CN115197185A - Preparation method of transition metal catalyzed pyranoside derivative - Google Patents
Preparation method of transition metal catalyzed pyranoside derivative Download PDFInfo
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- CN115197185A CN115197185A CN202110388197.0A CN202110388197A CN115197185A CN 115197185 A CN115197185 A CN 115197185A CN 202110388197 A CN202110388197 A CN 202110388197A CN 115197185 A CN115197185 A CN 115197185A
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- China
- Prior art keywords
- transition metal
- acetylacetonate
- deionized water
- isopropanol
- reaction
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- 229910052723 transition metal Inorganic materials 0.000 title claims abstract description 26
- 150000003624 transition metals Chemical class 0.000 title claims abstract description 26
- 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 14
- 238000002360 preparation method Methods 0.000 title claims abstract description 7
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims abstract description 60
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 43
- 239000003054 catalyst Substances 0.000 claims abstract description 34
- 239000008367 deionised water Substances 0.000 claims abstract description 33
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 33
- 238000000034 method Methods 0.000 claims abstract description 24
- 150000001720 carbohydrates Chemical class 0.000 claims abstract description 16
- 239000012046 mixed solvent Substances 0.000 claims abstract description 16
- 239000002994 raw material Substances 0.000 claims abstract description 12
- 239000000010 aprotic solvent Substances 0.000 claims abstract description 9
- 230000009471 action Effects 0.000 claims abstract description 5
- 238000005859 coupling reaction Methods 0.000 claims abstract description 5
- 230000018044 dehydration Effects 0.000 claims abstract description 5
- 238000006297 dehydration reaction Methods 0.000 claims abstract description 5
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 claims description 51
- 238000006243 chemical reaction Methods 0.000 claims description 45
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 30
- 238000004821 distillation Methods 0.000 claims description 14
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 13
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 12
- 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 11
- 239000008103 glucose Substances 0.000 claims description 11
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 10
- 229910052750 molybdenum Inorganic materials 0.000 claims description 10
- 239000011733 molybdenum Substances 0.000 claims description 10
- POILWHVDKZOXJZ-ARJAWSKDSA-M (z)-4-oxopent-2-en-2-olate Chemical compound C\C([O-])=C\C(C)=O POILWHVDKZOXJZ-ARJAWSKDSA-M 0.000 claims description 7
- 238000001291 vacuum drying Methods 0.000 claims description 7
- 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 6
- PYMYPHUHKUWMLA-UHFFFAOYSA-N arabinose Natural products OCC(O)C(O)C(O)C=O PYMYPHUHKUWMLA-UHFFFAOYSA-N 0.000 claims description 5
- SRBFZHDQGSBBOR-UHFFFAOYSA-N beta-D-Pyranose-Lyxose Natural products OC1COC(O)C(O)C1O SRBFZHDQGSBBOR-UHFFFAOYSA-N 0.000 claims description 5
- 238000001914 filtration Methods 0.000 claims description 5
- FSJSYDFBTIVUFD-SUKNRPLKSA-N (z)-4-hydroxypent-3-en-2-one;oxovanadium Chemical compound [V]=O.C\C(O)=C\C(C)=O.C\C(O)=C\C(C)=O FSJSYDFBTIVUFD-SUKNRPLKSA-N 0.000 claims description 4
- 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
