CN108101937A - A kind of method for preparing L- α-glycerolphosphocholine - Google Patents

A kind of method for preparing L- α-glycerolphosphocholine Download PDF

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CN108101937A
CN108101937A CN201711115959.XA CN201711115959A CN108101937A CN 108101937 A CN108101937 A CN 108101937A CN 201711115959 A CN201711115959 A CN 201711115959A CN 108101937 A CN108101937 A CN 108101937A
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glycerine
protection object
hydroxyl protection
preparation
double hydroxyl
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CN108101937B (en
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皮士卿
谭跃
李乐欢
刘庆林
傅裕
黄本东
徐燕
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Hunan Warner Pharmaceutical Co Ltd
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Hunan Warner Pharmaceutical Co Ltd
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    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02Phosphorus compounds
    • C07F9/06Phosphorus compounds without P—C bonds
    • C07F9/08Esters of oxyacids of phosphorus
    • C07F9/09Esters of phosphoric acids
    • C07F9/10Phosphatides, e.g. lecithin

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  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
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Abstract

It is as follows comprising step the present invention provides a kind of preparation method of the L α glycerolphosphocholines of high-content:(1) reaction under the catalysis of acid generates the double hydroxyl protection object I of halogenated glycerine to halogenated glycerine with ester;(2) double hydroxyl protection object II crude products of phosphorylcholine salt and the double hydroxyl protection object I reactions generation L α glycerolphosphocholines of halogenated glycerine;(3) double hydroxyl protection object II of L α glycerolphosphocholines are separated with the double hydroxyl protection object I of unreacted halogenated glycerine, double hydroxyl protection object II of the L α glycerolphosphocholines purified;(4) double hydroxyl protection object II aqueous solutions of the L α glycerolphosphocholines of purifying, which react to be deprotected under catalytic amount acid catalysis, obtains L α glycerolphosphocholine aqueous solutions; remove moisture under reduced pressure; it is crystallized with alcohols solvent, obtains L α glycerolphosphocholines.Technical scheme is compared with the prior art, and purity is high, and high income, technique is suitable for industrialized production.

Description

A kind of method for preparing L- α-glycerolphosphocholine
Technical field:
The present invention relates to pharmaceutical chemistry technical fields, and in particular to a kind of preparation method of L- α-glycerolphosphocholine.
Background technology:
L- α-glycerolphosphocholine (L-alpha-Glycerphosphatidylcholine, abbreviation GPC) is a kind of tool Having improves the active material of brain function, has certain effect for prevention and auxiliary treatment senile dementia.
The known technological means for obtaining GPC is mainly by two kinds:One kind is to be extracted from natural products, such as from yolk Egg yolk lecithin is extracted, soybean lecithin is lifted from soybean.Further obtained by chemical method or enzymatic hydrolysis separating-purifying GPC (such as US5250719, US5315023, US6274362, EP217765 etc.).
Second method is that chemical synthesis obtains.
It is obtained from natural products since raw material sources, place of production difference have differences parameter, separates the complex process of impurity, It is higher to industrialize cost.The distinct methods report of synthetic method is more in recent years, and synthetic method is compared to natural extraction method with work Skill is relatively easy, Control of Impurities is good, and impurity is less.
Such as:European patent EP 0486100 is reported, using the isopropylidene glycerol-4-methanol of double hydroxyl protections, with diethylene glycol dilaurate list Phosphoryl chloride phosphorus oxychloride reacts, and forms phosphotriester, then acetone glycerol choline phosphate is obtained by the reaction under elevated pressure with trimethylamine, finally Hydrolysis deprotection obtains GPC crude products in dilute hydrochloric acid, and total recovery 50%, reaction equation is described as follows:
Japan Patent JP2007/269657 reports employ above-mentioned similar method.
What European patent EP 0502357 was reported is to protect double acetylating hydroxyl groups of glycerine, then route similar to the above It carries out that GPC is prepared.
It reports that chiral glycidol is condensed with phosphatldylcholine in WO2007/145476, is obtained by purifying resin GPC.This technique simplifies, but glycidol activity is strong, and polymerisation itself easily occurs, also can be with the hydroxyl of the product of generation into one Step condensation, so impurity is more.
Chinese patent CN101544667A on the basis of the above, protects the hydroxyl of glycidol so that generation Product further will not become impurity with glycidol reaction, there is certain effect.
Korean Patent KR2009/128631 is reacted using glycidol with phosphatidyl choline in sodium hydrate aqueous solution, Water layer is washed with ethyl acetate again, after condensed water ethyl alcohol crystallization is added to obtain GPC products.It equally exists multiple caused by glycidol The formation of impurity influences.
