CN108658882A - A kind of preparation method of Cyclen -1,4,7,10- tetraacethyls - Google Patents

A kind of preparation method of Cyclen -1,4,7,10- tetraacethyls Download PDF

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CN108658882A
CN108658882A CN201810255584.5A CN201810255584A CN108658882A CN 108658882 A CN108658882 A CN 108658882A CN 201810255584 A CN201810255584 A CN 201810255584A CN 108658882 A CN108658882 A CN 108658882A
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formula
compound
preparation
acid
meglumine
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李明
刘凯
王俊琰
梁冰
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Jiangsu Hengrui Medicine Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D257/00Heterocyclic compounds containing rings having four nitrogen atoms as the only ring hetero atoms
    • C07D257/02Heterocyclic compounds containing rings having four nitrogen atoms as the only ring hetero atoms not condensed with other rings
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F5/00Compounds containing elements of Groups 3 or 13 of the Periodic Table
    • C07F5/003Compounds containing elements of Groups 3 or 13 of the Periodic Table without C-Metal linkages

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Abstract

The present invention relates to a kind of preparation methods of 1,4,7,10 tetraazacyclododecanand, 1,4,7,10 tetraacethyl.Specifically, this method selects means re-crystallization to obtain high-purity compound of formula I, further, by meglumine, Gd2O3Gadoteric Acid meglumine can be obtained with compound of formula I complexing, the method is easy to operate, at low cost, environmentally protective, is suitable for mass producing.

