CN103601702B - A kind of preparation method of lomerizine hydrochloride - Google Patents

A kind of preparation method of lomerizine hydrochloride Download PDF

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CN103601702B
CN103601702B CN201310591413.7A CN201310591413A CN103601702B CN 103601702 B CN103601702 B CN 103601702B CN 201310591413 A CN201310591413 A CN 201310591413A CN 103601702 B CN103601702 B CN 103601702B
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compound
formic acid
preparation
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molar ratio
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CN103601702A (en
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吴荣贵
于年余
李大军
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Dijia Pharmaceutical Group Co ltd
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Disha Pharmaceutical Group Co Ltd
Weihai Disu Pharmaceutical Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D295/00Heterocyclic compounds containing polymethylene-imine rings with at least five ring members, 3-azabicyclo [3.2.2] nonane, piperazine, morpholine or thiomorpholine rings, having only hydrogen atoms directly attached to the ring carbon atoms
    • C07D295/04Heterocyclic compounds containing polymethylene-imine rings with at least five ring members, 3-azabicyclo [3.2.2] nonane, piperazine, morpholine or thiomorpholine rings, having only hydrogen atoms directly attached to the ring carbon atoms with substituted hydrocarbon radicals attached to ring nitrogen atoms
    • C07D295/08Heterocyclic compounds containing polymethylene-imine rings with at least five ring members, 3-azabicyclo [3.2.2] nonane, piperazine, morpholine or thiomorpholine rings, having only hydrogen atoms directly attached to the ring carbon atoms with substituted hydrocarbon radicals attached to ring nitrogen atoms substituted by singly bound oxygen or sulfur atoms
    • C07D295/096Heterocyclic compounds containing polymethylene-imine rings with at least five ring members, 3-azabicyclo [3.2.2] nonane, piperazine, morpholine or thiomorpholine rings, having only hydrogen atoms directly attached to the ring carbon atoms with substituted hydrocarbon radicals attached to ring nitrogen atoms substituted by singly bound oxygen or sulfur atoms with the ring nitrogen atoms and the oxygen or sulfur atoms separated by carbocyclic rings or by carbon chains interrupted by carbocyclic rings

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The present invention relates to a kind of preparation method of lomerizine hydrochloride, belong to bulk pharmaceutical chemicals preparing technical field.Technical solution of the present invention has also efficiently controlled the quality of product by adding solvent in the reaction system and by adjusting material input ratio, improving yield, and the crude product purity of lomerizine hydrochloride reaches more than 99.8%.

