e, the filtrate after the wet cake of 6Z-C15-Wittig salt is removed after the filtration step, for crystallization. The aprotic solvent may be ethyl acetate, chloroform, acetone, methyl ethyl ketone or methyl isobutyl ketone, or any combination thereof, and is preferably an ethyl acetate/acetone mixture. The crystallization operation takes place at between 25° C. to −30° C. for a relatively long time, preferably 0° C. to −20° C. for about 16 hours. After filtration and drying, C15-Wittig salts with an E isomer/Z isomer ratio of greater than 15:1 are obtained.
- In order to obtain C15-Wittig salts with high 6Z contents, the wet cake of 6Z-C15-Wittig salts obtained in the previous filtration step is rinsed in an aprotic solvent. The aprotic solvent may be acetone, methyl ethyl ketone or methyl isobutyl ketone, or any combination thereof, and is preferably acetone. The rinsing operation takes place at between 0° C. to 55° C., preferably 40° C. to 50° C., for about 2 hours. After filtration and drying, C15-Wittig salts with an E isomer/Z isomer ratio of less than 1:30 are obtained.
- In the synthesis of lycopenes, i.e., all-E-lycopene and 5Z-lycopene, products obtained from the purification step are reacted with C10-dialdehyde in a double Wittig reaction. A base reactant may be added to proceed the reaction. After thermal isomerization and filtration, a lycopene wet cake is collected. The product is washed, rinsed, filtered and dried to obtain all-E-lycopene powders with an all-E content of up to 95%, or 5Z-lycopene powders with a 5Z content of up to 97%.
- In the optional synthesis step of C15-OH, the C15 phosphonium salt cis/trans mixtures may be prepared by reacting vinyl-pseudoionol and triphenylphosphine with an inorganic or organic acid, preferably a strong inorganic or organic acid. The strong acid may be a hydrohalic acid such as hydrochloric acid and hydrobromic acid, sulfuric acid, phosphoric acid, sulfonic acid and other inorganic or any organic acid with a comparable degree of dissociation.
- The present invention discloses novel methods for the preparation of all-E-lycopenes and 5Z-lycopenes. The invented methods feature in their capability of producing C15-Wittig salts with controllable E isomer/Z isomer ratios and synthesis of all-E-lycopenes and 5Z-lycopenes using the particular C15-Wittig salts. All-E-lycopenes with an all-E content of up to 95% or 5Z-lycopenes with a 5Z content of up to 97% are obtained by using the method of this invention.
- The invented methods generally include the steps of purification of C15-Wittig salts and synthesis of all-E-lycopenes and 5Z-lycopenes using the purified C15-Wittig salts. In the purification of C15-Wittig salts, a C15 phosphonium salt cis/trans mixture is first obtained. The mixture is preferably a product from the synthesis of C15-Wittig salts, using the conventional synthesis methods. The mixture is first concentrated under vacuum to remove as much methanol/H2O as possible, if it is produced in a previous synthesis step. After enough quantity of methanol/H2O is removed, a C15-Wittig salt precipitate is emerged. The concentration takes place at around 30° C. for a relatively long period of time, such as 16 hours.
- According to this invention, by changing the combination of aprotic solvents used and the reaction temperature, C15-Witting salts of desired E isomer/Z isomer ratio may be obtained. For example, among the Wittig salts, both all-E-C15-Wittig salts and 6Z-C15-Wittig salts have poorer solubility than 2Z-C15-Wittig salts in ethyl acetate. On the other hand, both 2Z-C15-Wittig salts and all-E-C15-Wittig salts have much better solubility than 6Z-C15-Wittig salts in either acetone, methyl ethyl ketone or methyl isobutyl ketone. The solubility of 6Z-C15-Wittig salts in acetone, methyl ethyl ketone or methyl isobutyl ketone also varies with temperature. It is therefore possible to control the E isomer/Z isomer ratios in the resulted C15-Wittig salts by changing the combination of the aprotic solvents as well as the purification temperature.
- An aprotic solvent is later added to the precipitate for extraction of 6Z-C15-Wittig salts. The aprotic solvent may be ethyl acetate, chloroform, acetone, methyl ethyl ketone or methyl isobutyl ketone, or any combination thereof, and is preferably acetone. The extraction operation takes place at between 0° C. to 55° C., preferably 40° C. to 50° C., for about 2 hours. After filtration, a wet cake of 6Z-C15-Wittig salt is obtained. The 6Z-C15-Wittig salt wet cake is removed. The filtrate is again concentrated in an aprotic solvent, preferably ethyl acetate, to obtain C15-Wittig salts having an E isomer/Z isomer ratio of greater than 3:1. The E isomer content in the product is relatively low but the product is useful in direct reaction with a C10-dialdehyde without further purification, to produce a qualified (high all-E content) synthetic lycopene.
