CN110540555B - Method for dissociating nucleoside phosphate - Google Patents

Method for dissociating nucleoside phosphate Download PDF

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CN110540555B
CN110540555B CN201910444315.8A CN201910444315A CN110540555B CN 110540555 B CN110540555 B CN 110540555B CN 201910444315 A CN201910444315 A CN 201910444315A CN 110540555 B CN110540555 B CN 110540555B
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陈埔
侯云艳
樊波
蔡洪芳
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Jiangsu Hengrui Medicine Co Ltd
Chengdu Suncadia Pharmaceuticals Co Ltd
Chengdu Xinyue Medicine Co Ltd
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Chengdu Suncadia Pharmaceuticals Co Ltd
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    • C07HSUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H1/00Processes for the preparation of sugar derivatives
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    • C07ORGANIC CHEMISTRY
    • C07HSUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H19/00Compounds containing a hetero ring sharing one ring hetero atom with a saccharide radical; Nucleosides; Mononucleotides; Anhydro-derivatives thereof
    • C07H19/02Compounds containing a hetero ring sharing one ring hetero atom with a saccharide radical; Nucleosides; Mononucleotides; Anhydro-derivatives thereof sharing nitrogen
    • C07H19/04Heterocyclic radicals containing only nitrogen atoms as ring hetero atom
    • C07H19/06Pyrimidine radicals
    • C07H19/10Pyrimidine radicals with the saccharide radical esterified by phosphoric or polyphosphoric acids

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Abstract

The present invention provides a method for liberating nucleoside phosphates. Specifically, the present invention provides an environmentally friendly, novel method for liberating nucleoside phosphates, which avoids the use of a large amount of cation exchange resin and water, and reduces industrial costs.

Description

Method for dissociating nucleoside phosphate
Technical Field
The invention relates to an environment-friendly and novel method for preparing free nucleoside phosphate.
Background
Diquafosol tetrasodium salt, also known as P 1 ,P 4 -bis (uridine 5' -) tetrasodium tetraphosphate, having the structure shown below,
Figure BDA0002073127090000011
diquafosol tetrasodium is a dibasic uridine nucleotide analog, which is a P2Y2 receptor agonist and a mucin secretion stimulator, and 3% of diquafosol tetrasodium salt eye drops have been developed by japan panacea corporation for the treatment of dry eye. In addition, it is possible to develop an expectorant or a therapeutic drug for pneumonia, which has an effect of inducing expectoration.
The prior art discloses a large number of documents relating to P 1 ,P 4- The synthesis of disodium bis (uridine 5' -) tetraphosphate, summarized basically as follows, comprises liberating disodium uridine-5 ' -monophosphate by cationic resin as uridine-5 ' -monophosphate, then forming n-butylamine uridine-5 ' -monophosphate salt (UMP-TBA), liberating trisodium uridine-5 ' -triphosphate by cationic resin as uridine-5 ' -triphosphate, then forming tri-n-butylamine uridine-5 ' -triphosphate salt (UTP-3 TBA), wherein the eluent is water when liberated, and reacting UMP-TBA with UTP-3TBA by condensing agent to obtain P-TBA 1 ,P 4- Bis (uridine 5'-) tetraphosphoric acid, and then converting the acid into a sodium salt to obtain a final product, as specifically disclosed in the prior art CN107056859A, CN1292795A and the like.
This process for the preparation of uridine phosphates typically requires the use of large amounts of cation exchange resin and water, while removing the water azeotropically by lyophilization or by large amounts of solvent over a long period of time, is a time, energy and solvent consuming process. In addition, high boiling tributylamine is required to neutralize uridine phosphates due to lyophilization and azeotropic water entrainment. Tributylamine is listed as a highly toxic chemical, and is not favorable for safe operation and environmental protection.
The present invention provides an environment-friendly, novel method for dissociating nucleoside phosphate, which avoids the use of a large amount of cation exchange resin and water, and reduces industrial costs.
Disclosure of Invention
The present invention provides an environment-friendly, novel method for dissociating nucleoside phosphate, which avoids the use of a large amount of cation exchange resin and water, and reduces industrial costs.
