CN115197186A - Preparation method of biomass-based pyranoside derivative - Google Patents

Preparation method of biomass-based pyranoside derivative Download PDF

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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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CN115197186B (en
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路芳
卢锐
司晓勤
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Zhongke New Catalytic Technology Dalian Co ltd
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    • C07D309/00Heterocyclic compounds containing six-membered rings having one oxygen atom as the only ring hetero atom, not condensed with other rings
    • C07D309/02Heterocyclic 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
    • C07D309/08Heterocyclic 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
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    • C07HSUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
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    • C07HSUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
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    • C07H15/26Acyclic or carbocyclic radicals, substituted by hetero rings
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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

Preparation method of biomass-based pyranoside derivative
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:
Figure BDA0003016064330000041
example 1
Figure BDA0003016064330000042
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
Figure BDA0003016064330000043
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
Figure BDA0003016064330000051
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
Figure BDA0003016064330000052
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
Figure BDA0003016064330000061
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
Figure BDA0003016064330000062
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
Figure BDA0003016064330000071
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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