Description

A kind of preparation method of lomerizine hydrochloride
Technical field
The present invention relates to a kind of preparation method of lomerizine hydrochloride, belong to bulk pharmaceutical chemicals preparing technical field.
Background technology
Lomerizine hydrochloride is a kind of new calcium channel blocker, is mainly used for treating antimigraine.Antimigraine is a kind of anti- The common disease made is recurred, its cause of disease is still not clear.Compared with flunarizine hydrochloride, in a short time effect become apparent from and adverse reaction more Lightly.In addition stronger to cerebrovascular selectivity, increase brain blood flow, protect the effect of brain tissue stronger, influence to heart compared with It is small.There is the advantages of it is unique in terms for the treatment of and preventing antimigraine, therefore before the exploitation of lomerizine hydrochloride has good market Scape.
There are two kinds of crystal forms, crystal form I and II, referring to document [Journal of Pharmaceutical for lomerizine hydrochloride Sciences, 85 (7), 761-766;1996], crystal form I is stable below 64% in 25 DEG C of room temperature and humidity, is not inhaled Tide.And crystal form II, under the conditions of 25 DEG C of room temperature, humidity begins to the moisture absorption more than 0%, when reaching humidity 20%, can absorb 2 The water of molar equivalent.Therefore preparing needs product to be prepared to change into the storage that crystal form I could be steady in a long-term at normal temperatures and be adapted to For pharmaceutical preparation.The preparation method of crystal form I and II is reported at the same time, and crystal form I is obtained from recrystallized from acetonitrile, and crystal form II is from first It is prepared in alcohol, ethanol, normal propyl alcohol, isopropanol, n-butanol and butanone.
The synthesis of prior art lomerizine hydrochloride has following several method:
First, benzyl halide method of substitution:
Document [Synthesis, (12), 1989-1991;2010] using 2,3,4- trimethoxy bromobenzyls and 1- [double-(4- Fluorophenyl) methyl] piperazine is reacted, then by silica gel post separation, obtains Lomerizine, yield 90%, it is anti-not carry out into salt Should.Due to silicagel column separation, impurity removal to be used, be not suitable for industrialized production.
Document Chinese Journal of Pharmaceuticals, 34 (11), 539-540;2003, using 2,3,4- trimethoxy benzyl chlorine and 1- [double-(4- fluorophenyls) methyl] piperazine is reacted into 4 rows, then by obtaining lomerizine hydrochloride crude product into salt, yield 73%, not Carry out turning crystalline substance.
Document China Medicine University journal, 33 (2):164~166;2002 also use the method, into salt after turn total after crystalline substance again Yield is 56%.Since the reactivity of 2,3,4- trimethoxy benzyl chlorine is relatively low, causes yield substantially relatively low, be unfavorable for big life Produce the reduction of cost.
In addition compound V is to have larger irritation and tearing property containing benzyl chloride or benzyl bromide a-bromotoluene, this kind of compound, because This requires labor protection rank especially high.Limitation is applied to big production.
Second, Leuckart-Wallach methods:
The raw material of this reaction are readily available, and low to labor protection rank.Therefore most of document report uses this Method.Document Chemical & Pharmaceutica1Bulletin, 35 (8), 3270-5;1987, by compound I and compound II is heated to 120 DEG C of meltings, then formic acid reaction is added dropwise, and the yield into salt is 40%.
Document Radioisotopes, 37 (5), 265-8;1988, compound I and compound II are heated to 150 DEG C and melted Melt, then formic acid reaction is added dropwise, the yield into salt is 50.6%.
Document China journal of Medicinal Chemistry, 13 (5), 297-298;2003, it is heated to using by compound I and compound II 100 DEG C of meltings, then formic acid reaction is added dropwise, it is 83% through turning brilliant total recovery again into salt.Chinese patent CN1562988A is using same The method of sample, into salt after to turn brilliant total recovery again be 55.6%.
From the point of view of the experimentation of report, the prior art in the reaction and is not added with any solvent and makees diluent, total recovery It is relatively low.The all of above product prepared has no purity report and method report is controlled to impurity therein.
The content of the invention
Head technical problems to be solved of the invention are to overcome the synthesis technique total recovery of existing lomerizine hydrochloride relatively low Problem.Second object of the present invention is to solve the problems, such as that product purity is poor.
The present invention still uses Leuckart-Wallach methods.Found by studying, raw material II can be reacted with formic acid Formylated impurity IV is generated, this is an inevitable side reaction, more or less.
By research reaction, when temperature is less than 100 DEG C, the growing amount meeting showed increased of impurity IV, the amount of product is reduced. Therefore the temperature of reaction system cannot be below 100 DEG C, otherwise influence yield.Additionally by experiment find Lomerizine in high temperature and Under acid condition, demethylation can occur and generate following two impurity V and VI.
Since impurity V and VI and Lomerizine structure are very close, in salification process and subtractive process with hydrochloric acid Lome Sharp piperazine forms eutectic, it is difficult to removes.The two impurity once being formed, can not just be removed, therefore must pass through by method for crystallising Reaction process carries out the formation of the two impurity to control.