- APUPEJJSWDHEBO-UHFFFAOYSA-P ammonium molybdate Chemical compound [NH4+].[NH4+].[O-][Mo]([O-])(=O)=O APUPEJJSWDHEBO-UHFFFAOYSA-P 0.000 claims description 3
- 229940010552 ammonium molybdate Drugs 0.000 claims description 3
- 235000018660 ammonium molybdate Nutrition 0.000 claims description 3
- 239000011609 ammonium molybdate Substances 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
- VZSXFJPZOCRDPW-UHFFFAOYSA-N carbanide;trioxorhenium Chemical compound [CH3-].O=[Re](=O)=O VZSXFJPZOCRDPW-UHFFFAOYSA-N 0.000 claims description 3
- FJDJVBXSSLDNJB-LNTINUHCSA-N cobalt;(z)-4-hydroxypent-3-en-2-one Chemical compound [Co].C\C(O)=C\C(C)=O.C\C(O)=C\C(C)=O.C\C(O)=C\C(C)=O FJDJVBXSSLDNJB-LNTINUHCSA-N 0.000 claims description 3
- CMTKJYPJPSONIT-UHFFFAOYSA-K trichlororuthenium;triphenylphosphane Chemical compound Cl[Ru](Cl)Cl.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 CMTKJYPJPSONIT-UHFFFAOYSA-K 0.000 claims description 3
- SHWZFQPXYGHRKT-FDGPNNRMSA-N (z)-4-hydroxypent-3-en-2-one;nickel Chemical compound [Ni].C\C(O)=C\C(C)=O.C\C(O)=C\C(C)=O SHWZFQPXYGHRKT-FDGPNNRMSA-N 0.000 claims description 2
- IYWJIYWFPADQAN-LNTINUHCSA-N (z)-4-hydroxypent-3-en-2-one;ruthenium Chemical compound [Ru].C\C(O)=C\C(C)=O.C\C(O)=C\C(C)=O.C\C(O)=C\C(C)=O IYWJIYWFPADQAN-LNTINUHCSA-N 0.000 claims description 2
- 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
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 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
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-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
- UNTBPXHCXVWYOI-UHFFFAOYSA-O azanium;oxido(dioxo)vanadium Chemical compound [NH4+].[O-][V](=O)=O UNTBPXHCXVWYOI-UHFFFAOYSA-O 0.000 claims description 2
- FQNHWXHRAUXLFU-UHFFFAOYSA-N carbon monoxide;tungsten Chemical group [W].[O+]#[C-].[O+]#[C-].[O+]#[C-].[O+]#[C-].[O+]#[C-].[O+]#[C-] FQNHWXHRAUXLFU-UHFFFAOYSA-N 0.000 claims description 2
- ILZSSCVGGYJLOG-UHFFFAOYSA-N cobaltocene Chemical compound [Co+2].C=1C=C[CH-]C=1.C=1C=C[CH-]C=1 ILZSSCVGGYJLOG-UHFFFAOYSA-N 0.000 claims description 2
- KZPXREABEBSAQM-UHFFFAOYSA-N cyclopenta-1,3-diene;nickel(2+) Chemical compound [Ni+2].C=1C=C[CH-]C=1.C=1C=C[CH-]C=1 KZPXREABEBSAQM-UHFFFAOYSA-N 0.000 claims description 2
- KTWOOEGAPBSYNW-UHFFFAOYSA-N ferrocene Chemical compound [Fe+2].C=1C=C[CH-]C=1.C=1C=C[CH-]C=1 KTWOOEGAPBSYNW-UHFFFAOYSA-N 0.000 claims description 2
- 229930182830 galactose Natural products 0.000 claims description 2
- GNOIPBMMFNIUFM-UHFFFAOYSA-N hexamethylphosphoric triamide Chemical compound CN(C)P(=O)(N(C)C)N(C)C GNOIPBMMFNIUFM-UHFFFAOYSA-N 0.000 claims description 2
- 239000008101 lactose Substances 0.000 claims description 2
- 229910052702 rhenium Inorganic materials 0.000 claims description 2
- UUUGYDOQQLOJQA-UHFFFAOYSA-L vanadyl sulfate Chemical compound [V+2]=O.[O-]S([O-])(=O)=O UUUGYDOQQLOJQA-UHFFFAOYSA-L 0.000 claims description 2
- 229940041260 vanadyl sulfate Drugs 0.000 claims description 2
- 229910000352 vanadyl sulfate Inorganic materials 0.000 claims description 2
- LZKLAOYSENRNKR-LNTINUHCSA-N iron;(z)-4-oxoniumylidenepent-2-en-2-olate Chemical compound [Fe].C\C(O)=C\C(C)=O.C\C(O)=C\C(C)=O.C\C(O)=C\C(C)=O LZKLAOYSENRNKR-LNTINUHCSA-N 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 claims 1
- 230000035484 reaction time Effects 0.000 claims 1
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 claims 1
- 235000014633 carbohydrates Nutrition 0.000 abstract 1
- 238000003756 stirring Methods 0.000 description 12
- 239000000047 product Substances 0.000 description 11
- 229910001220 stainless steel Inorganic materials 0.000 description 11
- 239000010935 stainless steel Substances 0.000 description 11
