CN103073546A - Preparation method of mebhydrolin napadisylate - Google Patents

Preparation method of mebhydrolin napadisylate Download PDF

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CN103073546A
CN103073546A CN2013100375493A CN201310037549A CN103073546A CN 103073546 A CN103073546 A CN 103073546A CN 2013100375493 A CN2013100375493 A CN 2013100375493A CN 201310037549 A CN201310037549 A CN 201310037549A CN 103073546 A CN103073546 A CN 103073546A
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preparation
hydrochloric acid
reaction
stirring
toluene
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张方正
曾锡瑞
肖芳政
龙梅
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JI'AN HAIZHOU CHEMICAL CO Ltd
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JI'AN HAIZHOU CHEMICAL CO Ltd
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Abstract

The invention relates to a preparation method of mebhydrolin napadisylate, which is characterized in that the preparation method comprises the following steps of (1) stirring methyl acrylate and methylamine gas for reaction at 15-30 DEG C, pumping low-boiling-point substances with a water pump, (2) adding toluene, diester, sodium hydride and liquid sodium methylate, stirring to initiate reaction, dropping a hydrochloric acid solution under violent stirring, conducting heating reflux, obtaining a hydrochloric acid solution of 1-methyl-piperidone hydrochloride, (3) adding phenylhydrazine, toluene and triethylamine, stirring, heating, slowly and dropwise adding benzyl chloride for reaction, and (4) adding the hydrochloric acid solution of 1-methyl-piperidone hydrochloride into an ethanol solution of a product from Step (3), adding 1,5-naphthalenedisulfonate for reaction, reducing to a room temperature, conducting swing filtration, using methanol and water to wash successively, obtaining a crude product through the swing filtration, using DMF (dimethyl formamide) and ammonia water to recrystallize, using methanol to spray, and obtaining high-purity mebhydrolin napadisylate. The method avoids using sulfuric acid for acidification, and a sulfonation reaction is facilitated. A technology is simple; a yield is high; and the product quality is good.