- In order to obtain higher all-E content of C15-Wittig salts, an aprotic solvent in either a pure solvent form or a solvent mixture form is added to the C15-Wittig salts obtained in the previous extraction step for crystallization. The aprotic solvent is preferably ethyl acetate. The crystallization operation may take place under the temperature of between 25° C. to −30° C. for a predetermined period of time, preferably under 0° C. to −20° C. for, for example, 16 hours. The produced wet cake may be further purified in an ethyl acetate/acetone solvent. The products are filtered and dried to obtain high all-E content of C15-Wittig salts with an E isomer/Z isomer ratio of greater than 15:1.
- In order to obtain C15-Wittig salts with high 6Z content, the wet cake of 6Z-C15-Wittig salts obtained in the above-mentioned extraction step is subjected to further purification. An aprotic solvent is added to the wet cake. Aprotic solvents applicable in this purification step include acetone, methyl ethyl ketone and methyl isobutyl ketone and any of their combinations. The purification is operated under the temperature of 0° C. to 55° C., preferably 40° C. to 50° C., for a period of time such as 2 hours. The products are filtered and dried to obtain a high 6Z content of C15-Wittig salts with an E isomer/Z isomer ratio of less than 1:30.
- In the synthesis of lycopene, C10-dialdehyde is reacting with products of the purification steps. The high all-E content or high 6Z content of C15-Wittig salts obtained in the purification process is reacted with the C10-dialdehyde in a double Wittig reaction. A base reactant may be added to proceed the reaction. The product is then processed by thermal isomerization and filtration, to obtain a lycopene wet cake. Acetone and water are added separately for washing and rinsing treatments. After filtration and drying, all-E-lycopene powders with all-E content of up to 95% or 5Z-lycopene powders with 5Z content of up to 97% are obtained.
- The invented methods may include optionally synthesis of C15-OH, to be used as the C15-Wittig salts. In the synthesis of C15-OH, a purified pseudoionone (Fluka, E/Z=2.7:1) is reacted with vinyl magnesium chloride. Since the reactant, pseudoionone, is a cis/trans mixture, the produced C15-OH is also a cis/trans mixture and has the same level of E isomer/Z isomer ratio as in the pseudoionone. Thereafter, the C15-OH is reacted with a triphenylphosphine and a strong acid, to produce the desired C15 phosphonium salts. The resulted C15 phosphonium salt is also a cis/trans mixture, containing about 40% of all-E content. According to the present invention, methods that produce C15-Wittig salts with almost any desirable E isomer/Z isomer ratio are provided. As a result, lycopenes with almost any desirable E isomer/Z isomer ratio of lycopene may also be prepared, using the C15-Wittig salts, purified according to this invention, as material. The present invention provides new methods of producing desirable synthetic lycopene.
- In the followings, embodiments in the purification of C15-Wittig salts and in the synthesis of all-E-lycopenes and 5Z-lycopenes using the purified C15-Wittig salts will be illustrated.
- Preparation of C15-TPP salts with high all-E content or high 6Z content
- 250.0 g of 3,7,11-trimethyldodeca-2,4,6,10-tetraen-1-yl-triphenylphosphonium chloride salt solution (purity 38.6% in methanol) with 40.9% of all-E content, 38.7%, of, 6Z content and 4.1% of 2Z content (E isomer/Z isomer ratio=1:1) were concentrated by vacuum distillation at 30° C., to remove methanol solvent. Then 135 g of ethyl acetate were added. After concentration by vacuum distillation, 60 g of ethyl acetate was added in addition. The salt solution was then heated to 30° C. and stirred for 16 hours. Thereafter, 120 g of acetone was added into the mixture. Temperature was raised to 50° C. and maintained for 2 hours then lowered to 30° C. The products were filtered to obtained solid phase 3,7,11-trimethyldodeca-2E,4E,6Z,10E-tetraen-1-yl-triphenylphosphonium chloride (6Z-C15TPPCl) salt wet cake in the amount of 48.5 g (assay 6z-%=73.3%; assay All E %=12%). The wet cake was removed and the filtrate was concentrated at 50° C. by vacuum distillation. Thereafter, the concentrated filtrate was added 197 g of ethyl acetate, cooled to −20° C. and stirred for 16 hours. A 3,7,11-trimethyldodeca-2E,4E,6E,10E-tetraen-1-yl-triphenylphosphonium chloride salt wet cake was obtained by filtration. 167 ml of ethyl acetate and 33 ml of acetone were added to the obtained wet cake. The mixture was stirred at 25° C. for 30 minutes then cooled to 5° C. and stirred for 16 hours. After filtration and drying, 30 g of 3,7,11-trimethyl-dodeca-2E,4E,6E,10E-tetraen-1-yl-triphenyl phosphonium chloride (All E-C15TPPCl) salt powder were obtained. HPLC analysis revealed that the powder contains 94.8% of all-E isomer, 3.3% of 6Z isomer, and 1.9% of 2Z isomer. The E isomer/Z isomer ratio is accordingly 18.2:1.
