CN115197186A - Preparation method of biomass-based pyranoside derivative - Google Patents
Preparation method of biomass-based pyranoside derivative Download PDFInfo
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- CN115197186A CN115197186A CN202110388743.0A CN202110388743A CN115197186A CN 115197186 A CN115197186 A CN 115197186A CN 202110388743 A CN202110388743 A CN 202110388743A CN 115197186 A CN115197186 A CN 115197186A
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- molybdenum
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- 239000002028 Biomass Substances 0.000 title claims abstract description 16
- RYVMUASDIZQXAA-UHFFFAOYSA-N pyranoside Natural products O1C2(OCC(C)C(OC3C(C(O)C(O)C(CO)O3)O)C2)C(C)C(C2(CCC3C4(C)CC5O)C)C1CC2C3CC=C4CC5OC(C(C1O)O)OC(CO)C1OC(C1OC2C(C(OC3C(C(O)C(O)C(CO)O3)O)C(O)C(CO)O2)O)OC(CO)C(O)C1OC1OCC(O)C(O)C1O RYVMUASDIZQXAA-UHFFFAOYSA-N 0.000 title claims abstract description 16
- 238000002360 preparation method Methods 0.000 title claims abstract description 10
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims abstract description 72
- 238000006243 chemical reaction Methods 0.000 claims abstract description 42
- 239000003054 catalyst Substances 0.000 claims abstract description 41
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000002994 raw material Substances 0.000 claims abstract description 28
- 238000000034 method Methods 0.000 claims abstract description 26
- 239000008367 deionised water Substances 0.000 claims abstract description 24
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 24
- 150000001720 carbohydrates Chemical class 0.000 claims abstract description 19
- 239000002904 solvent Substances 0.000 claims abstract description 19
- 150000004696 coordination complex Chemical class 0.000 claims abstract description 17
- 239000011968 lewis acid catalyst Substances 0.000 claims abstract description 16
- 230000009471 action Effects 0.000 claims abstract description 4
- CREMABGTGYGIQB-UHFFFAOYSA-N carbon carbon Chemical compound C.C CREMABGTGYGIQB-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000011203 carbon fibre reinforced carbon Substances 0.000 claims abstract description 4
- 230000008878 coupling Effects 0.000 claims abstract description 4
- 238000010168 coupling process Methods 0.000 claims abstract description 4
- 238000005859 coupling reaction Methods 0.000 claims abstract description 4
- 238000005906 dihydroxylation reaction Methods 0.000 claims abstract description 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 27
- 238000003756 stirring Methods 0.000 claims description 23
- -1 tetra (p-methylphenyl) porphyrin molybdenum Chemical compound 0.000 claims description 17
- 238000004821 distillation Methods 0.000 claims description 14
- 238000001914 filtration Methods 0.000 claims description 13
- SRBFZHDQGSBBOR-IOVATXLUSA-N D-xylopyranose Chemical compound O[C@@H]1COC(O)[C@H](O)[C@H]1O SRBFZHDQGSBBOR-IOVATXLUSA-N 0.000 claims description 12
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 9
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 9
- 239000008103 glucose Substances 0.000 claims description 9
- 239000002808 molecular sieve Substances 0.000 claims description 9
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 9
- PYMYPHUHKUWMLA-UHFFFAOYSA-N arabinose Natural products OCC(O)C(O)C(O)C=O PYMYPHUHKUWMLA-UHFFFAOYSA-N 0.000 claims description 8
- SRBFZHDQGSBBOR-UHFFFAOYSA-N beta-D-Pyranose-Lyxose Natural products OC1COC(O)C(O)C1O SRBFZHDQGSBBOR-UHFFFAOYSA-N 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 8
- 230000002572 peristaltic effect Effects 0.000 claims description 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 6
- 229910052750 molybdenum Inorganic materials 0.000 claims description 6
- 239000011733 molybdenum Substances 0.000 claims description 6
- OWEGMIWEEQEYGQ-UHFFFAOYSA-N 100676-05-9 Natural products OC1C(O)C(O)C(CO)OC1OCC1C(O)C(O)C(O)C(OC2C(OC(O)C(O)C2O)CO)O1 OWEGMIWEEQEYGQ-UHFFFAOYSA-N 0.000 claims description 4
