A kind of preparation method of thiocol
Technical field
The present invention relates to a kind of new synthetic method of thiocol, particularly the synthetic method of highly purified contraposition thiocol, belongs to pharmaceutical chemistry technical field.
Background technology
Thiocol is powerful expectorant, and respiratory tract glandular secretion is increased, and sputum is diluted, and is easy to expectoration; Anticholinergic drug can be strengthened as atropinic effect; With calmness, soporific, anti-allergy agent also with increasing the restraining effect of this product to maincenter.The thiocol finished product of current commercial type is usually the mixture of 4-hydroxy 3-methoxybenzene potassium sulfonate and 3-hydroxyl-4-methoxy benzenesulfonic acid potassium (English name is potassium 4-hydroxy-3-methoxybenzene-sulphonate/potassium 3-hydroxy-4-methoxybenzenesulphonate).2014, Chinese thiocol compound medicine sales volume reached 5MG, comparatively within 2013, increased by 25%.5 years (2009-2014) increases by 30% every year in the past.The market demand potential is very large.
The method of current synthesizing guaiacol potassium sulfonate is mainly carried out sulfonation by methyl catechol (hydroxyanisole) and derivative thereof and is obtained.The mixture of products therefrom mainly 4-hydroxy 3-methoxybenzene potassium sulfonate and 3-hydroxyl-4-methoxy benzenesulfonic acid potassium, roughly the ratio of 4-hydroxy 3-methoxybenzene potassium sulfonate and 3-hydroxyl-4-methoxy benzenesulfonic acid potassium is 70%: 30%.The product only having Japan to produce can reach 4-hydroxy 3-methoxybenzene potassium sulfonate more than 98%.Because the drug effect of the mixture of two kinds of isomer of thiocol is relatively poor, therefore, development research highly purified 4-hydroxy 3-methoxybenzene potassium sulfonate product has wide market outlook.
Sulfonation reaction is traditional conventional organic chemical reactions, is that sulphonating agent is directly with the reaction that sulfonic group replacement hydrogen atom carries out.The mixture of sulphur trioxide, chlorsulfonic acid, sulfurous gas and chlorine in the different solvents such as conventional sulphonating agent has the vitriol oil, is dissolved in hydrochloric ether, sulfur dioxide liquid, dioxane and pyridine and sulfuryl chloride etc.Sulfuric acid is a kind of relatively mild sulphonating agent, for the sulfonation of most of aromatics; Sulphur trioxide is fiercer sulphonating agent, owing to producing by product, is generally be dissolved in solvent using.In addition, the temperature controlling sulfonation reaction is extremely important, and when temperature is low, sulfonic group easily enters substituent ortho position, and during temperature height, sulfonic group easily enters substituent contraposition.When using catalyzer in sulfonation reaction, the direction of malleable sulfonation reaction, this is also a feature of sulfonation reaction.The catalyzer of sulfonation reaction is usually the vitriol of sodium Metal 99.5, mercury, cadmium, aluminium, lead, arsenic, bismuth and iron and the mixture of Vanadium Pentoxide in FLAKES; Silicon oxide and bone black are also a kind of sulfonation catalysts preferably.But utilize the sulfonation reaction of methyl catechol to prepare highly purified thiocol, namely the 4-hydroxy 3-methoxybenzene potassium sulfonate of single structure has larger difficulty, is necessary the synthetic route that research and development one are new.Further, there is not been reported to prepare the patent of invention technology of the 4-hydroxy 3-methoxybenzene potassium sulfonate target product of single structure.
Summary of the invention
Technical problem to be solved by this invention is, provides a kind of new reaction raw material cheap and easy to get, gentle at reaction conditions, aftertreatment simple and be suitable for the synthetic method of high-purity guaiacol potassium sulfonate of large-scale production.