Chinese patent CN101967160A generates thick GPC and nothing using Phosphorylcholine inorganic salts and halogenated glycerine reaction Machine salt halide filters out a large amount of inorganic salts, and crude product contains a small amount of inorganic salts, unreacted raw material and impurity, due to impurity Water-soluble fine, acetone solubility is smaller, it is necessary to be washed with a large amount of acetone extracts, and actually also needing to purifying resin can just obtain GPC sterlings.
Chinese patent CN103665028A discloses a kind of preparation method of L- α-Choline Glycerophosphate, with (2S) -3- it is halogenated - 1,2- propylene oxide is raw material with phosphorylcholine salt, obtains L- α-Choline Glycerophosphate after esterification, hydrolysis in a solvent Crude product, then obtain L- α-Choline Glycerophosphate sterling through silica gel column chromatography, ion-exchange resin purification.But this method preparation L- α- The Choline Glycerophosphate reaction time is longer, and yield is not high.
The content of the invention:
It is completed it is an object of the invention to provide a kind of easy industrialization, high income and easy purifying obtain high-purity GPC new synthetic methods.
The invention is realized by the following technical scheme:
Double hydroxyl protection object II (Formula II) of L- α-glycerolphosphocholine (L- α-GPC) are anti-under catalytic amount acid catalysis It should be deprotected to obtain L- α-glycerolphosphocholine,
Formula IIWherein R is alkyl.
Specifically, L- α-glycerolphosphocholine synthetic method includes the following steps:
(1) reaction under the catalysis of acid generates the double hydroxyl protection object I (formulas of the halogenated glycerine of (R) -3- to halogenated glycerine with protective agent I), Formulas IWherein R is alkyl, and X is halogen;
(2) phosphorylcholine salt and the double hydroxyl protection object I reactions generation L- α-glycerophosphatide acyl courages of the halogenated glycerine of (R) -3- Double hydroxyl protection object II (Formula II) crude products of alkali;
(3) by double hydroxyl protection object II of L- α-glycerolphosphocholine and the double hydroxyls of the halogenated glycerine of unreacted (R) -3- Protection I is separated, double hydroxyl protection object II of the L- α-glycerolphosphocholine purified;
(4) double hydroxyl protection object II aqueous solutions of L- α-glycerolphosphocholine of purifying react under catalytic amount acid catalysis Deprotection obtains L- α-glycerolphosphocholine aqueous solution, removes moisture under reduced pressure, is crystallized with alcohols solvent, obtains L- α-glycerine phosphorus Phosphatidylcholine.
In step (1), the halogenated glycerine is (R) -3- glycerin chlorohydrins or (R) -3- bromo glycerine.
In step (1), the protective agent is selected from alkyl orthoformate, triethyl orthoformate, vinyl ethers, acrylic The one or more of ether, 2- methoxyl groups propylene or 2- ethoxy propylenes.
In step (1), with molar amount, the protective agent inventory is more than or equal to 1.2 times of halogenated glycerine.
In step (1), acid is selected from p-methyl benzenesulfonic acid, anhydrous hydrogen chloride, the concentrated sulfuric acid, anhydrous oxalic acid, with molar amount, dosage For the 1-10% of reactant.
In step (1), reaction temperature is 10-110 DEG C, is preferably 40-80 DEG C.
In step (1), react and carried out under negative pressure condition.
In step (1), reaction time control is in 1-15h, preferably 5-10h.
In step (1), after reaction, extra protective agent is recovered under reduced pressure.
(R) R=CH in the double hydroxyl protection object I of the halogenated glycerine of -3-3Or C2H5, X=Cl or Br;L- α-glycerophosphatide acyl courage R=CH in double hydroxyl protection object II of alkali3Or C2H5
In step (2), the phosphorylcholine salt is phosphorylcholine mono-sodium salt and/or phosphorylcholine monopotassium salt.
The step (2) is anti-in alcohols solvent for phosphorylcholine salt and the double hydroxyl protection object I of the halogenated glycerine of (R) -3- Double hydroxyl protection object II of L- α-glycerolphosphocholine should be generated, alcohols solvent is recycled, is dissolved in water to obtain L- α-glycerine phosphorus The crude product aqueous solution of double hydroxyl protection object II of phosphatidylcholine, wherein, with molar amount, the double hydroxyl protections of the halogenated glycerine of (R) -3- The inventory of object I is 1.2 to 3.0 times of phosphorylcholine salt, is preferably 1.5 times.
In step (2), the alcohols solvent is selected from methanol, ethyl alcohol, isopropanol.
In step (2), reaction temperature is 50-90 DEG C, is preferably 65-85 DEG C.
Preferably, in step (2), reaction time 1min-5h is preferably 0.5-2h.