- GUBGYTABKSRVRQ-PICCSMPSSA-N Maltose Natural products O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-PICCSMPSSA-N 0.000 claims description 4
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 4
- DGEZNRSVGBDHLK-UHFFFAOYSA-N [1,10]phenanthroline Chemical compound C1=CN=C2C3=NC=CC=C3C=CC2=C1 DGEZNRSVGBDHLK-UHFFFAOYSA-N 0.000 claims description 4
- MNSFATSRSQVCJF-UHFFFAOYSA-N C1(=CC=CC=C1)C1=C2C=CC(C(=C3C=CC(=C(C=4C=CC(=C(C5=CC=C1N5)C5=CC=CC=C5)N4)C4=CC=CC=C4)N3)C3=CC=CC=C3)=N2.[Mo] Chemical compound C1(=CC=CC=C1)C1=C2C=CC(C(=C3C=CC(=C(C=4C=CC(=C(C5=CC=C1N5)C5=CC=CC=C5)N4)C4=CC=CC=C4)N3)C3=CC=CC=C3)=N2.[Mo] MNSFATSRSQVCJF-UHFFFAOYSA-N 0.000 claims description 3
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 claims description 3
- GUBGYTABKSRVRQ-QUYVBRFLSA-N beta-maltose Chemical compound OC[C@H]1O[C@H](O[C@H]2[C@H](O)[C@@H](O)[C@H](O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@@H]1O GUBGYTABKSRVRQ-QUYVBRFLSA-N 0.000 claims description 3
- YNCPOLRISDJRKS-UHFFFAOYSA-N molybdenum;quinolin-8-ol Chemical compound [Mo].C1=CN=C2C(O)=CC=CC2=C1 YNCPOLRISDJRKS-UHFFFAOYSA-N 0.000 claims description 3
- 150000004032 porphyrins Chemical class 0.000 claims description 3
- GUBGYTABKSRVRQ-XLOQQCSPSA-N Alpha-Lactose Chemical compound O[C@@H]1[C@@H](O)[C@@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)O[C@H](O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-XLOQQCSPSA-N 0.000 claims description 2
- GUBGYTABKSRVRQ-CUHNMECISA-N D-Cellobiose Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-CUHNMECISA-N 0.000 claims description 2
- WQZGKKKJIJFFOK-QTVWNMPRSA-N D-mannopyranose Chemical compound OC[C@H]1OC(O)[C@@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-QTVWNMPRSA-N 0.000 claims description 2
- GUBGYTABKSRVRQ-QKKXKWKRSA-N Lactose Natural products OC[C@H]1O[C@@H](O[C@H]2[C@H](O)[C@@H](O)C(O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@H]1O GUBGYTABKSRVRQ-QKKXKWKRSA-N 0.000 claims description 2
- WQZGKKKJIJFFOK-PHYPRBDBSA-N alpha-D-galactose Chemical compound OC[C@H]1O[C@H](O)[C@H](O)[C@@H](O)[C@H]1O WQZGKKKJIJFFOK-PHYPRBDBSA-N 0.000 claims description 2
- PYMYPHUHKUWMLA-WDCZJNDASA-N arabinose Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)C=O PYMYPHUHKUWMLA-WDCZJNDASA-N 0.000 claims description 2
- XOYLJNJLGBYDTH-UHFFFAOYSA-M chlorogallium Chemical compound [Ga]Cl XOYLJNJLGBYDTH-UHFFFAOYSA-M 0.000 claims description 2
- 229930182830 galactose Natural products 0.000 claims description 2
- 239000008101 lactose Substances 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims 4
- 239000000203 mixture Substances 0.000 claims 1
- 230000008569 process Effects 0.000 abstract description 6
- 239000007788 liquid Substances 0.000 description 14
- 239000000243 solution Substances 0.000 description 14
- 229910001220 stainless steel Inorganic materials 0.000 description 9
- 239000010935 stainless steel Substances 0.000 description 9
- 239000012295 chemical reaction liquid Substances 0.000 description 8
- 238000002156 mixing Methods 0.000 description 8
- 238000005086 pumping Methods 0.000 description 7
- 238000007789 sealing Methods 0.000 description 7
- 239000011949 solid catalyst Substances 0.000 description 7
- 229910052723 transition metal Inorganic materials 0.000 description 7
- 150000003624 transition metals Chemical class 0.000 description 7
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 6
- YRKCREAYFQTBPV-UHFFFAOYSA-N acetylacetone Chemical compound CC(=O)CC(C)=O YRKCREAYFQTBPV-UHFFFAOYSA-N 0.000 description 6
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 5
- 229930182476 C-glycoside Natural products 0.000 description 4
- 150000000700 C-glycosides Chemical class 0.000 description 4
- DDADCBXAKYGDEH-UHFFFAOYSA-N 2-(3-hydroxypropyl)oxane-2,3,4-triol Chemical compound OCCCC1(O)OCCC(O)C1O DDADCBXAKYGDEH-UHFFFAOYSA-N 0.000 description 3