For solving above technical problem, the preparation method of thiocol of the present invention, in turn includes the following steps:
A, with structure such as formula the 2-hydroxyacetanilide shown in (I) for raw material, carry out sulfonation reaction with the sulphur trioxide be dissolved in organic solvent and obtain 2-hydroxyl-5-sulfonic group Acetanilide, and concentrated;
B, carry out kharophen hydrolysis and diazotization reaction in acid condition, especially by adding dilute hydrochloric acid and slowly drip sodium nitrite solution in reactant, realize 2-hydroxyl-5-sulfonic group Acetanilide and kharophen hydrolysis occurs in acid condition, the nitrous acid generation diazotization reaction simultaneously generated in hydrolysate and solution;
C, gained diazonium salt carry out methoxylation with the methanol solution containing potassium hydroxide and obtain structure such as formula the 3-methoxyl group-4-hydroxy benzenesulfonic acid shown in (II);
D, then separation and purification in Klorvess Liquid, obtained purity reaches the structure of more than 99% such as formula the 4-hydroxy 3-methoxybenzene potassium sulfonate target product shown in (III), Klorvess Liquid makes this target product be easy to precipitate and separate while making 3-methoxyl group-4-hydroxy benzenesulfonic acid be converted into 4-hydroxy 3-methoxybenzene potassium sulfonate:
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Further, during sulfonation reaction, organic solvent used can be selected from combination that is one of following or more than one solvents: methylene dichloride, chloroform, tetrachloroethane, dioxane, pyridine.
Further, described organic solvent is preferably one in tetrachloroethane, dioxane or its mixture.
Further, described organic solvent most preferably is the mixture of tetrachloroethane and dioxane, and its volume ratio is 1: 1 ~ 10.
Further, the volumetric usage of described organic solvent counts 5 ~ 10 mL/g with the quality of 2-hydroxyacetanilide.
Further, described 2-hydroxyacetanilide and the molar ratio of sulphur trioxide are 1: 1 ~ 3.
Further, described 2-hydroxyacetanilide and the molar ratio of sulphur trioxide are 1: 1 ~ 1.5.
Further, in diazotization reaction, the mole number of nitrous acid is 3 ~ 5 times of 2-hydroxyacetanilide.
Further, sulfonation reaction temperature is 60 ~ 90 DEG C, diazotization reaction temperature is 0 ~ 5 DEG C, methoxylation temperature is 50 ~ 100 DEG C.
Further, the described methoxylation time is 5 ~ 10 hours.
It is reaction raw materials that the present invention have selected this material cheap and easy to get of 2-hydroxyacetanilide, pass through sulfonation reaction, sulfonic group is introduced in hydroxyl contraposition, and make kharophen that hydrolysis and diazotization reaction occur, and the performance utilizing gained diazonium salt directly can introduce methoxyl group in containing the basic solution of methyl alcohol prepares 3-methoxyl group-4-hydroxy benzenesulfonic acid, target product 4-hydroxy 3-methoxybenzene potassium sulfonate is converted into again further in Klorvess Liquid, it is a brand-new reaction scheme preparing thiocol, and products therefrom structure is single, 4-hydroxy 3-methoxybenzene potassium sulfonate purity reaches more than 99%, to sum up, reaction raw materials of the present invention is cheap and easy to get, reaction conditions is gentle, aftertreatment is simple and be suitable for large-scale production.
Embodiment
With specific embodiment, technical scheme of the present invention is described below, but protection scope of the present invention is not limited thereto:
embodiment 1
In 500 milliliters of there-necked flasks, add 2-hydroxyacetanilide 15.1 grams (0.1 mole), dioxane 150 milliliters, sulphur trioxide 9.6 grams (0.12 mole), react under 80 DEG C of conditions, follow the tracks of reaction raw materials with thin-layer chromatography to disappear, add 20%(quality again) dilute hydrochloric acid, dilute hydrochloric acid consumption is as the criterion with wherein containing hydrogen chloride 0.3 mole, slowly drip the aqueous solution 100 milliliters containing Sodium Nitrite 20.7 grams (0.3 mole), control temperature of reaction and be no more than 5 DEG C, the situation of the nitrous acid that dissociates with the inspection of starch-kalium iodide test paper, until reaction terminates.Then obtained diazonium salt solution is slowly added drop-wise in the methanol solution 100 milliliters containing 8 grams of potassium hydroxide, reacts 10 hours at 100 DEG C, add solid potassium chloride 10 grams, stir and make it to dissolve, slowly cool, filter, dry, obtain product 15.7 grams, productive rate 65%, purity >=99%.