The step (3) for double hydroxyl protection object II of L- α-glycerolphosphocholine crude product aqueous solution with water-insoluble Organic solvent extracts the double hydroxyl protection object I of the halogenated glycerine of unreacted (R) -3-, discards organic phase, the L- α-glycerine purified Double hydroxyl protection object II of phosphatidyl choline.
In step (3), extractant is ether solvent such as methyl tertiary butyl ether(MTBE) or esters solvent such as ethyl acetate, acetic acid Isobutyl ester, isopropyl acetate, n-propyl acetate.
In step (4), the acid is adjusted pH value of solution to 1-3 selected from dilute hydrochloric acid, dilute sulfuric acid.
In step (4), deprotection reaction temperature is 10-40 DEG C, is preferably 20-30 DEG C.
In step (4), after deprotection, L- α-glycerolphosphocholine aqueous solution is removed into hydrochloric acid by ion exchange resin With remaining inorganic salts.
In step (4), the alcohols solvent is isobutanol.
Preferably, in step (4), reaction time 1min-5h is preferably 0.5-2h.
The product purity prepared by this method is more than 99.8%, is calculated with Phosphorylcholine salt, and overall yield of reaction is more than 88%.
The halogenated glycerine of (the R) -3-, phosphorylcholine list potassium (sodium) salt can be obtained from market purchasing.
The synthesis of GPC there are two difficult point needs to overcome, one is the control of inorganic salts, it is desirable that inorganic salts residual 0.01% with Under, can inorganic salts be removed by resins exchange.Second difficult point is the removal of impurity.Second point is most crucial technology, on The method for stating most introductions is to surround that deimpurity principle is gone to carry out highway route design.The present invention is by by the two of halogenated glycerine A hydroxyl protection so that the intermediate polarity after protection becomes smaller, and solubility in water substantially becomes smaller, in common organic solvents Solubility greatly enhance, so as to become very big with the polarity difference of product so that after the completion of reaction, it is only necessary to simply will production Object is dissolved in the water, and carries out extracting and demixing with for example environment amenable solvent esters solvent of organic solvent, that is, realizes product Purifying.And the ingredient proportion by increasing intermediate compound I, make another starting raw material phosphor acyl group choline list potassium (sodium) reactant salt complete Entirely, the reaction was complete not only greatly improves its reaction yield for this raw material, and will not remain and form impurity in the product.By upper Content can finally be obtained more than 99.8% by stating scheme, and the effect of molar yield more than 88% has reached the mesh of invention 's.
Specific reaction equation is as follows:
R=CH3、C2H5;X=Cl, Br (I)
R=CH3、C2H5;M=Na, K
In the present invention, the halogenated glycerine of (R) -3- is specially (R) -3- glycerin chlorohydrins or (R) -3- bromo glycerine, both are former Material can be cheaper commercially to obtain.Protective agent is preferably trimethyl orthoformate or triethyl orthoformate.Also may be used To select vinyl ethers, propenyl ether, 2- methoxyl groups propylene or 2- ethoxy propylenes, obtain being acetal or ketal class after protection Compound, the main description trimethyl orthoformate of the present invention or triethyl orthoformate are as protectant technical solution.
During halogenated with the 3- glycerine reaction of trimethyl orthoformate or ethyl ester, since two kinds of reactants are liquid, during reaction not With solvent, more than trimethyl orthoformate or the excessive 1.2 times of equivalents of ethyl ester, even if trimethyl orthoformate or ethyl ester substantially exceed Amount needed for reaction, also has facilitation for reaction speed, shortens the time of reaction, and reaction charging sequence does not have any want It asks, but the acid of catalytic amount is needed to carry out catalysis to accelerate reaction, sour dosage is generally the 1-10% equivalents of reactant, Can be p-methyl benzenesulfonic acid, anhydrous hydrogen chloride, the concentrated sulfuric acid, anhydrous oxalic acid etc. for common inorganic acid.Reaction temperature is in 40-80 ℃.Temperature is less than this scope, and the reaction time needs longer.Reaction preferably carries out under certain negative pressure condition, reaction process The methanol or ethyl alcohol of middle generation are steamed by decompression, are conducive to the complete conversion of reaction, it is possible to reduce trimethyl orthoformate or second The usage amount of ester.Reaction converts complete generally when 5-10 is small.Reaction finishes is recovered under reduced pressure extra raw material orthoformic acid three again Methyl esters or ethyl ester, obtained product can be directly used for reacting in next step.
Another raw material of the present invention is Phosphorylcholine monopotassium salt and Phosphorylcholine mono-sodium salt.Due to sylvite and chloro thing Reactivity is higher than sodium salt, and preferably Phosphorylcholine monopotassium salt is another synthesis segment in the present invention.