The present invention provides a process for liberating a compound represented by the formula (I) into an acid, which is characterized by the step of contacting a compound represented by the formula (I) in an organic solvent with a cation exchange resin,
Figure BDA0002073127090000021
wherein Y is selected from
Figure BDA0002073127090000022
Preference is given to
Figure BDA0002073127090000023
X is selected from Na + 、K + 、NH 4 + Preferably Na +
n and m are each independently selected from 1, 2, 3, 4, 5.
The compounds of formula (I) described in the present invention optionally contain one or more water.
The organic solvent in the present invention is selected from the group consisting of N, N-Dimethylformamide (DMF), dimethylacetamide (DMAC), dioxane, tetrahydrofuran, acetone, acetonitrile, dimethyl sulfoxide, dimethyl imidazolidinone, hexamethylphosphoric triamide, trimethyl phosphate, triethyl phosphate or a mixture thereof, preferably N, N-dimethylformamide.
The method provided by the invention further comprises a step of separating the organic solvent from the cation exchange resin, and the method can be filtration, throwing filtration and the like.
The method for dissociating the compound shown as the formula I into the corresponding acid is characterized in that the cation exchange resin is gel type strong acid cation exchange resin, such as DOWEX IR100S H type resin.
In the dissociation method provided by the invention, the mass ratio of the cation exchange resin to the compound shown in the formula I is selected from 1-30, preferably 2-10, and most preferably 3-5.
In the dissociation method provided by the invention, the dissociation temperature is selected from-15-70 ℃, preferably-5-30 ℃, and most preferably 10-15 ℃.
In the dissociation method provided by the invention, the mass-to-volume (g/mL) ratio of the compound represented by the formula (I) to the organic solvent is selected from 0.05 to 0.50, preferably 0.1 to 0.4, and most preferably 0.25 to 0.35.
The free method provided by the invention can be selected from the following operation modes:
a) Mixing the cation exchange resin with an organic solvent;
b) Adding a compound shown in a formula (I) under stirring;
c) The corresponding free acid is obtained by filtration.
In the dissociation method provided by the present invention, the compound represented by the formula (I) is preferably
Figure BDA0002073127090000031
The invention further provides a P 1 ,P 4 Process for the preparation of (uridine 5' -) tetraphosphate, characterised in that it comprises the free compound of formula (Ia) or (Ib) as defined aboveThe steps are performed in the presence of a compound represented by the formula (IIa) and a compound represented by the formula (IIb).
P provided by the invention 1 ,P 4 A process for the preparation of (E) -bis (uridine 5' -) tetraphosphate, further comprising the step of forming an amine salt of the compound of formula (IIa) and (IIb) in an aprotic organic solvent.
P provided by the invention 1 ,P 4 -bis (uridine 5' -) tetraphosphate, wherein said aprotic organic solvent is selected from the group consisting of N, N-Dimethylformamide (DMF), dimethylacetamide (DMA), dimethylsulfoxide, alone or in combination, preferably N, N-Dimethylformamide (DMF).
P provided by the invention 1 ,P 4 The amine of the amine salt in the process for the preparation of (uridine 5' -) tetraphosphoric acid is selected from the group consisting of triethylamine, N-diisopropylethylamine, tributylamine, trioctylamine, tetrabutylammonium, heterocyclic amines, preferably triethylamine.
In the preparation method provided by the invention, the water content in the aprotic organic solution of the amine salt of the compound shown in the formula (IIa) and the compound shown in the formula (IIb) is controlled to be less than 1.0%, preferably less than 0.7%, and more preferably less than 0.3%.
In the method provided by the invention, the water removal of the aprotic organic solution of the compounds represented by the formula (IIa) and the formula (IIb) can be carried out by using a molecular sieve, azeotropic method or freeze-drying method.
P provided by the invention 1 ,P 4 A process for producing (E) -bis (uridine 5' -) tetraphosphate, further comprising the step of reacting an amine salt of the compound represented by formula (IIa) or (IIb) with a condensing agent and a metal ion catalyst.
The condensing agent of the present invention is selected from: dicyclohexylcarbodiimide, water-soluble carbodiimide, diisopropylcarbodiimide, 1- (3-dimethylaminopropyl) -3-ethylcarbodiimide or a hydrochloride thereof, carbonyldiimidazole, and preferably diisopropylcarbodiimide.