Because formic acid is reactant, participates in reaction and obtain Lomerizine, but itself be also the original for producing impurity IV, V and VI Cause.Therefore the concentration of formic acid in reaction solution is reduced, and it is the best of these impurity contents in reduction finished product to separate immediately Method.In order to realize this purpose, we using into reaction system add solvent be diluted and use be added dropwise while The method of distillation is reacted, and immediately distills the formic acid of non-immediate reaction immediately, prevents that formic acid is rich in the reaction system Collection.By research, appropriate solvent effect is added clearly.Technical grade formic acid has two kinds, and one kind is anhydrous formic acid, another It is 85%~88% water-containing formic acid, both put into reaction effect no significant difference.Water and formic acid can steam when higher than 100 DEG C Issue, but due to immediately be added dropwise when reaction system in water and amount of formic acid it is fewer, in the case of no solubilizer be difficult It is steamed out, and can forms azeotropic mixture after adding nonaqueous solvents and immediately take away both of which at the same time, while so can guarantee that system Temperature it is more stable.
The solvent added must meet the following conditions, and boiling point is higher than 100 DEG C of organic solvent, and this solvent under normal pressure Cannot be with compound I, II and formic acid reaction, it is impossible to miscible with water.Because boiling point is less than 100 DEG C of solvent, though it can react Conversion ratio is obvious relatively low and makes yield low, different such as benzene, dichloromethane, chloroform, n-hexane, hexamethylene, petroleum ether, ethyl acetate The low boiling point solvents such as propyl ether, methyl tertiary butyl ether(MTBE), tetrahydrofuran, acetonitrile.
All alcohol, ketone, amine solvent can participate in reacting and being not suitable for making retarder thinner, such as methanol, ethanol, isopropanol, just Butanol, acetone, butanone, 2 pentanone, propione, cyclopentanone, cyclohexanone, triethylamine, isopropylamine equal solvent.
Solvent miscible with water is not suitable for making retarder thinner, due to need during the reaction by react generation water and The formic acid of non-immediate reaction is constantly distilled off.And solvent miscible with water water-scavenging capability difference and moisture of withing a hook at the end in distillation Effect, water content is big after recycling, is unfavorable for recycling, this kind of solvent such as dioxane, dimethyl sulfoxide (DMSO), N, N- dimethyl Formamide, n,N-dimethylacetamide, diglycol ethylene dimethyl ether etc..
Controlled in view of production cost, reaction dissolvent preferential recommendation uses common solvent such as toluene, dimethylbenzene, cycloheptyl Alkane, monochloro-benzene, methyl phenyl ethers anisole, but be not limited to cited.
By research, tested after adding reaction dissolvent, effect clearly, not only increases yield, while also have The quality of product is controlled to effect, the crude product purity of lomerizine hydrochloride reaches more than 99.8%.
One kind must be added to meet above-mentioned condition limit unlike the technical solution of existing report, in reaction system of the present invention The solvent of system, such as toluene, dimethylbenzene, cycloheptane, monochloro-benzene, methyl phenyl ethers anisole, after heating is changed into homogeneous system, then are warming up to 100 Formic acid could be added dropwise more than DEG C, and keep distillation state, make system steady temperature, time for adding control is dripped when 1-4 is small Bi Fanying 0.5-1 can stop reacting when small, added after concentration the stirring of anhydrous HCl/ ethanol solutions can crystallization obtain Crude product, step are as follows:
(1) by compound I and II in molar ratio 1:1~1:1.1 feed intake, along with compound I and II gross weight 0.10-10 Times solvent, such as toluene, dimethylbenzene, cycloheptane, monochloro-benzene, methyl phenyl ethers anisole, agitating and heating dissolve and continue to be heated to 100 DEG C~ Between 140 DEG C.
(2) it is 1 to press with compound I molar ratios:1~1:2 formic acid is added drop-wise in above-mentioned reaction system, and keeps distillation shape State, by moisture and the formic acid of non-immediate reaction, the azeotropic together with solvent steams, and time for adding is controlled when 1~4 is small.
(3) it is added dropwise, when continuing to keep azeotropic temperature reaction 0.5~1 small.
(4) it is evaporated under reduced pressure out retarder thinner
(5) absolute ethyl alcohol dissolution residual substance is added, filtering, adds anhydrous HCl/ ethanol solutions, control and mole of II Than for 1:2~1:3.
(6) 10~20 DEG C of crystallizations are cooled to crude product is obtained by filtration.
(7) carry out recrystallization with acetonitrile and turn crystalline substance.
The technique of the present invention compared with prior art, improves reaction yield and product quality, while reduce the three wastes Produce.Retarder thinner can be applied mechanically after distilling.And the acetonitrile mother liquor after absolute ethyl alcohol crystallization mother liquor and turn crystalline substance, it can recycle Recycle.A small amount of debris can burning disposal after distillation.
Embodiment:
Reference examples 1:
By 19.6g compounds I (0.1mol) and 28.8g compounds II (0.1mol), 105 DEG C are stirred and heated to, is kept back Stream mode, to melt homogeneous system, is added dropwise 88% formic acid 6.9g (0.132mol), drips off within two hours, reaction 1 is further continued for after dripping off Hour.Low boiling point component is evaporated off, adds absolute ethyl alcohol 100ml, filtering, adds 20% anhydrous HCl/ ethanol solutions 90ml, cold But to 10~20 DEG C, stirring and crystallizing, filtering, 70 DEG C of dryings, obtain product 41.0g, yield 75.8%, HPLC purity:98.19%.