Solvent used in second step esterification is alcohols solvent, including methanol, ethyl alcohol, isopropanol.Reaction temperature 65- 85℃.(R) inventory of the double hydroxyl protection object I of the halogenated glycerine of -3- is 1.2 to 3.0 equivalents of Phosphorylcholine list potassium (sodium) salt, excellent Select 1:1.5 equivalent.Make Phosphorylcholine list potassium (sodium) reactant salt complete by detection.Reaction finishes, and reaction dissolvent is recovered under reduced pressure, into Row purifying, purification process are simple two-phase extraction.I.e.:Directly add water and extractant, extractant can be ether solvent Such as methyl tertiary butyl ether(MTBE), esters solvent is such as ethyl acetate, isobutyl acetate, isopropyl acetate, n-propyl acetate.Extraction Unreacted raw material and the double hydroxyl protection objects of impurity glycerine for decomposing generation.Organic phase is discarded, water mutually as purifies obtained II.
Second step reaction product abstraction purification finishes, and adds in catalytic amount diluted acid inorganic acid such as dilute hydrochloric acid, dilute sulfuric acid, dilute Sour addition is to adjust aqueous solution to 1-3.Deprotection reaction temperature is room temperature.Reaction finishes, and the aqueous solution of obtained GPC leads to Ion exchange resin removing hydrochloric acid and remaining inorganic salts are crossed, product steams moisture, adds in isobutanol alcohol crystallization and obtains white powder Last shape solid is dried under reduced pressure solvent and obtains the GPC products that purity is more than 99.8%.It is calculated with Phosphorylcholine list potassium (sodium) salt, instead It is more than 88% to answer total recovery.
Beneficial effects of the present invention:(1) using the method for the present invention preparation L- α-glycerolphosphocholine, its is simple for process, easily In industrialized production;(2) L- α-glycerolphosphocholine prepared by the method for the present invention is used compared with the prior art, purity Height, overall yield of reaction are high.
Specific embodiment
Here exemplary embodiment will be illustrated in detail.Embodiment described in following exemplary embodiment Do not represent all embodiments consistent with the present invention.On the contrary, they be only with as being described in detail in the appended claims , the examples of the apparatus and method that some aspects of the invention are consistent.
It is only merely for the purpose of description specific embodiment in terminology used in the present invention, is not intended to limit the invention. It is also intended in " one kind " of singulative of the invention and used in the attached claims, " described " and "the" including majority Form, unless context clearly shows that other meanings.It is also understood that term "and/or" used herein refers to and wraps Containing one or more associated list items purposes, any or all may be combined.
It will be appreciated that though various information, but this may be described using term first, second, third, etc. in the present invention A little information should not necessarily be limited by these terms.These terms are only used for same type of information being distinguished from each other out.For example, it is not departing from In the case of the scope of the invention, the first information can also be referred to as the second information, and similarly, the second information can also be referred to as One information.Depending on linguistic context, word as used in this " if " can be construed to " ... when " or " when ... When " or " in response to determining ".
The present invention will be described in detail by way of examples below.
Comparative example 1
L- α-glycerolphosphocholine is prepared using the preparation method of EP0502357.
Comparative example 2
The preparation method of CN103665028A prepares L- α-glycerolphosphocholine.
Embodiment 1
(R) preparation of -2- methoxyl groups -4- chloromethyls -1,3- dioxo pentamethylene.
In 500mL vials, (R) -3- glycerin chlorohydrins 115.5g (1.0 moles), trimethyl orthoformate 138.0g are weighed (1.3 moles), p-methyl benzenesulfonic acid 19.0g, after mixing, stirring is heated to 70-90 DEG C of reaction, is steamed in reaction process from still head Go out low boiling material, predominantly methanol and a small amount of methyl formate.GC detect reaction process, about 6 it is small when the reaction was complete.It has reacted Finish, be cooled to room temperature, add in sodium methoxide and be neutralized to pH=6-7.First heating low boiling point solvent is recovered under reduced pressure, then- 0.096Mpa collects 102-105 DEG C of fraction, obtains 143.4g products, yield 91%.
Embodiment 2
(R) preparation of -2- ethyoxyls -4- chloromethyls -1,3- dioxo pentamethylene.
In 500mL vials, (R) -3- glycerin chlorohydrins 115.5g (1.0 moles), triethyl orthoformate 192.5g are weighed (1.3 moles), p-methyl benzenesulfonic acid 19.0g, after mixing, stirring is heated to 70-90 DEG C of reaction, is steamed in reaction process from still head Go out low boiling material, predominantly ethyl alcohol and a small amount of Ethyl formate.GC detect reaction process, about 8 it is small when the reaction was complete.It has reacted Finish, be cooled to room temperature, add in sodium ethoxide and be neutralized to pH=6-7.First heating low boiling point solvent is recovered under reduced pressure, then- 0.096Mpa collects 114-116 DEG C of fraction, obtains 154.5g products, yield 90%.