Description

A kind of preparation method of Mebhydrolin napadisilate
Technical field
The present invention relates to a kind of preparation method of medical compounds, be specifically related to a kind of preparation method of Mebhydrolin napadisilate.
Background technology
The Mebhydrolin napadisilate is white crystalline powder, molecular formula (C 19H 20N 2) 2C 10H 8O 6S 2, nontoxic, non-corrosiveness, "dead", nonflammable, non-explosive, belong to antihistaminic; And cholinolytic and sedative effect are arranged, be used for various allergic diseases.Be used for clinically urticaria, rhinitis, vasodilation and serum sickness, antianaphylactic curative effect is 10 times of Toldrin, and preparation is tablet.
United States Patent (USP) was reported synthetic (patent No. 2786059) of Y-carboline derivative in 1975, Chinese patent CN03150674.7 had also reported mehailuolin-1 in 2005, the preparation method of 5 napadisilates, technique shown in this patent shows that its flow process is to prepare first Mebhydrolin vitriol, convert thereof into again sulfonate, because sulfate ion is residual, the conversion reaction of p-sulfonic acid salt is impacted, the sulfate ion residual concentration is relatively high, and purifying products is difficulty relatively.
Summary of the invention
The objective of the invention is to propose a kind of preparation method of Mebhydrolin napadisilate, high, the steady quality of the product purity of the method preparation.
The object of the present invention is achieved like this, its chemical equation is as follows:
Figure 518806DEST_PATH_IMAGE001
Concrete synthetic method step is as follows:
1. the preparation of dibasic acid esters thing:
Add the methyl acrylate of charging capacity in glassed steel reaction vessels, stirring temperature control is 15-30 ℃, directly passes into methylamine gas in the reactor, temperature control is in 35-45 ℃ of reaction, (with the cooling water control temperature of ventilating, controlling consumption with weight reduction), logical finish censorship, reach requirement content after.In 30-35 ℃ of stirring 40 minutes, water rushed pump and takes out low-boiling-point substance.Need not to concentrate, the dibasic acid esters substrate concentration is on the not impact of quality of later stage finished product herein.
2. cyclization, decarboxylation:
In reactor, add toluene, dibasic acid esters, be cooled to 20 ℃, add sodium hydride and liquid methanol sodium, stir initiation reaction in 30 minutes, interior temperature is no more than 45 ℃, is down to normal-temperature reaction 30 minutes, to clarifying thickness.Above reactant is cooled to 0 ℃, splashing into 20% hydrochloric acid to solution in 0-10 ℃ under the violent stirring clarifies, static layering, divide and get toluene, extract toluene twice with concentrated hydrochloric acid, merge the hydrochloric acid layer, stir lower reflux, until till no longer including carbonic acid gas and emitting, (refluxing 6 hours) gets the hydrochloric acid soln of 1-methyl-piperidone hydrochloride.Decompression steams hydrochloric acid, adds ethanol.
The sulfuric acid of herein former decarboxylation being used changes hydrochloric acid into, reduces reflux temperature, reduces return time, improves service life of equipment.Return time was 12 hours in the past, was kept to now 6 hours.
3. the preparation of benzyl hydrazinobenzene hydrochloride salt:
In glassed steel reaction vessels, pass into nitrogen protection, add phenylhydrazine, toluene, triethylamine, stir and heat up in 35 ~ 65 ℃ of slow Benzyl Chlorides that drip, temperature control drips 1 hour below 85 ℃, drips to finish.In 85-95 ℃ of reaction 1 hour, slowly be warming up to again and refluxed 4 hours, then be cooled to 30 ~ 60 ℃ of filtrations, the filter cake toluene wash.Decompression is steamed toluene to doing.
Behind the triethylamine salt soda acid, recycling has reduced solid waste, has improved the service efficiency of material.
4. the preparation of finished product:
With step 3 products obtained therefrom, add in the ethanolic soln of step 2, be warming up to 84 ℃ and refluxed 4 hours, be cooled to 60 ℃, add again 1,5-naphthalene disulfonic acid sodium salt, being warming up to 84 ℃ refluxed 3 hours, be down to the room temperature rejection filter, use the methanol wash filter cake, the filter cake still that enters to pull an oar, add the making beating of 2T water, be warming up to 45 ℃, stirred 1 hour, rejection filter gets crude product.The DMF of 8 times of crude product weight of vacuum suction adds crude product and ammoniacal liquor and stirs to clarify suction filtration, filtrate control steams 2/3(less than 70 ℃ of decompressions has solid to separate out), be chilled to the room temperature rejection filter, filter cake sprays with methyl alcohol, distillate is applied mechanically, and the mother liquor distillate is applied mechanically, and the pin material is processed.