- 239000006227 byproduct Substances 0.000 description 9
- 239000012295 chemical reaction liquid Substances 0.000 description 9
- 238000002156 mixing Methods 0.000 description 9
- 230000002572 peristaltic effect Effects 0.000 description 9
- 239000002904 solvent Substances 0.000 description 9
- 238000005086 pumping Methods 0.000 description 8
- 238000000605 extraction Methods 0.000 description 6
- 229930182476 C-glycoside Natural products 0.000 description 5
- 150000000700 C-glycosides Chemical class 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 102000004190 Enzymes Human genes 0.000 description 3
- 108090000790 Enzymes Proteins 0.000 description 3
- 239000002537 cosmetic Substances 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- -1 glucoside compound Chemical class 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- 239000005740 Boscalid Substances 0.000 description 2
- 229940118790 boscalid Drugs 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 125000001570 methylene group Chemical group [H]C([H])([*:1])[*:2] 0.000 description 2
- 238000005580 one pot reaction Methods 0.000 description 2
- 125000004430 oxygen atom Chemical group O* 0.000 description 2
- CDVAIHNNWWJFJW-UHFFFAOYSA-N 3,5-diethoxycarbonyl-1,4-dihydrocollidine Chemical compound CCOC(=O)C1=C(C)NC(C)=C(C(=O)OCC)C1C CDVAIHNNWWJFJW-UHFFFAOYSA-N 0.000 description 1
- 102000005751 Alcohol Oxidoreductases Human genes 0.000 description 1
- 108010031132 Alcohol Oxidoreductases Proteins 0.000 description 1
- 101710088194 Dehydrogenase Proteins 0.000 description 1
- 102000003960 Ligases Human genes 0.000 description 1
- 108090000364 Ligases Proteins 0.000 description 1
- BAWFJGJZGIEFAR-NNYOXOHSSA-N NAD zwitterion Chemical compound NC(=O)C1=CC=C[N+]([C@H]2[C@@H]([C@H](O)[C@@H](COP([O-])(=O)OP(O)(=O)OC[C@@H]3[C@H]([C@@H](O)[C@@H](O3)N3C4=NC=NC(N)=C4N=C3)O)O2)O)=C1 BAWFJGJZGIEFAR-NNYOXOHSSA-N 0.000 description 1
- 229930182473 O-glycoside Natural products 0.000 description 1
- 150000008444 O-glycosides Chemical class 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- WYEMLYFITZORAB-UHFFFAOYSA-N boscalid Chemical compound C1=CC(Cl)=CC=C1C1=CC=CC=C1NC(=O)C1=CC=CN=C1Cl WYEMLYFITZORAB-UHFFFAOYSA-N 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 125000003636 chemical group Chemical group 0.000 description 1
- 239000005515 coenzyme Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- 229930182478 glucoside Natural products 0.000 description 1
- 229930182470 glycoside Natural products 0.000 description 1
- 150000002338 glycosides Chemical class 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229950006238 nadide Drugs 0.000 description 1
- 229930027945 nicotinamide-adenine dinucleotide Natural products 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- HYERJXDYFLQTGF-UHFFFAOYSA-N rhenium Chemical compound [Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re][Re] HYERJXDYFLQTGF-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000012360 testing method 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
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)
Abstract
The invention discloses a preparation method of a pyranoside derivative catalyzed by transition metal. In particular to a method for preparing pyranoside derivatives by one-step dehydration coupling reaction of carbohydrates and the like serving as raw materials and isopropanol in a mixed solvent system of deionized water and a dipolar aprotic solvent under the action of a transition metal catalyst. The method has the advantages of short route, mild conditions, high atom economy and good application prospect.
