Disclosure of Invention
The present invention has been made to solve the above problems and an object of the present invention is to achieve a high yield of Pyriofenone by increasing the yield of (5-chloro-2-methoxy-4-methylpyridin-3-yl) (2,3, 4-trimethoxy-6-methylphenyl) methanol.
In one aspect, the invention provides a preparation method of a novel methoxybenzene cry bacterial intermediate, wherein the intermediate M3 is prepared by the following reaction:
wherein:
the reaction is carried out in an alkaline system under the action of a catalyst.
The chemical names of M1, M2 and M3 are respectively as follows:
m1: 5-chloro-2-methoxy-4-methylnicotinaldehyde;
m2: (2,3, 4-trimethoxy-6-methylphenyl) boronic acid;
m3: (5-chloro-2-methoxy-4-methylpyridin-3-yl) (2,3, 4-trimethoxy-6-methylphenyl) methanol.
The arylboronic acid M2 is used as a reaction material, and has the advantages of good thermal stability, functional group compatibility, insensitivity to air and water and the like.
In some embodiments, the molar ratio of M1 to M2 is 1 (0.8-5). For example, the molar ratio of M1 to M2 is 1:0:8, 1:1, 1:1.5, 1:2, 1:2.5, 1:3, 1:4, 1:5, and so forth.
In some embodiments, the catalyst of the present invention is one or more of rhodium-based catalyst, palladium-based catalyst, nickel-based catalyst, copper-based catalyst, and iron-based catalyst.
In still other embodiments, the rhodium-based catalyst is selected from [ RhCl (cod) ]]2、RhCl3 .3H2O、Rh(PPh3)3Cl、Rh2(OAc)4And one or more of Rh-NHC complex.
In still other embodiments, the palladium-based catalyst is selected from Pd (OAc)2、PdCl2/P(1-Nap)3、[Pd(allyl)Cl]2、PdCl2(PPh3)2One or more of (a).
In still other embodiments, the nickel-based catalyst is selected from the group consisting of Ni (cod)2、NiCl2 .6H2O、Ni(OAc)2 .4H2O、Ni(acac)2 .2H2O、NiCl2(PPh3)2One or more of (a).
In still other embodiments, the copper-based catalyst is selected from cuprous iodide and/or cupric acetate.
In still other embodiments, the iron-based catalyst is selected from ferric chloride.
In the prior art, noble metals such as rhodium, palladium and the like are used for similar reactions; the invention adopts the nickel catalyst, and can obtain good catalytic effect while reducing the cost.
Preferably, the first and second electrodes are formed of a metal,the nickel catalyst is NiCl2(PPh3)2Are commercially available or can be prepared by methods conventional in the art.
For example, NiCl2(PPh3)2The preparation method of (A) can be as follows: dissolving nickel chloride hexahydrate in absolute ethyl alcohol, dripping absolute ethyl alcohol containing triphenylphosphine, stirring and refluxing in nitrogen atmosphere to obtain dark green solution, cooling, standing, precipitating solid, filtering, washing, and vacuum drying.
In some embodiments, the molar ratio of M1 to the catalyst is 1 (0.01-0.10). For example, M1 may be used in a molar ratio to the catalyst of 1:0.01, 1:0.03, 1:0.04, 1:0.05, 1:0.06, 1:0.07, 1:0.08, 1:0.09, 1:0.10, and the like.
In some of these embodiments, the base is one or more of lithium carbonate, sodium carbonate, potassium carbonate, cesium carbonate, sodium bicarbonate, sodium phosphate, potassium phosphate, sodium acetate.
Preferably, the base is potassium phosphate.
Further, the amount of the base used is not particularly limited; for example, the molar ratio of M1 to base is 1 (1-2), specifically, 1:1, 1:1.2, 1:1.25, 1:1.3, 1:1.4, 1:1.5, 1:2, etc.
In still other embodiments, the reaction is carried out in a solvent system that is one or more of dimethyl sulfoxide (DMSO), toluene, acetonitrile, Tetrahydrofuran (THF), methyl tert-butyl ether (MTBE), 1, 4-dioxane, ethanol, isopropanol, tert-butanol, acetone, N-Dimethylformamide (DMF), N-Dimethylacetamide (DMAC), water.
Research shows that the solvent system has great influence on the reaction; preferably, the solvent is one or two of toluene or tetrahydrofuran; further preferably, the solvent is a mixture of toluene and tetrahydrofuran.
More preferably, the volume ratio of toluene to tetrahydrofuran is (3-10):1 or (6-9): 1. For example, the volume ratio of toluene to tetrahydrofuran is 3:1, 3.5:1, 4:1, 4.5:1, 5:1, 6:1, 7:1, 8:1, 9:1, 10:1, and so forth.
Most preferably, the volume ratio of toluene to tetrahydrofuran is 9: 1.
Furthermore, the total volume of the solvent is not particularly required, and the reaction can be carried out smoothly, for example, the ratio of M1 to the total volume of the solvent may be 1mmol (10 to 30) mL, based on M1.
In some embodiments, the reaction temperature is 70-130 ℃, for example, the reaction temperature is 70 ℃, 80 ℃, 85 ℃, 90 ℃, 95 ℃, 100 ℃, 110 ℃, 120 ℃, 130 ℃, etc.