Description

A kind of preparation of Cyclen -1,4,7,10- tetraacethyls Method
Technical field
The invention belongs to medicinal chemistry arts, are related to a kind of Isosorbide-5-Nitrae, 7,10- tetraazacyclododecanands-Isosorbide-5-Nitrae, 7,10- tetrems Acid and its complex compound preparation method.
Background technology
Gadoteric Acid meglumine (Gadoteric Acid Meglumine), the entitled Isosorbide-5-Nitrae of chemistry, 7,10- tetraazacyclododecanes 12 Alkane-Isosorbide-5-Nitrae, 7,10- tetraacethyl gadolinium meglumines are to be developed and listed by Guerbet, are used as the Magnetic resonance imaging radiography of cancer Agent.
Gadoteric Acid meglumine is that the ring-like gadolinium preparation of ion belongs to low-risk drug due to its design feature, is being listed 9 kinds of gadolinium contrast agent in, cause the risk of kidney source sexual system fibrosis (NSF) theoretically to be analyzed to be minimum.Compared to other Gadolinium contrast agent, this product indication is wider, and other than liver, this product can be used for maincenter, whole body and angiography,
Currently, existing literature report discloses the preparation method of a plurality of Gadoteric Acid meglumine, substantially it is summarized as follows:
Wangler et al. (Bioorganic&Medicinal Chemistry, 16,2606-2616,2008) report with Cycleanine and ethyl chloroacetate are raw material, and through N- nucleophilic displacement of fluorine, ester hydrolysis is acidified, and is reacted after gadolinium cooperation, then with meglumine Generate gadoterlc acid meglumine saltlniection.A large amount of sodium chloride are will produce in the reaction process to remove by organic extractant phase method, effect is excessively poor, Intermediate 2 is not readily passed through refined mode and is purified by design feature in the route simultaneously, and purifying process is cumbersome, uncomfortable Industrialized production is closed,
US5428156A is reacted by Mannich from torus Teng Ning and generates intermediate 6, is hydrolyzed under LiOH catalysis Obtain 1,4,7,10-tetraazacyclododecane-1,4,7,10-tetraacetic acid (also known as DOTA), then be complexed with gadolinium oxide, finally with Meglumine reaction generates Gadoteric Acid meglumine.Potassium cyanide is toxic articles in the route, is not suitable for technique productions,
US4963344 is then disclosed using cycleanine as raw material, occurs N- nucleophilic displacement of fluorine through monoxone, acidification, then with Portugal's first Amine, Gd2O3Complexing, the method that " one kettle way " prepares gadoterlc acid meglumine saltlniection.When technical staff repeats the technique, find due to intermediate Gadoteric Acid is unstable, and dissociating in finished product Gadoteric Acid meglumine, gadolinium concentrations are exceeded, and process repeatability is poor, is unsuitable for technique and puts Big production, and needed after obtaining Gadoteric Acid meglumine crude product without salt-removal steps in entire technical process, desalination operation is just carried out, To aggravate the difficulty and workload of technique desalination, it is not suitable for technique productions,
Meanwhile CN104955822A and CN105939994 disclose the purifying in the way of resin or nanofiltration and prepare gadolinium respectively Special acid meglumine intermediate DOTA, and utilize gained DOTA further with meglumine, Gd2O3Complexing prepares Gadoteric Acid meglumine Method.The technique greatest drawback be using resin or nanofiltration purifying intermediate DOTA production capacities it is not high, technique is cumbersome, while also depositing The risk of unknown impuritie is introduced in purifying resin.
For this purpose, the present invention provides a kind of preparation method of 1,4,7,10-tetraazacyclododecane-1,4,7,10-tetraacetic acid, Preparation is simple for this, environmentally protective, is suitable for the needs that industry produces greatly.
Invention content
The present invention provides a kind of system of Cyclen -1,4,7,10- tetraacethyls (Formulas I) compound Preparation Method, this method include:Compound of formula I crude product re-crystallization step will be contained.Recrystallization gained compound of formula I purity is not less than 95.0%, in embodiments can be 95.0%, 95.2%, 95.4%, 95.6%, 95.8%, 96.0%, 96.2%, 96.4%, 96.6%, 96.8%, 97.0%, 97.2%, 97.4%, 97.6%, 97.8%, 98.0%, 99.0% or higher,
Meanwhile gained compound of formula I compound of formula H content is not more than 1%.In some embodiments, Formula II chemical combination Object content can be 1%, 0.9%, 0.8%, 0.7%, 0.6%, 0.5%, 0.4%, 0.3%, 0.2%, 0.1%, 0.09%, 0.08%, 0.07%, 0.06%, 0.05%, 0.04%, 0.03%, 0.02%, 0.01% or smaller, further, the formula II compounds contents are not more than 0.5%, preferably no greater than 0.2%,
Formula II compound have with Formulas I chemical combination similar structures, chemical polarity is close, during preparation of compounds of formula I, formula II compounds invariably accompany generation, and are not easy to remove, and in Gadoteric Acid meglumine or Gadoteric Acid finished product, Formula II compound with The impurity of gadolinium complexing is also extremely not easy to remove.If compound of formula I compound of formula H content is more than 1%, subsequently gadolinium is being prepared During special acid or Gadoteric Acid meglumine, 0.05% cannot be down to once by resin or nanofiltration purifying, it is difficult to meet ICH Guideline requirement.
In embodiments, recrystallization solvent of the present invention is selected from least one of water, alcohols solvent, the alcohols Solvent is C1-6Alkylol can be at least one of methanol, ethyl alcohol, propyl alcohol;Further, the recrystallization solvent is selected from At least one of water, ethyl alcohol.
Further, when volume-weight ratio of re-crystallization step solvent for use amount of the present invention and compound of formula I crude product It needs to control in a certain range, such as selects nonelectrolyte mixed aqueous solution, the two ratio can be with 30:1~100:1, it in embodiments, can Think 30:1、35:1、40:1、45:1、50:1、55:1、60:1、65:1、70:1、75:1、80:1、85:1、90:1、95:1、 100:1。