Description
Technical Field
The invention relates to the fields of organic synthesis, fine chemical industry, medicine, daily cosmetics and the like, relates to a preparation method of a pyranoside derivative catalyzed by a transition metal, and particularly relates to a method for obtaining the pyranoside derivative in one step by taking carbohydrate and isopropanol as raw materials and performing a dehydration coupling reaction under the action of a transition metal catalyst.
Background
The glucoside compound has important biological activity, and can be widely applied to the industries of medicine and cosmetics. The C-glycoside is an O-glycoside analogue in which the oxygen atom on the glycosidic bond is replaced by a methylene group, so that the C-glycoside molecule has good stability to acid and enzyme catalytic hydrolysis due to the fact that the oxygen atom of the glycoside is replaced by the methylene group. Currently, only limited C-glycoside synthesis methods are disclosed, and most require a hydrogenation step to obtain the final target product. CN202010629023.4 discloses a method for preparing C-pyranoside, namely boscalid, by using a biological enzyme one-pot method, and specifically, xylose and isopropanol are used as substrates, and corresponding C-pyranoside is generated under the catalytic action of isopropanol dehydrogenase, boscalid synthetase, carbonyl reductase and coenzyme nicotinamide adenine dinucleotide. However, the process needs the synergistic effect of multiple enzyme catalysts, and has the disadvantages of long flow, low efficiency, high cost and difficulty in realizing large-scale production. Therefore, the development of a simple, efficient and low-cost preparation method of the C-glycoside derivative is very important for the application of the C-glycoside derivative in the fields of medicine, cosmetic industry and the like.
Disclosure of Invention
The invention aims to provide a method for one-step obtaining pyranoside derivatives by taking carbohydrate and isopropanol as raw materials and performing dehydration coupling reaction under the action of a transition metal catalyst.
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 a mixture of 1:10 to 10: dissolving a carbohydrate and isopropanol reaction raw material of 1 in a mixed solvent system of deionized water and a dipolar aprotic solvent (the mass ratio of the carbohydrate and the mixed solvent is 1; 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 transition metal catalyst is selected from at least one of ferric acetylacetonate, nickel acetylacetonate, cobalt acetylacetonate, vanadyl acetylacetonate, molybdenum acetylacetonate, ruthenium acetylacetonate, vanadyl sulfate, ammonium metavanadate, ammonium molybdate, methyl rhenium trioxide, rhenium heptoxide, ammonium perrhenate, molybdenum hexacarbonyl, tungsten hexacarbonyl, ferrocene, cobaltocene, nickelocene and ruthenium triphenylphosphine chloride;
the dipolar aprotic solvent is selected from at least one of acetonitrile, acetone, N, N-dimethyl sulfoxide, N, N-dimethylformamide, N, N-dimethylacetamide and hexamethylphosphoramide.
Optionally, the lower limit of the molar ratio of carbohydrate feedstock to isopropanol is selected from the group consisting of 1, 1:5, 2:5, 3:5, 1:1; the upper limit is selected from the group consisting of 10, 5:1, 5:2, 5:3, 1:1;
optionally, the lower limit of the volume ratio of the deionized water to the dipolar aprotic solvent in the mixed solvent system is selected from the group consisting of 1; the upper limit is selected from 2:1, 3:2, 1:1;
optionally, the lower limit of the molar ratio of the transition metal catalyst to the carbohydrate feedstock of the saccharide is selected from 1; the upper limit is selected from 1;
optionally, the reaction temperature is 120 ℃.
Compared with the route of the prior art, the method has the following characteristics:
the invention provides a method for one-step obtaining pyranoside derivatives by taking carbohydrate and isopropanol as raw materials and carrying out dehydration coupling reaction under the action of a transition metal catalyst. The method has the advantages of simple process, strong operability, wide raw material source, recoverable catalyst and considerable large-scale prospect.
Detailed Description
The present application will be described in detail with reference to examples, but the present application is not limited to these examples.
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 Ltd.
Transition metal complex catalysts such as cobalt acetylacetonate, vanadyl acetylacetonate, molybdenum hexacarbonyl, and the like are commercially available from the national pharmaceutical group chemical agents ltd.
Dipolar aprotic solvents such as acetonitrile, N-dimethyl sulfoxide, N-dimethylformamide and the like are available from chemicals of the national chemical group ltd.