The metal salt catalyst is selected from magnesium salt, zinc salt, calcium salt, ferric salt, manganese salt and barium salt, and calcium salt is preferred.
The calcium salt according to the present invention is not particularly limited, and specifically, calcium fluoride, calcium chloride, calcium bromide, calcium iodide, calcium sulfate, calcium nitrate, calcium phosphate, calcium perchlorate, calcium tetrafluoroborate, calcium trifluoromethanesulfonate, calcium methanesulfonate, calcium toluenesulfonate, calcium acetate, calcium trifluoroacetate, calcium stearate, and calcium citrate can be exemplified, and calcium chloride is preferable.
In the preparation method provided by the invention, the molar ratio of the metal ion catalyst to the compound shown in the formula (IIb) is selected from 0.1-5, preferably 1.0-2, and most preferably 1.1-1.5.
The optimal method provided by the invention is specifically carried out by a process shown in Scheme 1:
Figure BDA0002073127090000041
in the method provided by the invention, after the reaction is finished, P for the synthetic target substance 1 ,P 4 The di (uridine 5' -) tetraphosphate can be isolated and purified by appropriately combining methods used in the isolation and purification of a usual nucleotide (for example, recrystallization, ion exchange column chromatography, adsorption column chromatography, activated carbon column chromatography, etc.), and then prepared in the form of a sodium salt.
The invention provides a P 1 ,P 4 Process for the preparation of tetrasodium (uridine 5' -) tetraphosphate, characterized in that it comprises the above-mentioned preparation of P 1 ,P 4 -bis (uridine 5' -) tetraphosphate.
The invention provides a method for synthesizing P 1 ,P 4 Preparation of P from-bis (uridine 5' -) tetraphosphate 1 ,P 4 Process for the adsorption of P-tetra sodium-bis (uridine 5' -) tetraphosphate using an anion exchange resin 1 ,P 4 -bis (uridine 5' -) tetraphosphate followed by a fast elution with sodium chloride solution as eluent.
The invention provides a process for preparing P 1 ,P 4 The process for the production of sodium-bis (uridine 5' -) tetraphosphate further comprises one or more operations selected from nanofiltration, activated carbon adsorption, recrystallization.
The method provided by the invention avoids nanofiltration, freeze-drying or azeotropic dehydration, and shortens the total synthesis time by 40%. Meanwhile, the usage amount of resin is reduced by 60%, the usage amount of water and solvent is greatly reduced, and the yield of the target product is as high as 73.9%. (calculated as the conversion of UTP)
Detailed Description
The present invention will be explained in more detail with reference to examples, which are provided only for illustrating the technical solutions of the present invention and the spirit and scope of the present invention are not limited thereto.
Uridine-5 '-monophosphate disodium salt and uridine-5' -triphosphate trisodium salt were used in the experiments and were purchased commercially.
Example 1
1. Preparation of intermediate Compound (IIIa) (UMP-TEA)
60mL of Dowex IR100s H type resin was added to a 150mL glass suction filter funnel, suction filtered, rinsed twice with 20mL of N, N-Dimethylformamide (DMF), and suction filtered until no droplets were evident. The resin was transferred to a 250ml single neck flask, 55ml of N, N-Dimethylformamide (DMF) was added, uridine 5' -monophosphate disodium salt (54.3 mmol,20.0 g) was added in one portion with magnetic stirring, reacted at room temperature (15 ℃) for 2h, filtered through a glass suction filter funnel, stirred with 55ml of 2N, N-dimethylformamide and combined in N, N-dimethylformamide solution. Triethylamine (54.3 mmol,5.5 g) was added dropwise to the N, N-dimethylformamide solution while stirring, and the temperature was raised slightly, after the addition, the reaction was stirred at room temperature for 30min to obtain a N, N-dimethylformamide solution of UMP-TEA. Adding activated molecular sieve
Figure BDA0002073127090000051
The form (90.0 g) was dried and the water content was determined to be not more than 0.2%, and the filtered liquid was directly transferred to the next step.