If single solvent is selected to need, according to the solvent volume-weight ratio suitable to the selection of material dissolution performance, implementing In scheme, water is selected to be used as refining solvent, volume-weight ratio of solvent dosage and compound of formula I crude product is 1:2~5:1, in reality It applies in scheme, the two ratio can be 1:2、1:1.9、1:1.8、1:1.7、1:1.6、1:1.5、1:1.4、1:1.3、1:1.2、1: 1.1,1:1、1.4:1、1.6:1、1.8:1、2:1、2.2:1、2.4:1、2.6:1、2.8:1、3:1、3.2:1、3.4:1、3.6:1、 3.8:1、4:1、4.2:1、4.4:1、4.6:1、4.8:1、5.0:1, preferably 1:1~3:1.
During preparing Gadoteric Acid or Gadoteric Acid meglumine, salt content in intermediate DOTA is controlled into a certain range, this Sample not only can cause yield to reduce to avoid the intermediate exhaustive purification, but also can be to avoid the follow-up Gadoteric Acid of influence or Gadoteric Acid Portugal The purifying process of methylamine and the quality of subsequent product and yield.Salt content is not more than 20% in compound of formula I of the present invention, In embodiments can be 20,19,18,17,16,15,14,13,12,11,10,9,8,7,6,5,4,3,2,1% or smaller, Preferably no greater than 15%.
In embodiments, re-crystallization step of the present invention:
1) compound of formula I crude product is added in suitable solvent, heating stirring dissolving,
2) cooling crystallization is stirred,
3) it filters, washing, dry compound of formula I.
Further, formula Compound I crude product can by Isosorbide-5-Nitrae, 7,10- tetraazacyclododecanands (cycleanine) with Alkylated reaction obtains halogenated acetic acids under alkaline condition, as described below:
Wherein, X is halogen.
It being described as described in CN104955855, the alkylated reaction can be influenced by several factors, for example, halogen For the dosage of acetic acid, reaction time, reaction temperature etc..Alkali used in alkylated reaction of the present invention is selected from alkali metal hydroxide Object, preferably sodium hydroxide or potassium hydroxide.Except this, in embodiments, alkylated reaction also needs to strictly control reactant PH value in system, the usual alkylation reaction system alkaline pH are not more than 13, and the pair that can control the alkylation process very well is anti- It answers.Preferably 8~12, can be 8.0,8.2,8.4,8.6,8.8,9.0,9.1,9.2,9.3,9.4,9.5,9.6,9.7,9.8, 9.9、10.0、10.1、10.2、10.3、10.4、10.5、10.6、10.7、10.8、10.9、11.0、11.2、11.4、11.6、 11.8,12.0, more preferably 9.0~11.0.
Further, aforesaid alkylization reaction in halogenated acetic acids used can be iodoacetic acid, bromoacetic acid or chloracetic acid, it is excellent It is selected as chloracetic acid.
In some embodiments, prepared by 1,4,7,10-tetraazacyclododecane-1,4,7,10-tetraacetic acid (Formulas I) compound Method, including:
It is anti-that Cyclen (cycleanine) a) under alkaline condition to that alkyl occur with halogenated acetic acids It answers;
B) step a) after reaction, adjusts reaction solution pH to acidity, crystallization filters to obtain compound of formula I crude product;
C) compound of formula I crude product is recrystallized.
Further, the acid pH be not more than 3, in embodiments can be 3.0,2.9,2.8,2.7,2.6,2.5, 2.4,2.3,2.2,2.1,2.0,1.9,1.8,1.7,1.6,1.5,1.4,1.3,1.2,1.1,1.0, preferably 2.0~2.5.
The present invention also provides a kind of preparation method of Gadoteric Acid, this method includes the steps that above-mentioned preparation of compounds of formula I, with And by Gd2O3With the step of being complexed according to compound of formula I obtained by the preparation method.
The present invention also provides a kind of preparation method of Gadoteric Acid meglumine, this method includes above-mentioned preparation of compounds of formula I Step, and by Gd2O3, meglumine with being complexed according to compound of formula I obtained by above-mentioned preparation method the step of.
Detailed description of the invention
By the measurement of HPLC, the detection method is as follows for substance " content " of the present invention or " purity ":
2695 Alliance liquid chromatographs of Waters or 1200 liquid chromatographs of Agilent;
It is filler with octadecylsilane chemically bonded silica;It is respectively A, B mobile phase with 0.2% sodium ascorbyl phosphate, acetonitrile, ladder Degree elution, Detection wavelength 196nm.
Salometry can be by the method for HPLC in the present invention, and the retention time of salt is about 1.9min.May be used also By in the way of silver nitrate titration, then the content data for obtaining salt in sample can be quantified by simple mathematical calculations.It is described Silver nitrate titration method is known to those skilled in the art or it was determined that can also refer to the chief editors such as Liao Lifu《Analysisization It learns》Described in (publishing house of the Central China University of Science and Technology, 2015.8.).
Retention time about 19min in Formula II compound HPLC of the present invention, relative retention time 0.13.
Solvent dosage of the present invention is with volume units, and solid sample dosage is in terms of mass unit.
" volume-weight " of the present invention is stated:Compare between solvent for use volume and refining crude weight.
Free gadolinium assay method of the present invention:
Precision weighs this product 7.6g, sets in 250ml conical flasks, is dissolved in water, and pH to 5.0~7.5 is adjusted, with pyridine and two For cresols orange solution using the aobvious red of solution, it is in yellow to be titrated to solution with Calcium Disodium Versenate titrating solution.
If any free gadolinium in sample, calculated as the following formula:
Wherein:V is the volume (ml) of the titrating solution of consumption;Cs is the concentration (mol/ of Calcium Disodium Versenate titrating solution L);
M is the weight (g) of Gadoteric Acid meglumine test sample;
Quality standard provides Gadoteric Acid meglumine:It is calculated by anhydride, free gadolinium amount must not cross 0.013%.