- 238000005580 one pot reaction Methods 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 3
- 239000002537 cosmetic Substances 0.000 description 2
- NZZIMKJIVMHWJC-UHFFFAOYSA-N dibenzoylmethane Chemical compound C=1C=CC=CC=1C(=O)CC(=O)C1=CC=CC=C1 NZZIMKJIVMHWJC-UHFFFAOYSA-N 0.000 description 2
- 229940079593 drug Drugs 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- XYIBRDXRRQCHLP-UHFFFAOYSA-N ethyl acetoacetate Chemical compound CCOC(=O)CC(C)=O XYIBRDXRRQCHLP-UHFFFAOYSA-N 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 125000002524 organometallic group Chemical group 0.000 description 2
- 230000002195 synergetic effect Effects 0.000 description 2
- 230000002194 synthesizing effect Effects 0.000 description 2
- HSTXOEHMFRWNEO-UHFFFAOYSA-L Cl[Mo](=O)(=O)Cl.N1=CC=CC2=CC=C3C=CC=NC3=C12 Chemical compound Cl[Mo](=O)(=O)Cl.N1=CC=CC2=CC=C3C=CC=NC3=C12 HSTXOEHMFRWNEO-UHFFFAOYSA-L 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 238000010523 cascade reaction Methods 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- CNRRZWMERIANGJ-UHFFFAOYSA-N chloro hypochlorite;molybdenum Chemical compound [Mo].ClOCl CNRRZWMERIANGJ-UHFFFAOYSA-N 0.000 description 1
- 238000006114 decarboxylation reaction Methods 0.000 description 1
- 125000004185 ester group Chemical group 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- 239000003446 ligand Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- BQBYSLAFGRVJME-UHFFFAOYSA-L molybdenum(2+);dichloride Chemical compound Cl[Mo]Cl BQBYSLAFGRVJME-UHFFFAOYSA-L 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229910052706 scandium Inorganic materials 0.000 description 1
- SIXSYDAISGFNSX-UHFFFAOYSA-N scandium atom Chemical compound [Sc] SIXSYDAISGFNSX-UHFFFAOYSA-N 0.000 description 1
- 229910000033 sodium borohydride Inorganic materials 0.000 description 1
- 239000012279 sodium borohydride Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 238000007039 two-step reaction Methods 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D309/00—Heterocyclic compounds containing six-membered rings having one oxygen atom as the only ring hetero atom, not condensed with other rings
- C07D309/02—Heterocyclic compounds containing six-membered rings having one oxygen atom as the only ring hetero atom, not condensed with other rings having no double bonds between ring members or between ring members and non-ring members
- C07D309/08—Heterocyclic compounds containing six-membered rings having one oxygen atom as the only ring hetero atom, not condensed with other rings having no double bonds between ring members or between ring members and non-ring members with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D309/10—Oxygen atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
- C07H1/00—Processes for the preparation of sugar derivatives
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
- C07H15/00—Compounds containing hydrocarbon or substituted hydrocarbon radicals directly attached to hetero atoms of saccharide radicals
- C07H15/26—Acyclic or carbocyclic radicals, substituted by hetero rings
-
- 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
- C07B2200/07—Optical isomers
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Biotechnology (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Molecular Biology (AREA)
- Saccharide Compounds (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
The invention discloses a preparation method of a biomass-based pyranoside derivative. In particular to a method for obtaining pyranoside derivatives by taking carbohydrate and glycerol as raw materials and carrying out multi-step series reaction of selective dehydroxylation and carbon-carbon coupling in solvent deionized water under the action of an organic metal complex catalyst and a Lewis acid catalyst. The raw materials used in the method can be completely derived from biomass resources, and the method is simple in process, high in economy and wide in application prospect.