embodiment 2
In 500 milliliters of there-necked flasks, add 2-hydroxyacetanilide 15.1 grams (0.1 mole), dioxane and each 75 milliliters of tetrachloroethane, sulphur trioxide 12 grams (0.15 mole), react under 90 DEG C of conditions, follow the tracks of reaction raw materials with thin-layer chromatography to disappear, add 20%(quality again) dilute hydrochloric acid, dilute hydrochloric acid consumption is as the criterion with wherein containing hydrogen chloride 0.5 mole, slowly drip the aqueous solution 100 milliliters containing Sodium Nitrite 35 grams (0.5 mole), control temperature of reaction and be no more than 5 DEG C, the situation of the nitrous acid that dissociates with the inspection of starch-kalium iodide test paper, until reaction terminates.Then obtained diazonium salt solution is slowly added drop-wise in the methanol solution 100 milliliters containing 8 grams of potassium hydroxide, reacts 5 hours at 100 DEG C, add solid potassium chloride 10 grams, stir and make it to dissolve, slowly cool, filter, dry, obtain product 15 grams, productive rate 60%, purity >=99%.
embodiment 3
In 500 milliliters of there-necked flasks, add 2-hydroxyacetanilide 15.1 grams (0.1 mole), tetrachloroethane 150 milliliters, sulphur trioxide 9.6 grams (0.12 mole), react under 60 DEG C of conditions, follow the tracks of reaction raw materials with thin-layer chromatography to disappear, add 20%(quality again) dilute hydrochloric acid, dilute hydrochloric acid consumption is as the criterion with wherein containing hydrogen chloride 0.3 mole, slowly drip the aqueous solution 100 milliliters containing Sodium Nitrite 20.7 grams (0.3 mole), control temperature of reaction and be no more than 5 DEG C, the situation of the nitrous acid that dissociates with the inspection of starch-kalium iodide test paper, until reaction terminates.Then obtained diazonium salt solution is slowly added drop-wise in the methanol solution 100 milliliters containing 8 grams of potassium hydroxide, reacts 5 hours at 100 DEG C, add solid potassium chloride 10 grams, stir and make it to dissolve, slowly cool, filter, dry, obtain product 15.3 grams, productive rate 63%, purity >=99%.
embodiment 4
In 500 milliliters of there-necked flasks, add 2-hydroxyacetanilide 15.1 grams (0.1 mole), dioxane 150 milliliters, sulphur trioxide 8 grams (0.1 mole), react under 90 DEG C of conditions, follow the tracks of reaction raw materials with thin-layer chromatography to disappear, add 20%(quality again) dilute hydrochloric acid, dilute hydrochloric acid consumption is as the criterion with wherein containing hydrogen chloride 0.5 mole, slowly drip the aqueous solution 100 milliliters containing Sodium Nitrite 35 grams (0.5 mole), control temperature of reaction and be no more than 5 DEG C, the situation of the nitrous acid that dissociates with the inspection of starch-kalium iodide test paper, until reaction terminates.Then obtained diazonium salt solution is slowly added drop-wise in the methanol solution 100 milliliters containing 8 grams of potassium hydroxide, reacts 8 hours at 80 DEG C, add solid potassium chloride 10 grams, stir and make it to dissolve, slowly cool, filter, dry, obtain product 15.7 grams, productive rate 65%, purity >=99%.
Above in each embodiment, in dilute hydrochloric acid, the molar ratio of hydrogenchloride and Sodium Nitrite is 1:1, and the mole number of the nitrous acid generated after feeding intake is 3 ~ 5 times of raw material 2-hydroxyacetanilide consumption.