2. Preparation of intermediate Compound (IIIb) (UTP-3 TEA)
60ml of Dowex IR100s H-type resin was added to a 150mL glass suction filter funnel, suction filtered, rinsed twice with 20ml of N, N-dimethylformamide, and suction filtered until no significant droplets were present. The resin was transferred to a 250ml single-neck flask, 55ml of N, N-dimethylformamide was added, and uridine 5' -triphosphate trisodium salt (48.9mmol, 27.0 g) was added in one portion under magnetic stirring, and the mixture was inverted at room temperature (15 ℃ C.)The reaction solution is filtered by a glass suction filter funnel for 2 hours, and then is stirred and washed by 55mx 2N and N-dimethylformamide, and the N, N-dimethylformamide solution is combined. To the above DMF solution was added dropwise triethylamine (163mmol, 16.5 g) with stirring, and after the addition, the reaction was stirred at room temperature for 30min to obtain a DMF solution of UTP-3 TEA. Adding activated molecular sieve
Figure BDA0002073127090000052
The form (90.0 g) was dried and the water content was determined to be not more than 0.2%, and the filtered liquid was directly transferred to the next step.
3.P 1 ,P 4 Preparation of-bis (uridine 5' -) tetraphosphate
The prepared UTP-3TEA in N, N-dimethylformamide (UTP-3 TEA 3.80g, 4.83mmol) was placed in a 100ml three-necked flask, and diisopropylcarbodiimide (554mg, 5.80mmol), N-diisopropylcarbodiimide (554mg, 5.80mmol) was added 2 After 2 times of replacement, reacting for 5 hours at 25-30 ℃; to the reaction solution were added a solution of UMP-TEA in N, N-dimethylformamide (UMP-TEA 2.46g, 5.80mmol), anhydrous calcium chloride (484mg, 5.80mmol), followed by reaction at 25 to 30 ℃ for 5 hours, followed by sampling and HPLC analysis, and the UP4U content was calculated by area normalization in terms of the UTP conversion (yield: 73.9%).
Comparative example 1
1. Preparation of uridine-5' -monophosphoric tri-n-butylamine (UMP-TBA)
Adding uridine-5' -monophosphate disodium salt (54.3mmol, 20.0g) and purified water (100 g) into a 250mL glass beaker, dissolving completely under stirring, and filtering to obtain a filtrate for later use; loading 200mL of DOWEX IR100S resin converted into hydrogen form into a chromatographic column, washing with purified water (400 g), compacting the resin, discharging bubbles, discharging the washing solution, and closing a liquid discharge switch; slowly introducing the filtrate into a column, allowing the upper liquid level to just submerge the resin, standing, adding purified water (950 g) into the column for column chromatography, stopping elution when the pH of the eluent is 6.5-7.5, mixing the eluates, adding into a 2L reaction bottle, stirring, and dropwise adding tri-n-butylamine (9.2 g) to pH6.5-7.5 at 15-25 deg.C; the reaction solution was concentrated to a small volume by nanofiltration, and then lyophilized to remove water to obtain 25.3g. The residue was dissolved in N, N-dimethylformamide (85 mL) to make a solution of about 0.65mol/L IIa, and the activated molecule was addedSieve
Figure BDA0002073127090000061
Drying, measuring water content not more than 0.2%, filtering, and transferring the liquid to next step.
2. Preparation of uridine-5' -triphosphate, tri-n-butylamine salt (UTP-3 TBA)
Adding uridine-5' -triphosphate trisodium salt (45.4 mol, 25g) and purified water (125 g) into a 250mL plastic bucket, dissolving completely under stirring, and filtering to obtain filtrate for later use; 300mL of DOWEX IR100S resin converted to the hydrogen form was loaded into a chromatography column, washed with purified water (600 g), the resin was compacted, the wash was drained after venting the gas bubbles, and the drain switch was closed. Slowly introducing the filtrate into a column to ensure that the liquid level of the upper layer just submerges the resin, standing, adding purified water (1.30 kg) into the column for column-passing elution, controlling the flow rate until the pH value of the eluent is 6.5-7.5, stopping elution, combining the eluents, adding the eluates into a 2L reaction bottle, starting stirring, and dropwise adding tri-n-butylamine (22.7 g) to the pH value of 6.5-7.5 at 15-25 ℃; the reaction solution was concentrated by nanofiltration to a small volume and then lyophilized to remove water to obtain 42.5g. The residue was dissolved in N, N-dimethylformamide (140 mL) to prepare an about 0.32mol/L IIb solution, and activated molecular sieves were added
Figure BDA0002073127090000062
Drying, measuring water content not more than 0.2%, filtering, and transferring the liquid to next step.