Description
Technical Field
The invention relates to the fields of organic synthesis, efficient utilization of biomass resources, fine chemical engineering, medicines, daily cosmetics and the like, relates to a preparation method of a biomass-based pyranoside derivative, and particularly relates to a method for obtaining the pyranoside derivative by taking carbohydrate and glycerol as raw materials through continuous multi-step tandem reaction.
Background
The C-glucoside has excellent biological activity, better acid-resistant and enzyme-catalyzed hydrolysis performance, and important application in organic synthesis, biomedicine and daily cosmetic industries. However, the methods of C-glycoside synthesis reported in the literature are limited. Wherein, US20040048785A1 discloses a method for synthesizing C-glycoside derivatives by taking xylose and acetylacetone or dibenzoylmethane as raw materials through two-step reaction. CN202010643748.9 discloses a synthesis method of hydroxypropyl tetrahydropyrane triol, which is similar to that of US20040048785A1, and xylose and acetylacetone are used as raw materials to obtain the hydroxypropyl tetrahydropyrane triol under the continuous action of alkali and sodium borohydride. CN201910785216.6 discloses a method for preparing a product hydroxypropyl tetrahydropyrane triol (vitriol) by using xylose and ethyl acetoacetate as raw materials and a metal scandium complex as a catalyst and promoting hydrolysis decarboxylation of an ester group and carbonyl reduction. CN202010629023.4 discloses a method for preparing C-pyranoside, namely vitreoside, by using a one-pot method of reaction of xylose and isopropanol catalyzed by a biological enzyme. In the above process for synthesizing the C-glycoside derivative, the acetylacetone, dibenzoylmethane, ethyl acetoacetate, and isopropyl alcohol used are derived from fossil resources, and it is difficult to obtain 100% biomass-based C-glycoside derivatives. Therefore, it is very important to develop a preparation method of biomass-based C-glucoside derivatives with high efficiency, convenience and high economy.
Disclosure of Invention
The invention aims to provide a preparation method of biomass-based pyranoside derivatives, which specifically comprises the step of carrying out one-pot multi-step series reaction of selective dehydroxylation and carbon-carbon coupling in a deionized water solvent by taking carbohydrate and glycerol as raw materials under the action of an organic metal complex catalyst and a Lewis acid catalyst to obtain the pyranoside derivatives.
In order to achieve the purpose, the technical scheme adopted by the invention is as follows:
the specific process method comprises the following steps: mixing the components in a molar ratio of 1:3 to 3: the method comprises the following steps of 1, sequentially adding a saccharide carbohydrate and glycerol reaction raw material, a deionized water solvent (the mass ratio of the saccharide carbohydrate raw material to the deionized water solvent is 1. After the reaction is stopped, filtering reaction liquid to remove a Lewis acid catalyst, extracting with ethyl acetate for three times to remove an organic metal complex catalyst, collecting a water layer, distilling under reduced pressure to remove solvent water to obtain light yellow oily liquid, dissolving with absolute ethyl alcohol, filtering to remove unreacted raw materials, and distilling and concentrating under reduced pressure to obtain a target product C-pyranoside derivative; the examples of the present invention were subjected to performance evaluation and process condition testing in a stainless steel reaction vessel, but are not limited to the stainless steel reaction vessel.