Embodiment 3
(R) preparation of -2- methoxyl groups -4- bromomethyls -1,3- dioxo pentamethylene.
In 500mL vials, (R) -3- bromo glycerine 199.0g (1.0 moles), trimethyl orthoformate 138.0g are weighed (1.3 moles), p-methyl benzenesulfonic acid 19.0g, after mixing, stirring is heated to 70-90 DEG C of reaction, is steamed in reaction process from still head Go out low boiling material, predominantly methanol and a small amount of methyl formate.GC detect reaction process, about 6 it is small when the reaction was complete.It has reacted Finish, be cooled to room temperature, add in sodium methoxide and be neutralized to pH=6-7.First low boiling point solvent is recovered under reduced pressure in heating, then left in 100pa 68-73 DEG C of fraction of right collection, obtains 177.8g products, yield 88%.
Embodiment 4
(R) preparation of -2- ethyoxyls -4- bromomethyls -1,3- dioxo pentamethylene.
In 500mL vials, (R) -3- bromo glycerine 199.0g (1.0 moles), triethyl orthoformate 192.5g are weighed (1.3 moles), p-methyl benzenesulfonic acid 19.0g, after mixing, stirring is heated to 70-90 DEG C of reaction, is steamed in reaction process from still head Go out low boiling material, predominantly ethyl alcohol and a small amount of Ethyl formate.GC detect reaction process, about 8 it is small when the reaction was complete.It has reacted Finish, be cooled to room temperature, add in sodium ethoxide and be neutralized to pH=6-7.First low boiling point solvent is recovered under reduced pressure in heating, then left in 100pa 118-121 DEG C of fraction of right collection, obtains 161.5g products, yield 87%.
The preparation of embodiment 5L- α-GPC
In 500mL four-hole bottles, Phosphorylcholine monopotassium salt 44.2g (0.2mol), (R) -2- methoxyl group -4- chloromethanes are added in Base -1,3- dioxo pentamethylene 45.7g (0.3mol), absolute ethyl alcohol 250mL, when back flow reaction 20 is small more than, HPLC detections are former Expect that Phosphorylcholine monopotassium salt is less than less than 0.5%, stop being heated to reflux, etoh solvent is recovered under reduced pressure to dry, residue addition drink With water 150mL and ethyl acetate 100mL, after ten minutes, stratification discards organic layer, and water layer uses ethyl acetate again for stirring 100mL is extracted 2 times, discards organic layer.Hydrochloric acid is added dropwise into the water layer after extraction, makes pH that it is small to be stirred to react 5 at room temperature for 1-2 When more than, after deprotection completely, the remaining inorganic salts of spent ion exchange resin removing, the aqueous solution decompression containing GPC steams water Point, isobutanol 200mL is added in into residue, cooling and stirring crystallization filters, dry, obtains white powder GPC solids 45.2g, yield 88%.
The preparation of embodiment 6L- α-GPC
In 500mL four-hole bottles, Phosphorylcholine monopotassium salt 44.2g (0.2mol), (R) -2- methoxyl group -4- bromine first are added in Base -1,3- dioxo pentamethylene 47.3g (0.24mol), absolute ethyl alcohol 250mL, when back flow reaction 10 is small more than, HPLC detections are former Expect that Phosphorylcholine monopotassium salt is less than less than 0.5%, stop being heated to reflux, etoh solvent is recovered under reduced pressure to dry, residue addition drink With water 150mL and isopropyl acetate 100mL, after ten minutes, stratification discards organic layer, and water layer uses isopropyl acetate again for stirring Ester 100mL is extracted 2 times, discards organic layer.Hydrochloric acid is added dropwise into the water layer after extraction, pH is made to be stirred to react 5 at room temperature for 1-2 Hour or more, after deprotection completely, the remaining inorganic salts of spent ion exchange resin removing, the aqueous solution decompression containing GPC steams Moisture adds in isobutanol 200mL into residue, and cooling and stirring crystallization filters, dry, obtains white powder GPC solids 46.7g, yield 91%.
The preparation of embodiment 7L- α-GPC
In 500mL four-hole bottles, Phosphorylcholine mono-sodium salt 41.0g (0.2mol), (R) -2- methoxyl group -4- chloromethanes are added in Base -1,3- dioxo pentamethylene 45.7g (0.3mol), absolute ethyl alcohol 250mL, when back flow reaction 36 is small more than, HPLC detections are former Expect that Phosphorylcholine mono-sodium salt is less than less than 0.5%, stop being heated to reflux, etoh solvent is recovered under reduced pressure to dry, residue addition drink With water 150mL and ethyl acetate 100mL, after ten minutes, stratification discards organic layer, and water layer uses ethyl acetate again for stirring 100mL is extracted 2 times, discards organic layer.Hydrochloric acid is added dropwise into the water layer after extraction, makes pH that it is small to be stirred to react 5 at room temperature for 1-2 When more than, after deprotection completely, the remaining inorganic salts of spent ion exchange resin removing, the aqueous solution decompression containing GPC steams water Point, isobutanol 200mL is added in into residue, cooling and stirring crystallization filters, dry, obtains white powder GPC solids 45.0g, yield 87.6%.