By gained crude product add 160ml acetonitriles reflux 6 it is small when, cool down, filtering, 70 DEG C are dried to obtain crystal form I hydrochloric acid Lome Sharp piperazine 38.0g, turns brilliant yield 92.7%, HPLC purity:98.96%.
Reference examples 1 Impurity IV Impurity V Impurity IV Total purity
Crude product 0.27% 0.33% 0.16% 98.19%
Turn brilliant product 0.05% 0.31% 0.17% 98.96%
Reference examples 2:
By 9.8g compounds I (0.05mol) and 14.4g compounds II (0.05mol), dimethyl sulfoxide (DMSO) 24.2g is added, is stirred Mix and be heated to 115 DEG C, 88% formic acid 3.6g (0.069mol) is added dropwise, drips off within two hours, be further continued for after dripping off reaction 1 it is small when.It is high Vacuum distillation removes dimethyl sulfoxide, adds absolute ethyl alcohol 50ml, filtering, adds 20% anhydrous HCl/ ethanol solutions 45ml, cold But to 10~20 DEG C of stirring and crystallizings, filtering, 70 DEG C of dryings, obtain product 18.70g, yield 69.1%, HPLC purity:97.98%.
By gained crude product add 75ml acetonitriles reflux 6 it is small when, cool down, filtering, 70 DEG C are dried to obtain crystal form I hydrochloric acid Lome profit Piperazine 17.4g, turns brilliant yield 93.0%, HPLC purity:98.56%.
Reference examples 2 Impurity IV Impurity V Impurity IV Total purity
Crude product 0.33% 0.23% 0.11% 97.98%
Turn brilliant product 0.07% 0.20% 0.11% 98.56%
Reference examples 3
19.6g compounds I (0.1mol), 28.8g compounds II (0.1mol) are mixed, distilling apparatus is installed additional, is starting Heating first melts, and is further continued for being stirred and heated to 115 DEG C, serious curing phenomenon occurs for reaction system.88% formic acid is added dropwise again 6.9g (0.132mol), drips off for two hours, keep be added dropwise process temperature at 115 DEG C or so, be further continued for after dripping off reaction 1 it is small when. Low boiling point component is evaporated under reduced pressure out after reaction, Liquid Residue adds absolute ethyl alcohol 100ml, and filtering, adds 20% anhydrous HCl/ second Alcoholic solution 90ml, is cooled to 10~20 DEG C of stirring and crystallizings, and filtering, 70 DEG C of dryings, obtain product 44.9g, yield 83.0%, HPLC is pure Degree:98.11%.
By gained crude product add 200ml acetonitriles reflux 6 it is small when, cool down, filtering, 70 DEG C are dried to obtain crystal form I hydrochloric acid Lome Sharp piperazine 48.0g, turns brilliant yield 92.7%, HPLC purity:98.95%.
Reference examples 3 Impurity IV Impurity V Impurity IV Total purity
Crude product 0.22% 0.23% 0.16% 98.11%
Turn brilliant product 0.03% 0.22% 0.17% 98.95%
Embodiment 1:
19.6g compounds I (0.1mol), 28.8g compounds II (0.1mol) and 48.4g toluene are mixed, install distillation additional Device, is stirred and heated to 115 DEG C, and 88% formic acid 6.9g (0.132mol) is added dropwise, drips off within two hours, keeps dropwise addition process temperature to exist 115 DEG C or so, be further continued for after dripping off reaction 1 it is small when.Toluene is recovered under reduced pressure after reaction, Liquid Residue adds absolute ethyl alcohol 100ml, mistake Filter, adds 20% anhydrous HCl/ ethanol solutions 90ml, is cooled to 10~20 DEG C of stirring and crystallizings, filters, 70 DEG C of dryings, obtain product 51.83g, yield 95.8%, HPLC purity:99.86%.
By gained crude product add 200ml acetonitriles reflux 6 it is small when, cool down, filtering, 70 DEG C are dried to obtain crystal form I hydrochloric acid Lome Sharp piperazine 49.1g, turns brilliant yield 94.7%, HPLC purity:99.96%.
Embodiment 1 Impurity IV Impurity V Impurity IV Total purity
Crude product 0.07% 0.02% 0.01% 99.86%
Turn brilliant product 0 0.02% 0.01% 99.96%
Embodiment 2:
100g compounds I (0.51mol), 161g compounds II (0.56mol) and 2600g dimethylbenzene are mixed, installs additional and steams Distillation unit, is stirred and heated to 140 DEG C, and 88% formic acid 53.3g (1.02mol) is added dropwise, drips off within one hour, keeps that process temperature is added dropwise At 137-140 DEG C or so, be further continued for after dripping off reaction 1 it is small when.Dimethylbenzene is recovered under reduced pressure after reaction, Liquid Residue adds absolute ethyl alcohol 500ml, filtering, adds 20% anhydrous HCl/ ethanol solutions 186ml (1.02mol), is cooled to 10~20 DEG C of stirring and crystallizings, mistake Filter, 70 DEG C of dryings, obtain product 265g, yield 96.0%, HPLC purity:99.82%.
By gained crude product add 1000ml acetonitriles reflux 6 it is small when, cool down, filtering, 70 DEG C are dried to obtain crystal form I hydrochloric acid Lome Sharp piperazine 252g, turns brilliant yield 95.1%, HPLC purity:99.95%.
Embodiment 2 Impurity IV Impurity V Impurity IV Total purity
Crude product 0.03% 0.04% 0.01% 99.82%
Turn brilliant product 0 0.03% 0.01% 99.95%
Embodiment 3:
30.0kg compounds I (153mol), 45.4kg compounds II (157.6mol) and 15kg cycloheptane are mixed, installed additional Distilling apparatus, is stirred and heated to 100 DEG C, and 88% formic acid 8.0kg (153mol) is added dropwise, drips off within four hours, keeps dropwise addition process temperature Degree at 110 DEG C or so, be further continued for after dripping off reaction 0.5 it is small when.Cycloheptane is recycled after reaction, Liquid Residue adds absolute ethyl alcohol 120kg, filtering, adds 30% anhydrous HCl/ ethanol solutions 55.9kg, is cooled to 10~20 DEG C of stirring and crystallizings, filters, 70 DEG C It is dry, obtain product 78.4kg, yield 94.7%, HPLC purity:99.87%.
By gained crude product add 248kg acetonitriles reflux 6 it is small when, cool down, filtering, 70 DEG C are dried to obtain crystal form I hydrochloric acid Lome Sharp piperazine 75.1kg, turns brilliant yield 95.8%, HPLC purity:99.99%.
Embodiment 3 Impurity IV Impurity V Impurity IV Total purity
Crude product 0.03% 0.01% 0 99.87%
Turn brilliant product 0 0.01% 0 99.99%