The carbohydrate is selected from one of glucose, mannose, galactose, xylose, arabinose, lactose, maltose and cellobiose;
the organic metal complex catalyst is selected from at least one of 8-hydroxyquinoline molybdenum, 1, 10-phenanthroline dichloro-dioxy-molybdenum, tetraphenyl porphyrin molybdenum, tetra (p-alkoxy phenyl) porphyrin molybdenum, tetra (p-methylphenyl) porphyrin molybdenum and tetra (p-chlorophenyl) porphyrin molybdenum;
the Lewis acid catalyst is at least one of an anhydrous chloride catalyst or a molecular sieve catalyst;
the anhydrous chloride catalyst is selected from anhydrous SnCl 4 、TiCl 4 、LaCl 3 、GaCl 3 、AlCl 3 At least one of;
the molecular sieve catalyst is at least one of H beta, sn beta and Zr beta molecular sieves.
Optionally, the lower limit of the mass ratio of the carbohydrate to the deionized water solvent is selected from 1; the upper limit is selected from 2;
optionally, the lower limit of the molar ratio of carbohydrate to glycerol is selected from 1; the upper limit is selected from 3;
optionally, the lower limit of the molar ratio of the amount of the organometallic complex catalyst to the saccharide carbohydrate raw material is selected from the group consisting of 1; the upper limit is selected from 1,10, 1;
optionally, the lower limit of the molar ratio of the anhydrous chloride catalyst to the carbohydrate raw material is selected from 1; the upper limit is selected from 1, 1;
optionally, the lower limit of the mass ratio of the amount of the molecular sieve catalyst to the carbohydrate feedstock is selected from 1; the upper limit is selected from 1, 1;
optionally, the reaction temperature is 150 ℃.
Optionally, the reaction time is 12 hours.
Compared with the route of the prior art, the method has the following characteristics:
the invention provides a preparation method of a biomass-based pyranoside derivative, which specifically comprises the steps of taking carbohydrate and glycerol as raw materials, and carrying out selective deoxidation and carbon-carbon coupling multistep series reaction in a deionized water solvent under the synergistic action of an organic metal complex catalyst and a Lewis acid catalyst to obtain the pyranoside derivative. The raw materials can be completely derived from biomass resources, the process is simple, the solvent is green, the operability is strong, and the method has a large-scale prospect.
Detailed Description
The following examples will aid in the understanding of the invention, but the summary of the invention is not limited thereto.
Unless otherwise specified, the raw materials and catalysts in the examples of the present application were all purchased commercially.
Saccharides such as glucose and maltose are available from Shanghai Aladdin Biotechnology, inc.
Anhydrous SnCl 4 、LaCl 3 And the like are purchased from chemical agents of the national drug group, ltd.
Molecular sieves, hbeta, zr beta, sn beta, etc., were purchased from tianjin south chemical catalyst, inc.
The organometallic complex catalyst is prepared by ligand exchange method from 8-hydroxyquinoline molybdenum, 1, 10-phenanthroline dichloro-molybdenum dioxide, tetraphenyl porphyrin molybdenum, tetra (p-alkoxy phenyl) porphyrin molybdenum, tetra (p-methylphenyl) porphyrin molybdenum, tetra (p-chlorophenyl) porphyrin molybdenum and the like. Taking a typical preparation process of 1, 10-phenanthroline dimolybdenum as an example, 0.1mol of molybdenum dichloride and 1, 10-phenanthroline are dissolved in 100mL of tetrahydrofuran respectively and are completely dissolved to prepare two parts of solution. Adding the tetrahydrofuran solution of molybdenum oxydichloride into the tetrahydrofuran solution of 1, 10-phenanthroline while stirring. After the addition, the mixed solution was stirred at room temperature for 24 hours. After stirring, filtering and washing to obtain a light pink solid. Vacuum drying at 25 deg.C overnight to obtain 1, 10-phenanthroline dichloro molybdenum.
