Disclosure of Invention
Aiming at the technical problems, the invention provides a novel process for preparing (2, 5-dimethoxy pyridine-4-yl) boric acid simply and with high yield, which is realized by the following technical scheme:
the preparation method of the 1, 4-dioxane-2-ketone has the following reaction formula:
The method comprises the following steps:
s1, adding ethylene glycol and a solvent into a four-neck flask, and controlling the temperature of an ice water bath to be 0-10 ℃;
S2, adding potassium tert-butoxide, and controlling the temperature to be 0-10 ℃;
s3, after the addition is finished, preserving the temperature to be 0-10 ℃, and stirring and reacting for 1h;
s4, dropwise adding tert-butyl bromoacetate, and controlling the temperature to be 0-10 ℃;
S5, naturally recovering to room temperature after dripping, and reacting for 2 hours;
s6, after the reaction is finished, quenching reaction is carried out, and the PH in the system is adjusted to be neutral;
s7, adding water and DCM, stirring, extracting and layering, and washing an organic phase twice by using water;
S8, drying an organic phase by using anhydrous sodium sulfate, filtering, and concentrating filtrate under reduced pressure to obtain a light yellow oily substance;
S9, carrying out reduced pressure distillation on the light yellow oily matter, and controlling the temperature of an oil bath at 90-105 ℃ to obtain fraction 1, 4-dioxane-2-ketone.
Preferably, in S1, the solvent is N, N-dimethylformamide.
Preferably, the molar ratio of ethylene glycol, tert-butyl bromoacetate and potassium tert-butoxide added is 3:1:1.05.
Preferably, the weight (g) to volume (ml) ratio of t-butyl bromoacetate and N, N-dimethylformamide added is 1:4.
Preferably, the quenching reaction in S6 is performed with saturated aqueous ammonium chloride.
More preferably, the room temperature in S5 is 30 degrees.
The invention has the advantages that the raw materials are easy to obtain, the cost is low, the steps are simplified, the lactonization reaction is directly completed by only one-step reaction, meanwhile, the treatment operation of the reaction is simpler and more convenient, the yield of the obtained product 1, 4-dioxane-2-ketone is high, the consumption of the solvent and the production amount of waste liquid are less, the product is easy to separate, the selectivity is high, and the operation is simple, thereby being suitable for the requirements of industrial mass production.
Detailed Description
The following description of the embodiments of the present invention will be made clearly and completely, and it is apparent that the described embodiments are only some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
Meanwhile, the meaning of "and/or" and/or "appearing throughout the text is to include three schemes, taking" a and/or B "as an example, including a scheme, or B scheme, or a scheme that a and B satisfy simultaneously.
Furthermore, descriptions such as those referred to as "first," "second," and the like, are provided for descriptive purposes only and are not to be construed as indicating or implying a relative importance or implying an order of magnitude of the indicated technical features in the present disclosure. Thus, a feature defining "a first" or "a second" may explicitly or implicitly include at least one such feature. In addition, the technical solutions of the embodiments may be combined with each other, but it is necessary to base that the technical solutions can be realized by those skilled in the art, and when the technical solutions are contradictory or cannot be realized, the combination of the technical solutions should be considered to be absent and not within the scope of protection claimed in the present invention.
Example 1, 4-Dioxahexacyclic-2-one preparation method, the reaction formula is shown as follows:
The specific operation steps are as follows:
S1, adding 286.4g of ethylene glycol and 1.2L of N, N-dimethylformamide into a 3L four-neck flask, and controlling the temperature of an ice water bath to be 0-10 ℃;
S2, adding 181.2g of potassium tert-butoxide, and controlling the temperature to be 0-10 ℃;
s3, after the addition is finished, preserving the temperature to be 0-10 ℃ and stirring to react for 1h;
s4, beginning to dropwise add 300.0g of tert-butyl bromoacetate, and controlling the temperature to be 0-10 ℃;
S5, naturally recovering to room temperature (30 ℃) after the dripping is finished, and reacting for 2 hours;
S6, monitoring the end of the reaction, dropwise adding a saturated ammonium chloride aqueous solution to quench the reaction, and regulating the pH value in the system to be neutral;
s7, adding 2.4L of water and DCM1.5L L of water, stirring and layering, and washing the organic phase once by using 600ml of water and 300ml of water respectively;
S8, drying an organic phase by using anhydrous sodium sulfate, filtering, and concentrating filtrate under reduced pressure to obtain 180g of light yellow oily matter;
S9, 180g of light yellow oily matter is distilled under reduced pressure, the oil bath temperature is 90-105 ℃, 133.3g of white semisolid of fraction 1, 4-dioxane-2-one is obtained, the mixture is put into a refrigerator with the temperature of 2-8 ℃ for storage, the white powdery solid is obtained after the mixture is converted into the white powdery solid, the yield is 85%, and the GC purity is 99.9%.