- 1,534.0 g of a 3,7,11-trimethyldodeca-2,4,6,10-tetraen-1-yl-triphenylphosphonium chloride salt solution (purity 38.6% in methanol) with 42.6% of all-E isomer, 39.6% of 6Z and 2Z isomers (E isomer/Z isomer ratio=1.1:1) were concentrated by vacuum distillation at 30° C., followed by adding 400 ml of ethyl acetate and stirring for 16 hours. 400 ml of acetone were added and the mixture was stirred for additional 2 hours. After filtration, the obtained 230 g of solid phase 3,7,11-trimethyldodeca-2E,4E,6Z,10E-tetraen-1-yl-triphenylphosphonium chloride salt wet cake were removed and an filtrate was obtained. The filtrate was then concentrated by vacuum distillation at 45° C., to remove the solvent, whereby 640 g of residue (purity of C15 salts: 55.2%) were obtained. HPLC analysis revealed that the residue contains 77.2% of all-E isomer, 13.8% of 6Z isomer and 9.0% of 2Z isomer. Its E isomer/Z isomer ratio is accordingly 3.4:1.
- 500.0 g of 3,7,11 -trimethyldodeca-2E,4E,6Z,10E-tetraen-1-yl-triphenylphosphonium chloride salt wet cake obtained from example 1, with 12.0% of all-E isomer, 73.3% of 6Z isomer and 0.3% of 2Z isomer (E isomer/Z isomer ratio=1:6.1) was suspended in 1,000 ml of acetone. The salt solution was then heated to 40° C. and stirred for 1 hour. After filtration and drying, 362.g of 3,7,11-trimethylodeca-2E,4E,6Z,10E-tetraen-1-yl-triphenyl phosphonium chloride salt powder were obtained. HPLC analysis revealed that the powder obtained C15 phosphonium salt powder contained 2.9% of all-E isomer, 96.8% of 6Z isomer and 0.3% of 2Z isomer. The E isomer/Z isomer ratio is accordingly 1:33.5.
- 89.0 g of 3,7,11-trimethyldodeca-2E,4E,6E,10E-tetraen-1-yl-triphenylphosphonium chloride salt powder (purity 95.2%, E isomer/Z isomer ratio=15.8:1) and 9.3 g of 2,7-dimethyl-2,4,6-octatriene-1,8-dial were added into 90 g of methanol. The temperature of the composition was raised to 30° C. and maintained for 30 minutes. After 95 g of an ethyl acetate/n-heptane (w/w=1:1) solvent mixture were added, the solution mixture was cooled to room temperature. Then 175.5 g of a potassium carbonate solution by dissolving 63.5 g of potassium carbonate powder in 112 g of water were added dropwise. The solution mixture was then heated to 60° C. and maintained for 3 hours. Thereafter, the temperature of the solution mixture was raised to 100° C. to remove as much organic solvents as possible, then cooled to 80° C. and maintained for 16 hours. After filtration, 94.3 g of high all-E-lycopene wet cake were obtained. Acetone and water were added to the wet cake separately for washing and rinsing treatments. After filtration and drying, 24.5 g of high all-E-lycopene crystal were obtained. HPLC analysis revealed the lycopene crystal contained 95.3% of all-E-lycopene, and 3.3% of 5Z-lycopene. UV assay of the lycopene=101.0%.