Claims (5)

1. a kind of preparation method of lomerizine hydrochloride, reaction equation is as follows,
Explanation: C:\Documents and Settings\user\Application Data\Tencent\Users\1392798666\QQ\WinTemp\RichOle\[K7_5M]3H`XCRC4ZF7)XD_6.png
It is characterized in that, prepare according to the following steps:
(1) by compound I and II in molar ratio 1:1~1:1.1 feed intake, along with compound I and II gross weight 0.10-10 times of solvent, agitating and heating are dissolved and continued to be heated between 100 DEG C~140 DEG C;
The one kind of solvent described in this step in toluene, dimethylbenzene, cycloheptane;
(2) it is 1 to press with compound I molar ratios:1~1:2 formic acid is added drop-wise in above-mentioned reaction system, and keeps steaming State is evaporated, the azeotropic together with solvent steams by moisture and the formic acid of non-immediate reaction, and time for adding is controlled when 1~4 is small;
(3) it is added dropwise, when continuing to keep azeotropic temperature reaction 0.5~1 small;
(4) it is evaporated under reduced pressure out retarder thinner;
(5) absolute ethyl alcohol dissolution residual substance is added, filtering, adds anhydrous HCl/ethanol solution, control and the molar ratio of II For 1:2~1:3 ;
(6) 10~20 DEG C of crystallizations are cooled to crude product is obtained by filtration;
(7) carry out recrystallization with acetonitrile and turn crystalline substance.
2. preparation method described in claim 1, it is characterised in that in step (1), the molar ratio of compound I and II are 1: 1。
3. preparation method described in claim 1, it is characterised in that in step (1), the molar ratio of compound I and II are 1: 1.1。
4. preparation method described in claim 1, it is characterised in that in step (2), the molar ratio of compound I and formic acid is 1 :1.3.
5. preparation method described in claim 1, it is characterised in that in step (2), the molar ratio of compound I and formic acid is 1 :2.
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CN105175359A (en) * 2015-07-31 2015-12-23 四川省百草生物药业有限公司 Lomerizine Hydrochloride isomeride and preparation method therefor
CN114057667A (en) * 2021-12-22 2022-02-18 湖南增达生物科技有限公司 Preparation method of cinnarizine impurity and impurity