The preparation of embodiment 8L- α-GPC
In 500mL four-hole bottles, Phosphorylcholine mono-sodium salt 41.0g (0.2mol), (R) -2- methoxyl group -4- bromine first are added in Base -1,3- dioxo pentamethylene 47.3g (0.24mol), absolute ethyl alcohol 250mL, when back flow reaction 20 is small more than, HPLC detections are former Expect that Phosphorylcholine mono-sodium salt is less than less than 0.5%, stop being heated to reflux, etoh solvent is recovered under reduced pressure to dry, residue addition drink With water 150mL and isobutyl acetate 100mL, after ten minutes, stratification discards organic layer, and water layer uses Sucrose Acetate again for stirring Ester 100mL is extracted 2 times, discards organic layer.Hydrochloric acid is added dropwise into the water layer after extraction, pH is made to be stirred to react 5 at room temperature for 1-2 Hour or more, after deprotection completely, the remaining inorganic salts of spent ion exchange resin removing, the aqueous solution decompression containing GPC steams Moisture adds in isobutanol 200mL into residue, and cooling and stirring crystallization filters, dry, obtains white powder GPC solids 45.3g, yield 88.4%.
The preparation of embodiment 9L- α-GPC
In 500mL four-hole bottles, Phosphorylcholine monopotassium salt 44.2g (0.2mol), (R) -2- ethyoxyl -4- chloromethanes are added in Base -1,3- dioxo pentamethylene 50.0g (0.3mol), absolute ethyl alcohol 250mL, when back flow reaction 20 is small more than, HPLC detections are former Expect that Phosphorylcholine monopotassium salt is less than less than 0.5%, stop being heated to reflux, etoh solvent is recovered under reduced pressure to dry, residue addition drink With water 150mL and isopropyl acetate ester 100mL, after ten minutes, stratification discards organic layer, and water layer is different with acetic acid again for stirring Propyl ester 100mL is extracted 2 times, discards organic layer.Hydrochloric acid is added dropwise into the water layer after extraction, pH is made to be stirred to react at room temperature for 1-2 5 it is small when more than, after deprotection completely, the remaining inorganic salts of spent ion exchange resin removing, the aqueous solution decompression containing GPC steams Moisture adds in isobutanol 200mL into residue, and cooling and stirring crystallization filters, dry, obtains white powder GPC solids 45.3g, yield 88.2%.
The preparation of embodiment 10L- α-GPC
In 500mL four-hole bottles, Phosphorylcholine monopotassium salt 44.2g (0.2mol), (R) -2- ethyoxyl -4- bromine first are added in Base -1,3- dioxo pentamethylene 50.7g (0.24mol), absolute ethyl alcohol 250mL, when back flow reaction 10 is small more than, HPLC detections are former Expect that Phosphorylcholine monopotassium salt is less than less than 0.5%, stop being heated to reflux, etoh solvent is recovered under reduced pressure to dry, residue addition drink With water 150mL and isopropyl acetate 100mL, after ten minutes, stratification discards organic layer, and water layer uses isopropyl acetate again for stirring Ester 100mL is extracted 2 times, discards organic layer.Hydrochloric acid is added dropwise into the water layer after extraction, pH is made to be stirred to react 5 at room temperature for 1-2 Hour or more, after deprotection completely, the remaining inorganic salts of spent ion exchange resin removing, the aqueous solution decompression containing GPC steams Moisture adds in isobutanol 200mL into residue, and cooling and stirring crystallization filters, dry, obtains white powder GPC solids 46.2g, yield 90%.
The preparation of embodiment 11L- α-GPC
In 500mL four-hole bottles, Phosphorylcholine mono-sodium salt 41.0g (0.2mol), (R) -2- ethyoxyl -4- chloromethanes are added in Base -1,3- dioxo pentamethylene 50.0g (0.3mol), absolute ethyl alcohol 250mL, when back flow reaction 36 is small more than, HPLC detections are former Expect that Phosphorylcholine mono-sodium salt is less than less than 0.5%, stop being heated to reflux, etoh solvent is recovered under reduced pressure to dry, residue addition drink With water 150mL and isobutyl acetate ester 100mL, after ten minutes, stratification discards organic layer, and water layer is different with acetic acid again for stirring Butyl ester 100mL is extracted 2 times, discards organic layer.Hydrochloric acid is added dropwise into the water layer after extraction, pH is made to be stirred to react at room temperature for 1-2 5 it is small when more than, after deprotection completely, the remaining inorganic salts of spent ion exchange resin removing, the aqueous solution decompression containing GPC steams Moisture adds in isobutanol 200mL into residue, and cooling and stirring crystallization filters, dry, obtains white powder GPC solids 45.0g, yield 87.6%.