- 50.0 g of 3,7,11 -trimethyldodeca-2E,4E,6Z,10E-tetraen-1-yl-triphenylphosphonium chloride salt powder (purity 89.8%, E isomer/Z isomer ratio=1:33.1) and 5.4 g of 2,7-dimethyl-2,4,6-octatriene-1,8-dial were added into 60 ml of methanol. The temperature of the composition was raised to 30° C. and maintained for 30 minutes. After 55 g of an ethyl acetate/n-heptane (w/w=1:1) solvent mixture were added, the solution mixture was cooled to room temperature. Then 103.5 g of a potassium carbonate solution by dissolving 37.5 g of potassium carbonate powder in 66 g of water were added dropwise. The solution mixture was heated to 60° C. and maintained for 3 hours. Thereafter, the temperature of the solution mixture was raised to 100° C. to remove as much organic solvents as possible, then cooled to 80° C. and maintained for 16 hours. After filtration 62.0 g of 5Z-lycopene wet cake were obtained. Acetone and water were added to the wet cake separately for washing and rinsing treatments. After filtration and drying, 16.1 g of high 5Z-lycopene containing crystal were obtained. HPLC analysis revealed the lycopene crystal contained 97.9% of 5Z-lycopene and 1.4% of other Z-isomers. U V assay of the lycopene=100.5%.
- 203.0 g of 3,7,11-trimethyldodeca-2,4,6,10-tetraen-1-yl-triphenylphosphonium chloride salt solution (purity 58.4%, E isomer/Z isomer ratio=3.4:1) and 14.4 g of 2,7-dimethyl-2,4,6-octatriene-1,8-dial were added into 55 ml of methanol. After 316 ml of an ethyl acetate/n-heptane (w/w=1:1) solvent mixture were added, the solution mixture was heated to 30° C. Then 470.0 g of a potassium carbonate solution by dissolving 170.0 g of potassium carbonate powder in 300 g of water were added dropwise. The solution mixture was heated to 60° C. and stirred for 3 hours. Thereafter, the temperature of the solution mixture was raised to 100° C. to remove as much organic solvents as possible, then cooled to 80° C. and stirred for 16 hours. 95.9 g of lycopene wet cake were obtained by filtration. Acetone and water were added to the wet cake separately for washing and rinsing treatments. After filtration and drying, 24.6 g of synthetic lycopene crystal were obtained. HPLC analysis revealed the lycopene crystal contained 75.7% of all-E-lycopene, 19.2% of 5Z-lycopene and 3.1% of other Z-isomers. UV assay of the lycopene=99.0%.
- Lycopene is one of the many carotenoids that may alleviate coronary heart disease and prevent from several kinds of cancers. It can be produced by way of either extraction or synthesis. Current synthesis processes can produce synthetic lycopenes with all-E content of merely 87%, which is much lower than that of the biological lycopene extracted from B. trispora/natural source. This invention makes the synthetic lycopene to meet the all-E content standard for biological lycopene extracted from B. trispora/natural source, by separating the all-E-C15-Wittig salts from the C15 phosphonium salts cis/trans mixture through a series of purification operations in aprotic solvents such as ethyl acetate, chloroform, acetone, methyl ethyl ketone, methyl isobutyl ketone, etc. The C15-Wittig salts so obtained include significantly high all-E content or high 6Z content. A C10-dialdehyde is then reacting with the high all-E containing or high 6Z containing C15 phosphonium salts in a double Wittig reaction, to obtain synthesized all-E-lycopenes or 5Z-lycopenes.
Claims (4)
1. A product of lycopene crystals produced directly from a chemical synthesis process and containing an all-E content of at least 95% (HPLC area %).
2. The product according to claim 1 , formulated as one selected from the group consisted of a tablet, a capsule, emulsion water and an oil.
3. A product of lycopene crystals produced directly from a chemical synthesis process and containing a 5Z content of at least 95% (HPLC area %).
4. The product according to claim 3 , formulated as one selected from the group consisted of a tablet, a capsule, emulsion water and an oil.
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CN112957766A (en) * | 2021-02-22 | 2021-06-15 | 新疆农业职业技术学院 | Lycopene extraction |
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DE19734446A1 (en) * | 1997-08-08 | 1999-02-11 | Basf Ag | Process for the preparation of phosphonium salts |
DE10103708A1 (en) * | 2001-01-26 | 2002-08-01 | Basf Ag | Thermal isomerization of lycopene |
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US20160145173A1 (en) | 2016-05-26 |
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