3.P 1 ,P 4 Preparation of-bis (uridine 5' -) tetraphosphate
The prepared UTP-3TBA in N, N-dimethylformamide (UTP-3 TBA 5.02g, 4.83mmol) was placed in a 100ml three-necked flask and diisopropylcarbodiimide (562mg, 4.44mmol), N-dimethylformamide, added 2 After 2 times of replacement, reacting for 5 hours at 25-30 ℃; a solution of UMP-TBA in N, N-dimethylformamide (UMP-TBA 2.96g, 5.80mmol) and anhydrous calcium chloride (492mg, 4.43mmol) were added to the reaction mixture, and the mixture was reacted at 25 to 30 ℃ for 5 hours, followed by sampling and HPLC analysis, and the UP4U content was calculated by area normalization based on the conversion of UTP (yield: 75.9%).
The yields of the examples and comparative examples were substantially identical. However, the reaction time of the examples only needs 12The hour was 62 hours compared to the comparative example. The examples were carried out without water, whereas the comparative examples used 2176g of water. The examples only require 1/4 of the resin of the comparative example. The examples use triethylamine, which is less toxic, instead of tributylamine, which is highly toxic. Therefore, the invention provides an environment-friendly, energy-saving and time-saving P 1 ,P 4 A synthetic preparation method of (uridine 5' -) tetraphosphate.
Comparing the experimental results of the examples and comparative examples:
Figure BDA0002073127090000071

Claims (32)

1. a process for liberating a compound represented by the formula (I) into an acid, which comprises the step of contacting a compound represented by the formula (I) with a cation exchange resin in an organic solvent,
Figure FDA0003901505840000011
wherein Y is selected from
Figure FDA0003901505840000012
X is selected from Na + 、K + 、NH 4 +
n and m are each independently selected from 1, 2, 3, 4, 5;
the organic solvent is selected from N, N-dimethylformamide, dimethylacetamide, dioxane, tetrahydrofuran, acetone, acetonitrile, dimethyl sulfoxide, dimethyl imidazolidinone, hexamethylphosphoric triamide, trimethyl phosphate, triethyl phosphate or a mixture thereof;
the cation exchange resin is gel type strong acid cation exchange resin.
2. A process for liberating a compound represented by the formula (I) into an acid, which comprises the step of contacting a compound represented by the formula (I) with a cation exchange resin in an organic solvent,
Figure FDA0003901505840000013
wherein Y is
Figure FDA0003901505840000014
X is Na +
n and m are each independently selected from 1, 2, 3, 4, 5;
the organic solvent is selected from N, N-dimethylformamide, dimethylacetamide, dioxane, tetrahydrofuran, acetone, acetonitrile, dimethyl sulfoxide, dimethyl imidazolidinone, hexamethylphosphoric triamide, trimethyl phosphate, triethyl phosphate or a mixture thereof;
the cation exchange resin is gel type strong acid cation exchange resin.
3. The process according to any one of claims 1-2, characterized in that the organic solvent is N, N-dimethylformamide.
4. The method according to any one of claims 1 to 2, characterized by further comprising a step of separating the organic solvent from the cation exchange resin.
5. The process according to any one of claims 1-2, characterized in that the mass ratio of the cation exchange resin to the compound of formula (i) is selected from the range of 1 to 30.
6. The process according to any one of claims 1-2, characterized in that the mass ratio of the cation exchange resin to the compound of formula (i) is selected from the range of 2 to 10.
7. The process according to any one of claims 1-2, characterized in that the mass ratio of the cation exchange resin to the compound of formula (i) is selected from 3 to 5.
8. The method according to any one of claims 1-2, wherein the temperature of liberation is selected from the group consisting of-15 to 70 ℃.
9. The method according to any one of claims 1-2, wherein the temperature of liberation is-5 to 30 ℃.
10. The method according to any one of claims 1-2, characterized in that the temperature of liberation is selected from 10-15 ℃.
11. The process according to any one of claims 1-2, wherein the mass to volume (g/mL) ratio of the compound of formula (i) to the organic solvent is selected from 0.05 to 0.55.