The preparation of embodiment 12L- α-GPC
In 500mL four-hole bottles, Phosphorylcholine mono-sodium salt 41.0g (0.2mol), (R) -2- ethyoxyl -4- bromine first are added in Base -1,3- dioxo pentamethylene 63.3g (0.3mol), absolute ethyl alcohol 250mL, when back flow reaction 20 is small more than, HPLC detections are former Expect that Phosphorylcholine mono-sodium salt is less than less than 0.5%, stop being heated to reflux, etoh solvent is recovered under reduced pressure to dry, residue addition drink With water 150mL and isobutyl acetate 100mL, after ten minutes, stratification discards organic layer, and water layer uses Sucrose Acetate again for stirring Ester 100mL is extracted 2 times, discards organic layer.Hydrochloric acid is added dropwise into the water layer after extraction, pH is made to be stirred to react 5 at room temperature for 1-2 Hour or more, after deprotection completely, the remaining inorganic salts of spent ion exchange resin removing, the aqueous solution decompression containing GPC steams Moisture adds in isobutanol 200mL into residue, and cooling and stirring crystallization filters, dry, obtains white powder GPC solids 45.5g, yield 88.8%.
The detection of purity and the calculating of yield are carried out to the product of embodiment 5-12 and comparative example 1,2, as a result such as 1 institute of table Show.According to table 1 as a result, L- α-GPC prepared by the method for the present invention, whether purity or yield, are higher than the prior art Preparation method (comparative example 1, comparative example 2), and data have statistical significance (P < 0.01).
GPC purity and yield in 1 embodiment 5-12 of table
It should be pointed out that for those of ordinary skill in the art, without departing from the principle of the present invention, may be used also With to the present invention, some improvement and modification can also be carried out, these improvement and modification are also fallen into the protection domain of the claims in the present invention.

Claims (13)

1. a kind of preparation method of L- α-glycerolphosphocholine of high-content, it is characterised in that:Include the following steps:By L- α- Double hydroxyl protection object II (Formula II) of glycerolphosphocholine react deprotection under catalytic amount acid catalysis and obtain L- α-glycerine phosphorus Phosphatidylcholine,
Formula IIWherein R is alkyl.
2. according to the preparation method described in claim 1, it is characterised in that:Double hydroxyl protections of L- α-glycerolphosphocholine The preparation method of object II includes the following steps:
(1) reaction under the catalysis of acid generates the double hydroxyl protection object I (Formulas I) of the halogenated glycerine of (R) -3- to halogenated glycerine with protective agent, Formulas IWherein R is alkyl, and X is halogen;
(2) phosphorylcholine salt and the double hydroxyl protection object I reactions generation L- α-glycerolphosphocholines of the halogenated glycerine of (R) -3- Double hydroxyl protection object II crude products;
(3) by double hydroxyl protection object II of L- α-glycerolphosphocholine and the double hydroxyl protections of the halogenated glycerine of unreacted (R) -3- Object I is separated, double hydroxyl protection object II of the L- α-glycerolphosphocholine purified.
3. preparation method according to claim 2, it is characterised in that:In step (1), the halogenated glycerine is (R) -3- chlorine For glycerine or (R) -3- bromo glycerine.
4. preparation method according to claim 2, it is characterised in that:In step (1), the protective agent is selected from orthoformic acid Trialkyl ester, triethyl orthoformate, vinyl ethers, propenyl ether, one kind or several of 2- methoxyl groups propylene or 2- ethoxy propylenes Kind.
5. preparation method according to claim 2, it is characterised in that:In step (1), with molar amount, the protective agent Inventory is more than or equal to 1.2 times of halogenated glycerine.
6. preparation method according to claim 2, it is characterised in that:In step (1), acid is selected from p-methyl benzenesulfonic acid, anhydrous Hydrogen chloride, the concentrated sulfuric acid, anhydrous oxalic acid, with molar amount, dosage is the 1-10% of reactant.
7. preparation method according to claim 2, it is characterised in that:(R) R in the double hydroxyl protection object I of the halogenated glycerine of -3- =CH3Or C2H5, X=Cl or Br;R=CH in double hydroxyl protection object II of L- α-glycerolphosphocholine3Or C2H5
8. preparation method according to claim 2, it is characterised in that:In step (2), the phosphorylcholine salt is phosphinylidyne Base choline mono-sodium salt and/or phosphorylcholine monopotassium salt.