The yield of the pyranoside derivative was calculated according to the following formula:
example 1
Completely dissolving 1.08kg of glucose in 3.00kg of deionized water, adding into a 20L stainless steel reaction kettle, and stirring for dissolving; dissolving 0.36kg of glycerol in 3.00kg of deionized water, pumping the glycerol solution into a reaction kettle by using a peristaltic pump while stirring, and uniformly mixing. Adding 0.05kg of transition metal catalyst 1, 10-phenanthroline dichloro-molybdenum and 0.09kg of Lewis acid catalyst anhydrous LaCl 3 And sealing the reaction kettle, stirring, heating to 150 ℃, and reacting for 12 hours. After the reaction is stopped, the reaction liquid is filtered to remove the solid catalyst, ethyl acetate is extracted for three times (each dosage is 0.5L) to remove the organic metal complex catalyst, a water layer is collected, the solvent is removed by reduced pressure distillation to obtain light yellow oily liquid, the light yellow oily liquid is dissolved by 1L of absolute ethyl alcohol, unreacted raw materials are removed by filtration, the reduced pressure distillation and concentration are carried out to obtain 0.45kg of the target product C-glucopyranoside derivative, and the yield is 33.8%.
Example 2
Completely dissolving 1.08kg of glucose in 3.00kg of deionized water, adding the solution into a 20L stainless steel reaction kettle, and stirring and dissolving; dissolving 0.36kg of glycerol in 3.00kg of deionized water, and pumping the glycerol solution into a reaction kettle by using a peristaltic pump while stirringAnd (4) uniformly mixing. Adding 0.05kg of transition metal catalyst 1, 10-phenanthroline dichloro-molybdenum and 0.10kg of Lewis acid catalyst anhydrous SnCl 4 And sealing the reaction kettle, stirring, heating to 150 ℃, and reacting for 12 hours. After the reaction is stopped, the reaction liquid is filtered to remove the solid catalyst, ethyl acetate is extracted for three times (each dosage is 0.5L) to remove the organic metal complex catalyst, a water layer is collected, the solvent is removed by reduced pressure distillation to obtain light yellow oily liquid, the light yellow oily liquid is dissolved by 1L of absolute ethyl alcohol, unreacted raw materials are removed by filtration, the reduced pressure distillation and concentration are carried out to obtain 0.96kg of the target product C-glucopyranoside derivative, and the yield is 72.1%.
Example 3
Completely dissolving 1.08kg of glucose in 3.00kg of deionized water, adding into a 20L stainless steel reaction kettle, and stirring for dissolving; dissolving 0.36kg of glycerol in 3.00kg of deionized water, pumping the glycerol solution into a reaction kettle by using a peristaltic pump while stirring, and uniformly mixing. Adding 0.05kg of transition metal catalyst 1, 10-phenanthroline dichloro molybdenum and 0.10kg of Lewis acid catalyst H beta, sealing the reaction kettle, stirring, heating to 150 ℃, and reacting for 12 hours. After the reaction is stopped, the reaction liquid is filtered to remove the solid catalyst, ethyl acetate is extracted for three times (each dosage is 0.5L) to remove the organic metal complex catalyst, a water layer is collected, the solvent is removed by reduced pressure distillation to obtain light yellow oily liquid, the light yellow oily liquid is dissolved by 1L of absolute ethyl alcohol, unreacted raw materials are removed by filtration, the reduced pressure distillation and concentration are carried out to obtain 0.83kg of the target product C-glucopyranoside derivative, and the yield is 62.3%.