After the use of resin is all activation in the present invention, the resin activated method is well known to those skilled in the art Or it is identifiable.For example, D311 is resin activated:Purified water is utilized to impregnate successively, the washing of 5% hydrochloric acid solution purifies water washing It is not more than 7 to efflux pH value, conductivity is not more than 10 μ/cm.
" alkyl " of the present invention refers to the aliphatic hydrocarbon group of saturation, and alkyl of the choosing containing 1 to 6 carbon atom (can be expressed as C1-6 alkyl).Non-limiting embodiment includes methyl, ethyl, n-propyl, isopropyl, normal-butyl, isobutyl group, tertiary butyl, Zhong Ding Base, n-pentyl, 1,1- dimethyl propyls, 1,2- dimethyl propyls, 2,2- dimethyl propyls, 1- ethyl propyls, 2- methyl butyls, 3- methyl butyls, n-hexyl, 1- Ethyl-2-Methyls propyl, 1,1,2- thmethylpropyls, 1,1- dimethylbutyls, 1,2- diformazans Base butyl, 2,2- dimethylbutyls, 1,3- dimethylbutyls, 2- ethyl-butyls, 2- methyl amyls, 3- methyl amyls.
It is of the present invention to be obtained by commercial sources with reagent.
Specific implementation mode
The present invention is explained in greater detail below with reference to embodiment, the embodiment of the present invention is merely to illustrate the skill of the present invention Art scheme, the spirit and scope of the invention are not limited thereto.
Embodiment 1
Be added 11.8kg monoxones and 12l purified waters into 100L reaction kettles, stirring and dissolving, be added under ice bath dissolved with 3.2kg cycleanines are suspended in 6l water and are added in reaction by the 15l water of 5kg sodium hydroxides, are warming up to 80~85 DEG C, are added dropwise Dissolved with the 6L water of 5.2kg sodium hydroxides, for control reaction system pH 10~11, overnight, 10.4l is added dropwise after being cooled to room temperature in reaction Concentrated hydrochloric acid adjusts pH to 2~2.5, and filter cake is collected by filtration in stirring and crystallizing, dry that DOTA crude product 7.5kg, Formula II compound contain Amount about 3.1%.
DOTA crude products 7.5kg, 18kg purified water is added in 50L reaction kettles, after heating stirring dissolving, cooling crystallization, mistake Filter, washing, dry that DOTA 6.21kg, yield 82.7%, wherein content salt amount are 2%, Formula II compounds content is 0.05%.
Embodiment 2:DOTA crude product refining methods are groped
It takes 20g DOTA crude products to be added in reaction bulb, is separately added into the solvent to be screened, after heating for dissolving, cooling and stirring analysis Crystalline substance filters to obtain DOTA samples, detects respectively, and records under data such as table 1:
Table 1
Note:
A can be detected in solvent screening by TLC (plate layer chromatography plate), after obtaining general evaluation, then through inspections such as HPLC Survey means further detect;
B is detected through HPLC, and gained DOTA purifying is 96.9%, content salt amount 3.07%, Formula II chemical combination object amount 0.02%;
C is detected through HPLC, and gained DOTA purifying is 95.7, content salt amount 10.27% (titration measurement), Formula II compound Amount 0.05%;
D is detected through HPLC, and gained DOTA purifying is 95.1, content salt amount 6.11% (titration measurement), Formula II compound Amount 0.10%;
E TLC testing conditions:Solvent methanol/ammonium hydroxide (10:1), product Rf values 0.5.
Conclusion:
It is not difficult to find out from above-mentioned data, 2,5,6 couples of DOTA of experimental example, which are purified, relatively good effect, and experimental example 1,7 Although poor to DOTA purification effects Deng institute's sample high income.
Embodiment 3:
In 50L purified waters, 1 gained DOTA 5.1kg of embodiment are added, after 40~50 DEG C of heating stirrings dissolve, respectively Be added meglumine (2.5kg), gadolinium oxide (2.33kg), pH value of solution=7-9, heating reaction 3h, filtering, successively with 001 × 7 and D311 resin desalinations obtain satisfactory Gadoteric Acid meglumine solution, are concentrated to dryness or are lyophilized and to obtain Gadoteric Acid meglumine 7.46kg, Yield 78.5%, Formula II content is 0.01% hereinafter, free gadolinium concentrations are less than 0.013% after testing, salt content zero.
Embodiment 4:
In 100mL purified waters, 2 gained DOTA 10g of experimental example are added, after heating stirring dissolving, add 4.7g oxidations Gadolinium, heating reaction 3h, filtering obtain satisfactory Gadoteric Acid solution successively with 001 × 7 and D311 resin desalinations, 35~40 DEG C It is concentrated to dryness or is lyophilized and to obtain Gadoteric Acid 9.42g, yield 67.9%, Formula II content is 0.01% hereinafter, free gadolinium concentrations after testing It is 0.042%, salt content zero.
Embodiment 5:
In 300mL purified waters, 1 gained DOTA 30g of embodiment are added and add 14.1g oxygen after heating stirring dissolving Change gadolinium, heating reaction 3h, filtering successively with 001 × 7 and D311 resin desalinations, obtains satisfactory Gadoteric Acid solution, is concentrated into Solution is committed to 200ml, then the solution is rushed into ethyl alcohol, and white solid is precipitated, dry that gadolinium is special at 35~40 DEG C after filtering Sour 26.4g yields 63.4%, Formula II content is 0.01% hereinafter, free gadolinium concentrations are 0.027% after testing, salt content zero.
Embodiment 6:
In 28mL purified waters, 6 gained DOTA 2.8g of experimental example are added and sequentially add 1.14g after heating stirring dissolving It is special to obtain satisfactory gadolinium successively with 001 × 7 and D311 resin desalinations for gadolinium oxide, meglumine, reaction solution pH to 7-9, filtering Sour meglumine solution, 35~40 DEG C are concentrated to dryness or are lyophilized and to obtain Gadoteric Acid meglumine 4.13g, yield 78.8%, after testing Formula II Content is 0.01% hereinafter, salt content is zero.