9. according to any preparation method in claim 2-7, it is characterised in that:The step (2) is phosphoryl courage Alkali salt reacts double hydroxyls of generation L- α-glycerolphosphocholine with the double hydroxyl protection object I of the halogenated glycerine of (R) -3- in alcohols solvent Base protection II recycles alcohols solvent, is dissolved in water to obtain the crude product of double hydroxyl protection object II of L- α-glycerolphosphocholine Aqueous solution, wherein, with molar amount, the inventory of the double hydroxyl protection object I of the halogenated glycerine of (R) -3- is the 1.2 of phosphorylcholine salt To 3.0 times.
10. according to the preparation method described in claim 2, it is characterised in that:The step (3) is L- α-glycerophosphatide acyl courage The crude product aqueous solution of double hydroxyl protection object II of alkali extracts unreacted (R) -3- halogenated glycerine pair with water-insoluble organic solvent Hydroxyl protection object I, discards organic phase, double hydroxyl protection object II of the L- α-glycerolphosphocholine purified.
11. preparation method according to claim 10, it is characterised in that:In step (3), extractant is ether solvent first Base tertbutyl ether or esters solvent ethyl acetate, isobutyl acetate, isopropyl acetate or n-propyl acetate.
12. preparation method according to claim 1, it is characterised in that:The acid is selected from dilute hydrochloric acid, dilute sulfuric acid, by solution PH is adjusted to 1-3.
13. preparation method according to claim 1, it is characterised in that:After deprotection, by L- α-glycerolphosphocholine water Solution removes hydrochloric acid and remaining inorganic salts by ion exchange resin.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110128467A (en) * 2019-05-07 2019-08-16 天津康巢生物医药股份有限公司 A kind of process of purification of glycerol phosphatidyl choline crude product and its obtained glycerolphosphocholine

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0486100A1 (en) * 1990-11-15 1992-05-20 MAGIS FARMACEUTICI S.p.A. Process for preparing alpha-glycerophosphorylcholine
US5215973A (en) * 1991-03-07 1993-06-01 Magis Farmaceutici S.P.A. Optically active and racemic hydrated diacetylesters of α-glycero-phosphoryl-choline
WO2007145476A1 (en) * 2006-06-14 2007-12-21 Kim, Hyun Joo A process for preparation of l-alpha-glycerophosphoryl choline
CN101967160A (en) * 2010-09-09 2011-02-09 常熟富士莱医药化工有限公司 One-step method for preparing raceme DL, D or L-a-glycerin phosphorus acyl choline
CN103087091A (en) * 2011-10-27 2013-05-08 上海秀新臣邦医药科技有限公司 L-alpha-choline glycerophosphate synthesis method
CN104513267A (en) * 2014-01-11 2015-04-15 芜湖福民生物药业有限公司 Glycerophosphorylcholine preparation method
CN104844647A (en) * 2015-05-07 2015-08-19 芜湖福民生物药业有限公司 Preparation method of glycerinum phosphatidylcholine
CN104926862A (en) * 2015-05-07 2015-09-23 芜湖福民生物药业有限公司 Preparation method for glycerophosphatidylcholine

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0486100A1 (en) * 1990-11-15 1992-05-20 MAGIS FARMACEUTICI S.p.A. Process for preparing alpha-glycerophosphorylcholine
US5215973A (en) * 1991-03-07 1993-06-01 Magis Farmaceutici S.P.A. Optically active and racemic hydrated diacetylesters of α-glycero-phosphoryl-choline
WO2007145476A1 (en) * 2006-06-14 2007-12-21 Kim, Hyun Joo A process for preparation of l-alpha-glycerophosphoryl choline
CN101967160A (en) * 2010-09-09 2011-02-09 常熟富士莱医药化工有限公司 One-step method for preparing raceme DL, D or L-a-glycerin phosphorus acyl choline
CN103087091A (en) * 2011-10-27 2013-05-08 上海秀新臣邦医药科技有限公司 L-alpha-choline glycerophosphate synthesis method
CN104513267A (en) * 2014-01-11 2015-04-15 芜湖福民生物药业有限公司 Glycerophosphorylcholine preparation method
CN104844647A (en) * 2015-05-07 2015-08-19 芜湖福民生物药业有限公司 Preparation method of glycerinum phosphatidylcholine
CN104926862A (en) * 2015-05-07 2015-09-23 芜湖福民生物药业有限公司 Preparation method for glycerophosphatidylcholine

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110128467A (en) * 2019-05-07 2019-08-16 天津康巢生物医药股份有限公司 A kind of process of purification of glycerol phosphatidyl choline crude product and its obtained glycerolphosphocholine

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