5. packing is put in storage:
To be transported to through the wet product after centrifugal drying room and carry out the sabot oven dry, drying temperature is controlled in 85 ℃, and dry about 6 hours, when sampling detects moisture content≤0.3%, close baking oven steam, it is cooled to below 40 ℃ naturally, pulverize, mix rear packing.Pack into after packing with plastic inner bag fiber drum or metal bucket, (sampling is chemically examined before the barrelling) packing specifications is 20kg/ bucket or 25kg/ bucket, labels after quality test is qualified and puts in storage.
Advantage of the present invention is: the present invention avoids using sulfuric acid acidation, is conducive to sulfonated reaction.Technique is simple, and yield is high, good product quality.Every batch products can be stablized and reaches content more than 99.0%, and the foreign matter contents such as sulfate radical, heavy metal are all below the limit of quality standard regulation.
Description of drawings
Fig. 1 is production technological process of the present invention.
Embodiment
As shown in Figure 1, production craft step of the present invention is:
1. the preparation of dibasic acid esters thing:
The methyl acrylate that in glassed steel reaction vessels, adds 90Kg, stirring temperature control is 25 ℃, and methylamine gas 30Kg is directly passed in the reactor, temperature control is in 35 ℃ of reactions, logically finishes censorship, reach requirement content after.In 30-35 ℃ of stirring 40 minutes, water rushed pump and takes out low-boiling-point substance.
2. cyclization, decarboxylation:
In reactor, add 130Kg toluene and dibasic acid esters, be cooled to 20 ℃, add sodium hydride 20Kg and liquid methanol sodium 1000ml, stir initiation reaction in 30 minutes, interior temperature is no more than 45 ℃, is down to normal-temperature reaction 30 minutes, to clarifying thickness.Above reactant is cooled to 0 ℃, splash into 20% hydrochloric acid 470L in 0-10 ℃ under the violent stirring and clarify to solution, static layering is divided and is got toluene, extract toluene twice with concentrated hydrochloric acid, merge the hydrochloric acid layer, stir lower reflux, until till no longer including carbonic acid gas and emitting, (refluxing 6 hours), get the hydrochloric acid soln of 1-methyl piperidine keto hydrochloride, decompression steams hydrochloric acid, adds ethanol.
3. the preparation of benzyl hydrazinobenzene hydrochloride salt:
In glassed steel reaction vessels, pass into nitrogen protection, add phenylhydrazine 28kg, toluene 130Kg, triethylamine 35Kg, stir and heat up in 50 ℃ of slow Benzyl Chloride 35Kg that drip, temperature control drips 1 hour below 85 ℃, drips to finish.In 90 ℃ of reactions 1 hour, slowly be warming up to again and refluxed 4 hours, then be cooled to 50 ℃ of filtrations, the filter cake toluene wash, decompression is steamed toluene to doing.
4. the preparation of finished product:
With step 3 products obtained therefrom, add in the ethanolic soln of step 2, be warming up to 84 ℃ and refluxed 4 hours, be cooled to 60 ℃, add again 1,5-naphthalene disulfonic acid sodium salt 90Kg, being warming up to 84 ℃ refluxed 3 hours, be down to the room temperature rejection filter, with 30Kg methanol wash filter cake, the filter cake still that enters to pull an oar, add the making beating of 2T water, be warming up to 45 ℃, stirred 1 hour, rejection filter gets crude product.The DMF of vacuum suction 900Kg adds crude product and 10Kg ammoniacal liquor and stirs to clarify, suction filtration, and filtrate is controlled at less than 70 ℃ of lower decompressions and steams 2/3, has solid to separate out, and is chilled to the room temperature rejection filter, and filter cake sprays with a small amount of methyl alcohol.
5. packing is put in storage:
To be transported to through the wet product after centrifugal drying room and carry out the sabot oven dry, drying temperature is controlled in 85 ℃, and dry about 6 hours, when sampling detects moisture content≤0.3%, close baking oven steam, it is cooled to below 40 ℃ naturally, pulverize, mix rear packing.Pack into after packing with plastic inner bag fiber drum or metal bucket, packing specifications is 20kg/ bucket or 25kg/ bucket, labels after quality test is qualified and puts in storage.