Claims (10)

1. a kind of preparation method of compound of formula I, including:The step of compound of formula I crude product recrystallizes, gained compound of formula I is pure Degree is not less than 95%, wherein the Formula II compounds content is not more than 1%, the preferably described recrystallization solvent is selected from water or alcohols is molten At least one of agent,
2. preparation method according to claim 1, it is characterised in that the compound of formula I compound of formula H content is little In 0.5%, preferably no greater than 0.2%.
3. preparation method according to claim 1 or 2, it is characterised in that salt content is not more than in the compound of formula I 20%, preferably no greater than 15%.
4. according to claim 1-3 any one of them preparation methods, it is characterised in that the compound of formula I crude product is by Isosorbide-5-Nitrae, and 7, Alkylated reaction obtains 10- tetraazacyclododecanands under alkaline condition with halogenated acetic acids.
5. preparation method according to claim 4, which is characterized in that alkali used in alkylation reaction is selected from alkali metal hydroxide Object, preferably sodium hydroxide, potassium hydroxide.
6. preparation method according to claim 4, it is characterised in that the alkaline pH no more than 13.0, preferably 8.0~ 12.0, more preferably 9.0~11.0.
7. preparation method according to claim 4, it is characterised in that the halogenated acetic acids is selected from iodoacetic acid, bromoacetic acid and chlorine Acetic acid.
8. according to claim 1-7 any one of them preparation methods, which is characterized in that the compound of formula I preparation method packet It includes:
A) alkylation reaction is occurred under alkaline condition for Cyclen and halogenated acetic acids;
B) step a) after reaction, adjusts reaction solution pH to acidity, crystallization filters to obtain compound of formula I crude product, the preferably described acid Property pH be not more than 3.0, more preferably 2.0~2.5;
C) by compound of formula I crude product through solvent recrystallization.
9. a kind of preparation method of Gadoteric Acid, including claim 1-8 any one of them preparation process and by Gd2O3With right It is required that obtained by any one of 1-8 the step of compound of formula I complexing.
10. a kind of preparation method of Gadoteric Acid meglumine, including claim 1-8 any one of them preparation process and general Gd2O3, compound of formula I obtained by meglumine and any one of claim 1-8 the step of being complexed.
CN201810255584.5A 2017-03-28 2018-03-27 A kind of preparation method of Cyclen -1,4,7,10- tetraacethyls Pending CN108658882A (en)