The yield of the product pyranoside derivative was calculated according to the following formula:
example 1
Completely dissolving 1.80kg of glucose in 6.00L of a deionized water and acetonitrile mixed solvent (the volume ratio of the deionized water to the acetonitrile is 1:1), transferring the solution into a 20L stainless steel reaction kettle, pumping 0.90kg of isopropanol into the reaction kettle by using a peristaltic pump while stirring, and uniformly mixing. Then 0.24kg of transition metal catalyst vanadyl acetylacetonate is added, the reaction kettle is sealed and stirred, the temperature is raised to 120 ℃, the reaction is stopped after 12 hours, reaction liquid is collected, the solvent and excessive isopropanol are removed by reduced pressure distillation, 1L of deionized water is added to dissolve and filter the catalyst, ethyl acetate is used for extraction for three times (the dosage is 0.25L each time) to remove residual byproducts, water phase is collected, reduced pressure distillation is carried out, vacuum drying is carried out for 12 hours at 40 ℃, and 0.81kg of target product C-glucopyranoside derivative is obtained, wherein the yield is 36.5%.
Example 2
Completely dissolving 1.80kg of glucose in 6.00L of a deionized water and acetonitrile mixed solvent (the volume ratio of the deionized water to the acetonitrile is 1:1), transferring the solution into a 20L stainless steel reaction kettle, pumping 0.90kg of isopropanol into the reaction kettle by using a peristaltic pump while stirring, and uniformly mixing. And adding 0.18kg of transition metal catalyst ammonium molybdate, sealing the reaction kettle, stirring, heating to 120 ℃, stopping the reaction after 12 hours of reaction, collecting the reaction liquid, distilling under reduced pressure to remove the solvent and excessive isopropanol, adding 1L of deionized water to dissolve and filter to remove the catalyst, extracting with ethyl acetate for three times (0.25L of each dosage), removing residual byproducts, collecting the water phase, distilling under reduced pressure, and drying under vacuum at 40 ℃ for 12 hours to obtain 0.53kg of the target product C-glucopyranoside derivative, wherein the yield is 23.9%.
Example 3
Completely dissolving 1.80kg of glucose in 6.00L of a deionized water and acetonitrile mixed solvent (the volume ratio of the deionized water to the acetonitrile is 1:1), transferring the solution into a 20L stainless steel reaction kettle, pumping 0.90kg of isopropanol into the reaction kettle by using a peristaltic pump while stirring, and uniformly mixing. Then 0.23kg of transition metal catalyst methyl rhenium trioxide is added, the reaction kettle is sealed and stirred, the temperature is raised to 120 ℃, the reaction is stopped after 12 hours, the reaction liquid is collected, the solvent and excessive isopropanol are removed by reduced pressure distillation, 1L of deionized water is added for dissolving and filtering to remove the catalyst, ethyl acetate is used for extraction for three times (the dosage is 0.25L each time) to remove the residual by-products, the water phase is collected, reduced pressure distillation is carried out, vacuum drying is carried out for 12 hours at 40 ℃, and the target product C-glucopyranoside derivative is obtained, wherein the yield is 0.91kg, and the yield is 41.0%.
Example 4
Completely dissolving 1.80kg of glucose in 6.00L of a deionized water and acetonitrile mixed solvent (the volume ratio of the deionized water to the acetonitrile is 1:1), transferring the solution into a 20L stainless steel reaction kettle, pumping 0.90kg of isopropanol into the reaction kettle by using a peristaltic pump while stirring, and uniformly mixing. Then 0.08kg of transition metal catalyst triphenylphosphine ruthenium chloride is added, the reaction kettle is sealed and stirred, the temperature is raised to 120 ℃, the reaction is stopped after 12 hours, reaction liquid is collected, the solvent and excessive isopropanol are removed through reduced pressure distillation, 1L of deionized water is added for dissolving and filtering to remove the catalyst, ethyl acetate is used for extraction for three times (the dosage is 0.25L each time), residual byproducts are removed, water phase is collected, reduced pressure distillation is carried out, vacuum drying is carried out for 12 hours at 40 ℃, and the target product C-glucopyranoside derivative 1.21kg is obtained, and the yield is 54.5%.