Example 4
Completely dissolving 1.08kg of glucose in 3.00kg of deionized water, adding the solution into a 20L stainless steel reaction kettle, and stirring and dissolving; dissolving 0.36kg of glycerol in 3.00kg of deionized water, pumping the glycerol solution into a reaction kettle by using a peristaltic pump while stirring, and uniformly mixing. Adding 0.05kg of 1, 10-phenanthroline dichloro molybdenum oxide serving as a transition metal catalyst and 0.10kg of Zr beta serving as a Lewis acid catalyst, sealing the reaction kettle, stirring, heating to 150 ℃, and reacting for 12 hours. After the reaction is stopped, the reaction liquid is filtered to remove the solid catalyst, ethyl acetate is extracted for three times (each dosage is 0.5L) to remove the organic metal complex catalyst, a water layer is collected, the solvent is removed by reduced pressure distillation to obtain light yellow oily liquid, the light yellow oily liquid is dissolved by 1L of absolute ethyl alcohol, unreacted raw materials are removed by filtration, the reduced pressure distillation and concentration are carried out to obtain 1.01kg of the target product C-glucopyranoside derivative, and the yield is 76.0%.
Example 5
Completely dissolving 1.08kg of glucose in 3.00kg of deionized water, adding into a 20L stainless steel reaction kettle, and stirring for dissolving; dissolving 0.36kg of glycerol in 3.00kg of deionized water, pumping the glycerol solution into a reaction kettle by using a peristaltic pump while stirring, and uniformly mixing. Adding 0.05kg of transition metal catalyst 1, 10-phenanthroline dichloro molybdenum and 0.10kg of Lewis acid catalyst Sn beta, sealing the reaction kettle, stirring, heating to 150 ℃, and reacting for 12 hours. After the reaction is stopped, filtering the reaction liquid to remove the solid catalyst, extracting with ethyl acetate for three times (0.5L for each dosage) to remove the organic metal complex catalyst, collecting a water layer, distilling under reduced pressure to remove the solvent to obtain a light yellow oily liquid, dissolving with 1L of absolute ethyl alcohol, filtering to remove unreacted raw materials, distilling under reduced pressure and concentrating to obtain 1.21kg of the target product C-glucopyranoside derivative, wherein the yield is 90.8%.
Example 6
Completely dissolving 1.08kg of glucose in 3.00kg of deionized water, adding the solution into a 20L stainless steel reaction kettle, and stirring and dissolving; dissolving 0.36kg of glycerol in 3.00kg of deionized water, pumping the glycerol solution into a reaction kettle by using a peristaltic pump while stirring, and uniformly mixing. Adding 0.06kg of transition metal catalyst octohydroxyquinoline molybdenum and 0.10kg of Lewis acid catalyst Sn beta, sealing the reaction kettle, stirring, heating to 150 ℃, and reacting for 12 hours. After the reaction is stopped, the reaction liquid is filtered to remove the solid catalyst, ethyl acetate is extracted for three times (each dosage is 0.5L) to remove the organic metal complex catalyst, a water layer is collected, the solvent is removed by reduced pressure distillation to obtain light yellow oily liquid, the light yellow oily liquid is dissolved by 1L of absolute ethyl alcohol, unreacted raw materials are removed by filtration, the reduced pressure distillation and concentration are carried out to obtain 0.66kg of the target product C-glucopyranoside derivative, and the yield is 49.5%.
Example 7
Completely dissolving 2.05kg of maltose in 3.00kg of deionized water, adding the solution into a 20L stainless steel reaction kettle, and stirring and dissolving; dissolving 0.36kg of glycerol in 3.00kg of deionized water, pumping the glycerol solution into a reaction kettle by using a peristaltic pump while stirring, and uniformly mixing. Adding 0.05kg of transition metal catalyst 1, 10-phenanthroline dichloro molybdenum and 0.23kg of Lewis acid catalyst Sn beta, sealing the reaction kettle, stirring, heating to 150 ℃, and reacting for 12 hours. After the reaction is stopped, the reaction liquid is filtered to remove the solid catalyst, ethyl acetate is extracted for three times (each dosage is 0.5L) to remove the organic metal complex catalyst, a water layer is collected, the solvent is removed by reduced pressure distillation to obtain light yellow oily liquid, the light yellow oily liquid is dissolved by 1L of absolute ethyl alcohol, unreacted raw materials are removed by filtration, the reduced pressure distillation and concentration are carried out to obtain 1.90kg of the target product C-maltopyranoside derivative, and the yield is 82.5%.