12. The process according to any one of claims 1-2, characterized in that the mass to volume (g/mL) ratio of the compound of formula (i) to the organic solvent is selected from 0.1 to 0.4.
13. The process according to any one of claims 1-2, characterized in that the mass to volume (g/mL) ratio of the compound of formula (i) to the organic solvent is selected from the range of 0.25 to 0.35.
14. The method according to any one of claims 1-2, wherein the compound of formula (i) is selected from the group consisting of
Figure FDA0003901505840000021
15. P 1 ,P 4 -a process for the preparation of di (uridine 5' -) tetraphosphate comprising the process according to claim 14, wherein said compound of formula (Ia) or (Ib) is free as the corresponding acid, a compound of formula (IIa) or (IIb),
Figure FDA0003901505840000022
16. the method according to claim 15, further comprising a step of forming an amine salt of the compound represented by the formula (IIa) or (IIb) in an aprotic organic solvent.
17. The method according to claim 16, wherein the aprotic organic solvent is selected from the group consisting of N, N-dimethylformamide, dimethylacetamide and dimethylsulfoxide.
18. The method according to claim 16, wherein the aprotic organic solvent is N, N-dimethylformamide.
19. The method of claim 17, wherein the amine forming salt of an amine is selected from the group consisting of triethylamine, N-diisopropylethylamine, tributylamine, trioctylamine, tetrabutylammonium, and heterocyclic amines.
20. The method of claim 17, wherein the amine forming amine salt is triethylamine.
21. The process according to claim 19, wherein the water content of the aprotic organic solution of the amine salt of the compound represented by the formula (IIa) or (IIb) is controlled to less than 1.0%.
22. The process according to claim 19, wherein the water content of the aprotic organic solution of the amine salt of the compound represented by the formula (IIa) or (IIb) is controlled to less than 0.7%.
23. The process according to claim 19, wherein the water content of the aprotic organic solution of the amine salt of the compound represented by the formula (IIa) or (IIb) is controlled to less than 0.3%.
24. The method according to any one of claims 15 to 23, further comprising the step of reacting an amine salt of a compound represented by the formula (iia) and (iib) with a condensing agent selected from dicyclohexylcarbodiimide, water-soluble carbodiimide, diisopropylcarbodiimide, 1- (3-dimethylaminopropyl) -3-ethylcarbodiimide or a hydrochloride thereof, carbonyldiimidazole; the metal salt catalyst is selected from magnesium salt, zinc salt, calcium salt, iron salt, manganese salt and barium salt.
25. The method according to any one of claims 15 to 23, further comprising the step of reacting an amine salt of a compound represented by the formula (iia) and (iib) with a condensing agent which is diisopropylcarbodiimide; the metal salt catalyst is calcium salt.
26. The method of claim 24, wherein the calcium salt is selected from the group consisting of calcium fluoride, calcium chloride, calcium bromide, calcium iodide, calcium sulfate, calcium nitrate, calcium phosphate, calcium perchlorate, calcium tetrafluoroborate, calcium triflate, calcium methanesulfonate, calcium toluenesulfonate, calcium acetate, calcium trifluoroacetate, calcium stearate, and calcium citrate.
27. The method of claim 24, wherein the calcium salt is calcium chloride.
28. The method according to claim 24, wherein the molar ratio of the metal ion catalyst to the compound represented by the formula (IIb) is selected from the range of 0.1 to 5.
29. The method according to claim 24, wherein the molar ratio of the metal ion catalyst to the compound represented by the formula (IIb) is selected from the range of 1.0 to 2.
30. The method according to claim 24, wherein the molar ratio of the metal ion catalyst to the compound represented by the formula (IIb) is selected from the range of 1.1 to 1.5.
31. P 1 ,P 4 Process for the preparation of tetrasodium (uridine 5' -) tetraphosphate, comprising the preparation of P according to claim 24 1 ,P 4 -bis (uridine 5' -) tetraphosphate, further comprising a step of forming a sodium salt.
32. P 1 ,P 4 Process for the preparation of tetrasodium-salt of (E) -bis (uridine 5' -) tetraphosphate, characterized in that it comprises the preparation of P according to any one of claims 25 to 30 1 ,P 4 -bis (uridine 5' -) tetraphosphate, further comprising a step of forming a sodium salt.
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