Example 5
Completely dissolving 1.80kg of glucose in 6.00L of a deionized water and acetonitrile mixed solvent (the volume ratio of the deionized water to the acetonitrile is 1:1), transferring the solution into a 20L stainless steel reaction kettle, pumping 0.90kg of isopropanol into the reaction kettle by using a peristaltic pump while stirring, and uniformly mixing. And adding 0.30kg of transition metal catalyst molybdenum acetylacetonate, sealing the reaction kettle, stirring, heating to 120 ℃, stopping the reaction after 12 hours of reaction, collecting reaction liquid, distilling under reduced pressure to remove the solvent and excessive isopropanol, adding 1L of deionized water to dissolve and filter to remove the catalyst, extracting with ethyl acetate for three times (the dosage is 0.25L each time), removing residual byproducts, collecting a water phase, distilling under reduced pressure, and drying under vacuum at 40 ℃ for 12 hours to obtain 1.53kg of the target product C-glucopyranoside derivative, wherein the yield is 68.9%.
Example 6
Completely dissolving 1.80kg of glucose in 6.00L of deionized water and N, N-dimethylformamide mixed solvent (the volume ratio of the deionized water to the N, N-dimethylformamide is 1:1), transferring to a 20L stainless steel reaction kettle, pumping 0.90kg of isopropanol into the reaction kettle by using a peristaltic pump while stirring, and uniformly mixing. And then 0.30kg of transition metal catalyst molybdenum acetylacetonate is added, the reaction kettle is sealed and stirred, the temperature is raised to 120 ℃, the reaction is stopped after 12 hours, reaction liquid is collected, the solvent and excessive isopropanol are removed by reduced pressure distillation, 1L of deionized water is added to dissolve and filter the catalyst, ethyl acetate is used for extraction for three times (the dosage is 0.25L each time) to remove residual byproducts, water phase is collected, reduced pressure distillation is carried out, vacuum drying is carried out for 12 hours at the temperature of 40 ℃, and 1.05kg of the target product C-glucopyranoside derivative is obtained, wherein the yield is 47.3%.
Example 7
Completely dissolving 1.80kg of glucose in 6.00L of a mixed solvent of deionized water and acetone (the volume ratio of the deionized water to the acetone is 1:1), transferring the solution into a 20L stainless steel reaction kettle, pumping 0.90kg of isopropanol into the reaction kettle by using a peristaltic pump while stirring, and uniformly mixing. Then 0.30kg of transition metal catalyst molybdenum acetylacetonate is added, the reaction kettle is sealed and stirred, the temperature is raised to 120 ℃, the reaction is stopped after 12 hours, the reaction liquid is collected, the solvent and excessive isopropanol are removed by reduced pressure distillation, 1L of deionized water is added for dissolving and filtering to remove the catalyst, ethyl acetate is used for extraction for three times (the dosage is 0.25L each time) to remove the residual by-product, the water phase is collected, reduced pressure distillation is carried out, vacuum drying is carried out for 12 hours at the temperature of 40 ℃, and the target product C-glucopyranoside derivative 1.15kg is obtained, and the yield is 51.8 percent.
Example 8
Completely dissolving 1.80kg of glucose in 6.00L of deionized water and acetonitrile mixed solvent (the volume ratio of the deionized water to the acetonitrile is 1:3), transferring the solution into a 20L stainless steel reaction kettle, pumping 0.90kg of isopropanol into the reaction kettle by using a peristaltic pump while stirring, and uniformly mixing. And adding 0.30kg of transition metal catalyst molybdenum acetylacetonate, sealing the reaction kettle, stirring, heating to 120 ℃, stopping the reaction after 12 hours of reaction, collecting reaction liquid, distilling under reduced pressure to remove the solvent and excessive isopropanol, adding 1L of deionized water to dissolve and filter to remove the catalyst, extracting with ethyl acetate for three times (the dosage is 0.25L each time), removing residual byproducts, collecting a water phase, distilling under reduced pressure, and drying under vacuum at 40 ℃ for 12 hours to obtain 2.00kg of the target product C-glucopyranoside derivative, wherein the yield is 90.1%.