In some embodiments, the reaction is carried out for a reaction time of 6 to 20 hours, e.g., the reaction is carried out for a reaction time of 6 hours, 8 hours, 9 hours, 10 hours, 12 hours, 16 hours, 20 hours, etc.
In still other embodiments, the present invention provides a novel process for preparing an intermediate of methoxybenzene cry bacterium, said intermediate M3 being prepared by reacting M1 with M2:
wherein:
the reaction is carried out in a solvent under the action of a catalyst and an alkaline environment;
the solvent is toluene and tetrahydrofuran, wherein the volume ratio of toluene to tetrahydrofuran is (3-10) to 1 or (6-9) to 1; specifically, the volume ratio of toluene to tetrahydrofuran is 3:1, 3.5:1, 4:1, 4.5:1, 5:1, 6:1, 7:1, 8:1, 9:1 or 10: 1;
the base is potassium phosphate;
the catalyst is NiCl2(PPh3)2;
The molar using amount ratio of the M1 to the M2 is 1 (0.8-5); specifically, the molar ratio of M1 to M2 is 1:0:8, 1:1, 1:1.5, 1:2, 1:2.5, 1:3, 1:4 or 1: 5;
the molar using amount ratio of the M1 to the catalyst is 1 (0.01-0.10); specifically, the molar ratio of the M1 to the catalyst is 1:0.01, 1:0.03, 1:0.04, 1:0.05, 1:0.06, 1:0.07, 1:0.08, 1:0.09 or 1: 0.10.
On the other hand, the invention provides a preparation method of methoxybenzene cry bacteria, which comprises the step of carrying out oxidation reaction on the intermediate M3 to obtain the methoxybenzene cry bacteria.
Preferably, the oxidizing agent of the oxidation reaction is activated manganese dioxide, chromic acid or tert-butyl peroxide.
Specifically, for example, the intermediate (5-chloro-2-methoxy-4-methylpyridin-3-yl) (2,3, 4-trimethoxy-6-methylphenyl) methanol of the present invention is dissolved in a toluene solution, activated manganese dioxide is added, the mixture is stirred under heating reflux, filtered, and the solvent is removed under reduced pressure, so that a methoxybenzene cry bacterial product can be obtained.
Compared with the prior art, the invention has the beneficial effects that: (1) the (5-chloro-2-methoxy-4-methylpyridin-3-yl) (2,3, 4-trimethoxy-6-methylphenyl) methanol is prepared by adopting a new synthetic route, and a new thought is provided for the preparation of a methoxybenzene cry bacterium intermediate; (2) using NiCl as a nickel-based catalyst2(PPh3)2And other reaction conditions are matched to obtain a better catalytic effect, and compared with the prior art, the yield of (5-chloro-2-methoxy-4-methylpyridin-3-yl) (2,3, 4-trimethoxy-6-methylphenyl) methanol can be obviously improved.
Detailed Description
The present invention will be described in detail below by way of examples. In the following examples, various starting materials used are either commercially available or may be prepared by methods conventional in the art, unless otherwise specified. The following examples are not all-inclusive and other examples that may be obtained by one of ordinary skill in the art without making any inventive step are within the scope of the present invention.
Preparation of intermediate (5-chloro-2-methoxy-4-methylpyridin-3-yl) (2,3, 4-trimethoxy-6-methylphenyl) methanol
Example 1
A50 mL three-necked flask was charged with potassium phosphate (1mmol,212mg) and NiCl2(PPh3)2(0.04mmol,26.16mg) followed by the addition of 5-chloro-2-methoxy-4-methylnicotinaldehyde (E1mmol,185.6mg) and (2,3, 4-trimethoxy-6-methylphenyl) boronic acid (1.5mmol,339mg), followed by addition of dimethyl sulfoxide (17.5mL), heating the mixture to 80 ℃ under nitrogen atmosphere for reaction for 8h, cooling to room temperature, filtering, removing the solvent under reduced pressure, and purifying by silica gel column chromatography (eluent: ethyl acetate: petroleum ether is 1: 4) 121.4mg of a pale yellow oil are obtained in 33% yield and 98.3% purity.
1H NMR(CDCl3,300MHz)δ2.24(s,3H),2.27(s,3H),3.56(s,3H),3.80(s,3H),3.84(s,3H),3.95(s,3H),5.34(d,J=9.0Hz,1H),6.10(d,J=9.0Hz,1H),6.50(s,1H),8.02(s,1H).
Examples 2-16 below were prepared in a similar manner to example 1 to provide intermediate M3 according to the present invention.
TABLE 1
From the results in Table 1, it can be seen that:
(1) under the same other reaction conditions, the solvent system has an influence on the yield of the intermediate, and when a toluene/THF system is used and the volume ratio of the toluene/THF system to the intermediate is in the range of 6/1-9/1, the intermediate is obtained in higher yield;
(2) under the same other reaction conditions, the type of the base has an influence on the yield of the intermediate of the invention, and when potassium phosphate is used, the yield of the intermediate of the invention is higher;
(3) under the same other reaction conditions, the type of the catalyst has an influence on the yield of the intermediate of the invention, and the nickel-based catalyst of the invention can be used for obtaining the intermediate of the invention with higher yield.
The above description is only for the preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any changes or substitutions that can be easily conceived by those skilled in the art within the technical scope of the present invention are included in the scope of the present invention.