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1562988A (en) * 2004-03-17 2005-01-12 南京长澳医药科技有限公司 Method for synthesizing Lomerizine Hydrochlortde

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1562988A (en) * 2004-03-17 2005-01-12 南京长澳医药科技有限公司 Method for synthesizing Lomerizine Hydrochlortde

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
洛美利嗪的合成;王立升;《广西大学学报(自然科学版)》;20010630;第26卷(第2期);第105-107页 *
盐酸洛美利嗪的合成;彭东明,肖方青;《中国医药工业杂志》;20031231;第34卷(第7期);第317-318页 *
盐酸洛美利嗪的合成工艺改进;王华等;《中国药物化学杂志》;20031031;第13卷(第5期);第297-298页 *

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Patentee after: DISHA PHARMACEUTICAL GROUP Co.,Ltd.

Address before: 264205 Wendeng economic and Technological Development Zone, Weihai City, Shandong Province

Patentee before: Dijia Pharmaceutical Group Co.,Ltd.

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Effective date of registration: 20220407

Address after: 264205 268 Tianrun Road, Wendeng economic and Technological Development Zone, Weihai, Shandong

Patentee after: Dijia Pharmaceutical Group Co.,Ltd.

Address before: 264205 Wendeng economic and Technological Development Zone, Weihai City, Shandong Province

Patentee before: Dijia Pharmaceutical Group Co.,Ltd.

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Address after: No. 268, Tianrun Road, Wendeng Economic and Technological Development Zone, Weihai City, Shandong Province, 264200

Patentee after: Dijia Pharmaceutical Group Co.,Ltd.

Address before: 264205 268 Tianrun Road, Wendeng economic and Technological Development Zone, Weihai, Shandong

Patentee before: Dijia Pharmaceutical Group Co.,Ltd.

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