Claims (7)

1. the preparation method of a Mebhydrolin napadisilate is characterized in that the preparation method may further comprise the steps:
(1) preparation of dibasic acid esters thing: add methyl acrylate in glassed steel reaction vessels, stirring temperature control is 15-30 ℃, and methylamine gas is directly passed in the reactor, and temperature control was in 30-35 ℃ of stirring 40 minutes, and water rushes pump and takes out low-boiling-point substance;
(2) cyclization, decarboxylation: in reactor, add toluene, dibasic acid esters, cooling adds sodium hydride and liquid methanol sodium, stir initiation reaction, to clarifying thickness, reactant is cooled to 0 ℃, splash into 20% hydrochloric acid to solution under the violent stirring and clarify, static layering is divided and is got toluene, extract toluene twice with concentrated hydrochloric acid, merge the hydrochloric acid layer, stirred lower reflux 6 hours, get the hydrochloric acid soln of 1-methyl-piperidone hydrochloride, decompression steams hydrochloric acid, adds ethanol;
(3) preparation of benzyl hydrazinobenzene hydrochloride salt: in glassed steel reaction vessels, pass into nitrogen protection, add phenylhydrazine, toluene, triethylamine, stirring heats up in slow dropping Benzyl Chloride, reacts 1 hour, and slow temperature rising reflux is 4 hours again, then the filter cake toluene wash is filtered in cooling;
(4) preparation of finished product: with step 3 products obtained therefrom, add in the ethanolic soln of step 2, temperature rising reflux 4 hours, cooling add 1,5-naphthalene disulfonic acid sodium salt, temperature rising reflux is 3 hours again, be down to the room temperature rejection filter, successively get crude product with methyl alcohol, water washing rejection filter, use again DMF and ammoniacal liquor recrystallization, with the methyl alcohol spray, get high purity product at last.
2. a kind of preparation method of Mebhydrolin napadisilate as claimed in claim 1 is characterized in that step (1) temperature control is in 35-45 ℃ of reaction.
3. a kind of preparation method of Mebhydrolin napadisilate as claimed in claim 1 is characterized in that step (2) adds sodium hydride and liquid methanol sodium mixture reaction.
4. a kind of new preparation method of Mebhydrolin napadisilate as claimed in claim 1 is characterized in that step (2) adopts hydrochloric acid to carry out decarboxylic reaction.
5. a kind of preparation method of Mebhydrolin napadisilate as claimed in claim 1 is characterized in that step (3) directly prepares benzyl hydrazinobenzene hydrochloride salt solid, rather than benzyl phenylhydrazine oily liquids.
6. a kind of preparation method of Mebhydrolin napadisilate as claimed in claim 1, it is characterized in that step (4) adopts benzyl hydrazinobenzene hydrochloride salt solid and 1,5-naphthalene disulfonic acid sodium salt directly prepares the Mebhydrolin napadisilate, and must not use sulfuric acid acidation early stage.
7. a kind of preparation method of Mebhydrolin napadisilate as claimed in claim 1 is characterized in that the purification step of step (4) product adopts methyl alcohol, repeatedly drip washing of water, and with DMF and ammoniacal liquor recrystallization.
CN2013100375493A 2013-01-31 2013-01-31 Preparation method of mebhydrolin napadisylate Pending CN103073546A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110483375A (en) * 2019-09-11 2019-11-22 陈建江 A kind of synthetic method of intermediate 4- piperidones
CN116410190A (en) * 2022-09-06 2023-07-11 辽宁惠风生物医药科技有限公司 Method for preparing mehtaline naphthalene disulfonate

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2786059A (en) * 1951-04-30 1957-03-19 Schenley Ind Inc Derivatives of 2-nu-methyl-1, 2, 3, 4-tetrahydro-gamma-carbolines
CN1590387A (en) * 2003-08-29 2005-03-09 上海子能高科股份有限公司 Preparation method of mehailuolin -1,5- naphthaline disulfonate

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2786059A (en) * 1951-04-30 1957-03-19 Schenley Ind Inc Derivatives of 2-nu-methyl-1, 2, 3, 4-tetrahydro-gamma-carbolines
CN1590387A (en) * 2003-08-29 2005-03-09 上海子能高科股份有限公司 Preparation method of mehailuolin -1,5- naphthaline disulfonate

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
张帆 等: "抗组胺原料药美海曲林萘二磺酸盐合成方法的改进", 《江西化工》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110483375A (en) * 2019-09-11 2019-11-22 陈建江 A kind of synthetic method of intermediate 4- piperidones
CN116410190A (en) * 2022-09-06 2023-07-11 辽宁惠风生物医药科技有限公司 Method for preparing mehtaline naphthalene disulfonate

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Application publication date: 20130501