In summary, the application provides a preparation method of a full biomass-based pyranoside derivative, which takes carbohydrate and glycerol as raw materials, and carries out one-pot multi-step series reaction in a deionized water solvent under the synergistic action of an organic metal complex catalyst and a Lewis acid catalyst to obtain the pyranoside derivative. The raw materials can be completely from biomass resources, the process is simple and green, the operability is strong, and the method has a large-scale prospect.
Although the present application has been described with reference to a few embodiments, it should be understood that various changes, substitutions and alterations can be made herein without departing from the spirit and scope of the application as defined by the appended claims.
Claims (10)
1. A preparation method of biomass-based pyranoside derivatives is characterized by at least comprising the following steps: the biomass-based pyranoside derivative is obtained by taking a mixture containing carbohydrate and glycerol as a raw material and performing multi-step series reaction of selective dehydroxylation and carbon-carbon coupling in a solvent under the action of an organic metal complex catalyst and a Lewis acid catalyst.
2. The method of claim 1, wherein:
the carbohydrate is selected from one of glucose, mannose, galactose, xylose, arabinose, lactose, maltose and cellobiose;
the organic metal complex catalyst is selected from at least one of 8-hydroxyquinoline molybdenum, 1, 10-phenanthroline dichloro-dioxy-molybdenum, tetraphenyl porphyrin molybdenum, tetra (p-alkoxy phenyl) porphyrin molybdenum, tetra (p-methylphenyl) porphyrin molybdenum and tetra (p-chlorophenyl) porphyrin molybdenum;
the Lewis acid catalyst is at least one of an anhydrous chloride catalyst or a molecular sieve catalyst;
the anhydrous chloride catalyst is selected from anhydrous SnCl 4 、TiCl 4 、LaCl 3 、GaCl 3 、AlCl 3 At least one of (a);
the molecular sieve catalyst is at least one of H beta, sn beta and Zr beta molecular sieves;
the solvent is deionized water.
3. The production method according to claim 1, characterized in that: at least comprises the following steps: adding carbohydrate into deionized water, stirring for dissolving, simultaneously adding glycerol by using a peristaltic pump, adding an organic metal complex catalyst and a Lewis acid catalyst, and heating for reaction;
and after the reaction is finished, filtering, extracting with ethyl acetate, collecting a water layer, dissolving with absolute ethyl alcohol after reduced pressure distillation, filtering, and then carrying out reduced pressure distillation to obtain the biomass-based pyranoside derivative.
4. The production method according to claim 2, characterized in that: the mass ratio of the carbohydrate to the deionized water solvent is 1:100 to 2:1.
5. the method of claim 1, wherein: the molar ratio of the carbohydrate to the glycerol is 1:3 to 3:1.
6. the production method according to claim 1, characterized in that: the molar ratio of the dosage of the organic metal complex catalyst to the carbohydrate raw material is 1:100 to 1:10.
7. the production method according to claim 2, characterized in that: the molar ratio of the consumption of the anhydrous chloride catalyst to the carbohydrate raw material is 1: 200-1: 1.
8. the method of claim 2, wherein: the mass ratio of the dosage of the molecular sieve catalyst to the carbohydrate raw material is 1:100 to 1:1.
9. the method of claim 1, wherein: the reaction temperature is 30-200 ℃;
preferably 150 deg.c.
10. The method of claim 1, wherein: the reaction time is 0.5 to 24 hours;
preferably 12 hours.
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