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CN111375070A (en) * 2018-12-26 2020-07-07 江苏恒瑞医药股份有限公司 Method for preparing contrast agent
CN111375071A (en) * 2018-12-26 2020-07-07 江苏恒瑞医药股份有限公司 Method for preparing contrast agent
CN113087680A (en) * 2020-01-08 2021-07-09 威智医药有限公司 DOTA crystal form and preparation method thereof
CN113527222A (en) * 2020-04-21 2021-10-22 威智医药有限公司 Preparation method of meglumine gadoterate
KR20210152656A (en) * 2020-06-09 2021-12-16 주식회사 엔지켐생명과학 Menufacturing of Gadoteric acid as Gadoterate meglumine Intermediate and Gadoterate meglumine
CN113801071A (en) * 2021-09-14 2021-12-17 安徽普利药业有限公司 Refining method of meglumine gadoterate

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111375070A (en) * 2018-12-26 2020-07-07 江苏恒瑞医药股份有限公司 Method for preparing contrast agent
CN111375071A (en) * 2018-12-26 2020-07-07 江苏恒瑞医药股份有限公司 Method for preparing contrast agent
CN111375071B (en) * 2018-12-26 2023-04-07 江苏恒瑞医药股份有限公司 Method for preparing contrast agent
CN113087680A (en) * 2020-01-08 2021-07-09 威智医药有限公司 DOTA crystal form and preparation method thereof
CN113527222A (en) * 2020-04-21 2021-10-22 威智医药有限公司 Preparation method of meglumine gadoterate
CN113527222B (en) * 2020-04-21 2023-06-13 威智医药股份有限公司 Preparation method of gadoteric acid meglumine
KR20210152656A (en) * 2020-06-09 2021-12-16 주식회사 엔지켐생명과학 Menufacturing of Gadoteric acid as Gadoterate meglumine Intermediate and Gadoterate meglumine
KR102445756B1 (en) * 2020-06-09 2022-09-21 주식회사 엔지켐생명과학 Menufacturing of Gadoteric acid as Gadoterate meglumine Intermediate and Gadoterate meglumine
CN113801071A (en) * 2021-09-14 2021-12-17 安徽普利药业有限公司 Refining method of meglumine gadoterate

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