Example 9
3.42kg of maltose is completely dissolved in 6.00L of deionized water and acetonitrile mixed solvent (the volume ratio of the deionized water to the acetonitrile is 1:3), transferred into a 20L stainless steel reaction kettle, and 0.90kg of isopropanol is pumped into the reaction kettle by a peristaltic pump while stirring, and is uniformly mixed. Then 0.30kg of transition metal catalyst molybdenum acetylacetonate is added, the reaction kettle is sealed and stirred, the temperature is raised to 120 ℃, the reaction is stopped after 12 hours, the reaction liquid is collected, the solvent and excessive isopropanol are removed by reduced pressure distillation, 1L of deionized water is added for dissolving and filtering to remove the catalyst, ethyl acetate is used for extraction for three times (the dosage is 0.25L each time) to remove the residual by-product, the water phase is collected, reduced pressure distillation is carried out, vacuum drying is carried out for 12 hours at the temperature of 40 ℃, and the target product C-maltopyranoside derivative 3.21kg is obtained, and the yield is 83.6 percent.
In conclusion, the application provides a preparation method of the pyranoside derivative, which is a method for obtaining the pyranoside derivative by taking saccharide carbohydrate and isopropanol as raw materials and promoting one-step reaction through a transition metal catalyst, and has higher atom economy. The raw material source is wide, and the catalyst can be recovered. Simple process, mild condition, strong operability and large-scale prospect.
Although the present invention has been described with reference to a few preferred embodiments, it should be understood that various changes and modifications can be made without departing from the spirit and scope of the invention as defined by the appended claims.
Claims (10)
1. A preparation method of a transition metal catalyzed pyranoside derivative is characterized by comprising the following steps: at least comprises the following steps: the pyranoside derivative is obtained by one-step dehydration coupling reaction of a raw material containing carbohydrate and isopropanol in a mixed solvent system of deionized water and a dipolar aprotic solvent under the action of a transition metal catalyst.
2. The method of claim 1, wherein: the carbohydrate is selected from one of glucose, mannose, galactose, xylose, arabinose, lactose, maltose and cellobiose.
3. The method of claim 1, wherein: the transition metal catalyst is selected from at least one of iron acetylacetonate, nickel acetylacetonate, cobalt acetylacetonate, vanadyl acetylacetonate, molybdenum acetylacetonate, ruthenium acetylacetonate, vanadyl sulfate, ammonium metavanadate, ammonium molybdate, methyl rhenium trioxide, rhenium heptoxide, ammonium perrhenate, molybdenum hexacarbonyl, tungsten hexacarbonyl, ferrocene, cobaltocene, nickelocene and ruthenium triphenylphosphine chloride.
4. The method of claim 1, wherein: the dipolar aprotic solvent is selected from at least one of acetonitrile, acetone, N, N-dimethyl sulfoxide, N, N-dimethylformamide, N, N-dimethylacetamide and hexamethylphosphoramide.
5. The method of claim 1, wherein: at least comprises the following steps: dissolving carbohydrate in a mixed solvent system of deionized water and a dipolar aprotic solvent, sequentially adding isopropanol and a transition metal catalyst, after the reaction is finished, carrying out reduced pressure distillation, filtering, extracting with ethyl acetate, collecting a water phase, carrying out reduced pressure distillation again, and carrying out vacuum drying to obtain the pyranoside derivative.
6. The method of claim 1, wherein: the molar ratio of the carbohydrate raw material to the isopropanol is 1:10 to 10:1.
7. the method of claim 1, wherein: the volume ratio of the deionized water to the dipolar aprotic solvent in the mixed solvent system is 1:10 to 10:1.
8. the method of claim 1, wherein: the molar ratio of the dosage of the transition metal catalyst to the carbohydrate raw material is 1:1000 to 1:10.
9. the method of claim 1, wherein: the reaction temperature is 30-200 ℃;
preferably 120 deg.c.
10. The production method according to claim 1, characterized in that: the reaction time is 0.5 to 12 hours.
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