1HNMR(400MHz,CDCl3):δ3.88(t,J=4.0Hz,2H),4.38(s,2H),4.50(t,J=4.0Hz,2H)。
Comparative scheme 1 selection and adjustment of the reaction solvent in example 1, namely, using equivalent tetrahydrofuran to replace N, N-dimethylformamide, the addition amount of the rest raw materials, the reaction temperature, the reaction step and other conditions are unchanged, thus obtaining 36.1g of the 1, 4-dioxane-2-one white semisolid with the yield of 23% and the GC purity of 99.1%.
1HNMR(400MHz,CDCl3):δ3.88(t,J=4.0Hz,2H),4.38(s,2H),4.50(t,J=4.0Hz,2H)。
Compared with the scheme 2, the method is adjusted according to the selection of the reaction solvent in the example 1, namely, the same amount of tertiary butanol is used for replacing N, N-dimethylformamide as the reaction solvent, the feeding amount of the other raw materials, the reaction temperature, the reaction step and other conditions are unchanged, and 106.8g of white semi-solid of the product 1, 4-dioxane-2-one is obtained, the yield is 68%, and the GC purity is 99.7%.
1HNMR(400MHz,CDCl3):δ3.88(t,J=4.0Hz,2H),4.38(s,2H),4.50(t,J=4.0Hz,2H)。
As can be seen from comparative schemes 1 and 2, the influence of the type of solvent on the reaction is remarkable, so that the selection of N, N-dimethylformamide as the reaction solvent is an excellent solution, i.e., the technical scheme proposed by the present invention.
In the comparison scheme 3, the dosage of the ethylene glycol in the example 1 is adjusted to 190.9g, the conditions of the dosage, the reaction temperature, the reaction step and the like of the other raw materials are unchanged, and the product 1, 4-dioxane-2-one is 95.8g white semi-solid, the yield is 61%, and the GC purity is 99.4%.
1HNMR(400MHz,CDCl3):δ3.88(t,J=4.0Hz,2H),4.38(s,2H),4.50(t,J=4.0Hz,2H)。
In comparison scheme 4, the dosage of the ethylene glycol in the example 1 is adjusted to 477.3g, the conditions of the dosage, the reaction temperature, the reaction step and the like of the other raw materials are unchanged, and 134.5g of white semisolid of the product 1, 4-dioxane-2-one is obtained, the yield is 85.7%, and the GC purity is 99.7%.
1HNMR(400MHz,CDCl3):δ3.88(t,J=4.0Hz,2H),4.38(s,2H),4.50(t,J=4.0Hz,2H)。
As is clear from the comparison of the schemes 3 and 4, when the amount of ethylene glycol is small, the impurity content of the by-product of the reaction increases, the reaction yield decreases, and when the amount of ethylene glycol is large, the reaction yield does not change much, so that 286.4g of ethylene glycol is the preferred solution.
In comparison scheme 5, the dosage of the potassium tert-butoxide in the example 1 is adjusted to 207.1g, the conditions of the dosage, the reaction temperature, the reaction steps and the like of the other raw materials are unchanged, and 124.0g of white semisolid of the product 1, 4-dioxane-2-one is obtained, the yield is 79%, and the GC purity is 99.6%.
1HNMR(400MHz,CDCl3):δ3.88(t,J=4.0Hz,2H),4.38(s,2H),4.50(t,J=4.0Hz,2H)。
In comparison scheme 6, the dosage of the potassium tert-butoxide in the example 1 is adjusted to 241.6g, the conditions of the dosage, the reaction temperature, the reaction step and the like of the other raw materials are unchanged, and 100.5g of white semisolid of the product 1, 4-dioxane-2-one is obtained, the yield is 64%, and the GC purity is 99.3%.
1HNMR(400MHz,CDCl3):δ3.88(t,J=4.0Hz,2H),4.38(s,2H),4.50(t,J=4.0Hz,2H)。
As is clear from comparative examples 5 and 6, when the amount of potassium t-butoxide is increased, the stability of the starting material t-butyl bromoacetate is significantly affected, so that 181.2g of potassium t-butoxide is selected as the optimal solution.
The invention adopts the technical scheme that only one-step reaction is needed, namely, glycol and bromobutyl acetate react under the alkaline condition of tertiary butanol potassium, the reaction is directly carried out to synthesize 1, 4-dioxane-2-ketone, the high-purity 1, 4-dioxane-2-ketone is obtained through reduced pressure distillation, meanwhile, the treatment operation of the reaction is simpler and more convenient, the yield of the obtained product 1, 4-dioxane-2-ketone is high, the consumption of a solvent and the production amount of waste liquid are less, the process and the production cost are further simplified, the economic value is remarkable, and the industrialized production is easier.
It should be understood that these examples are for the purpose of illustrating the application only and are not intended to limit the scope of the application. Furthermore, it is to be understood that various changes, modifications and/or variations may be made by those skilled in the art after reading the technical content of the present application, and that all such equivalents are intended to fall within the scope of the present application as defined in the appended claims.