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CN117603068A - A kind of preparation method of tranexamic acid - Google Patents

A kind of preparation method of tranexamic acid Download PDF

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Publication number
CN117603068A
CN117603068A CN202311412480.8A CN202311412480A CN117603068A CN 117603068 A CN117603068 A CN 117603068A CN 202311412480 A CN202311412480 A CN 202311412480A CN 117603068 A CN117603068 A CN 117603068A
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acid
reaction
filtrate
tranexamic acid
hydrogenation
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韩加齐
蒋燕华
罗安贸
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CHANGZHOU YINSHENG PHARMACEUTICAL CO LTD
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C227/00Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • C07C227/04Formation of amino groups in compounds containing carboxyl groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C253/00Preparation of carboxylic acid nitriles
    • C07C253/30Preparation of carboxylic acid nitriles by reactions not involving the formation of cyano groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2601/00Systems containing only non-condensed rings
    • C07C2601/12Systems containing only non-condensed rings with a six-membered ring
    • C07C2601/14The ring being saturated

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  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention relates to a preparation method of tranexamic acid. The method comprises the following steps: adding p-cyanobenzoic acid into an autoclave, adding platinum black and a solvent, and then carrying out hydrogenation reaction under the conditions of 50-100 ℃ and 0.05-0.2 Mpa. Finishing the reaction, cooling and filtering; and (3) introducing a certain amount of liquid ammonia into the filtrate. Adding 5% Pd-C catalyst, and hydrogenation reaction at 100-150 deg.C and 2-4 MPa. Finishing the reaction, cooling and filtering; concentrating the filtrate under reduced pressure until solid is separated out, cooling to 0 ℃, filtering, washing with ethanol, and vacuum drying the solid to obtain tranexamic acid with the yield of more than 90%. The invention adopts the low-cost and easily-obtained p-cyanobenzoic acid as the raw material, and synthesizes the tranexamic acid by one step through 2 times of hydrogenation (benzene ring hydrogenation and cyano hydrogenation). Greatly reduces the production cost, improves the production environment, avoids the generation and discharge of toxic solid wastes, and greatly improves the quality of products.

Description

一种氨甲环酸的制备方法A kind of preparation method of tranexamic acid

技术领域Technical field

本发明属于药物与化工技术领域,涉及一种氨甲环酸(止血药)的制备方法。The invention belongs to the technical field of medicine and chemical industry and relates to a preparation method of tranexamic acid (hemostatic agent).

背景技术Background technique

氨甲环酸是效果良好的止血药,它是通过对结合于纤维蛋白溶酶原分子上赖氨酸的可逆性阻断,从而产生抗溶解纤维蛋白原的作用。它的止血机理与止血药氨基己酸相同,止血效果较氨基己酸强5-10倍,主要用于上消化道出血、渗血、外科手术出血及妇产科病出血等。此外,氨甲芳酸对治疗扁桃体发炎、肺结核咳血、痤疮、黄褐斑等有一定疗效。氨甲环酸虽然不是新药,但它到目前为此仍然属于全世界不可替代的最佳止血药。氨甲环酸的合成方法主要有两种,一种是丙烯酸甲酯法,由丙烯酸甲酯和氯代丁二烯经过一系列反应生成止血环酸;另一种是对氨甲基苯甲酸法,由对氨甲基苯甲酸经过催化氢化、转位生成氨甲环酸。由于在丙烯酸甲酯法中要使用剧毒的氰化物,因此工业上主要是使用对氨甲基苯甲酸法生产氨甲环酸。专利文献US 3932497记载了使用Ru催化剂,将Ru负载到惰性载体如氧化铝、硅藻土、活性炭、 硫酸钡、碳酸钙上,Ru在催化剂中的含量为1〜10 wt%。在温度150°C,氢气压力100 kg/cm2下反应,对氨甲基苯甲酸的转化率为100%,对氨甲基环己基甲酸的收率为97%。专利文献JP 49062444记载了使用Ru-C催化剂,将45g对氨甲基苯甲酸,16.7 gK0H,100 ml H20和25g5% Ru-C加入高压釜中,在温度90°C,氢气压力90 kg/cm2下反应,产物处理后得到43.5g对氨甲基环己基甲酸。专利文献JP 58032848记载了使用Rh催化剂,将Rh负载到活性炭上制得5%Rh-C催化剂,反应温度40℃,氢气压力30kg/cm2,反应3h,对氨甲基环己甲酸的收率达到90%。以上专利未报道将对氨甲基环已甲酸转位生成氨甲环酸的方法。专利文献CN201410079178.X、CN201110181414.5记载了用复合催化剂,将对氨甲基苯甲酸加氢,然后在碱土金属催化下转位,得到氨甲环酸。加氢转化率99.5%以上,收率未记载。Tranexamic acid is an effective hemostatic drug that reversibly blocks lysine bound to the plasminogen molecule, thereby producing an anti-fibrinogen dissolving effect. Its hemostatic mechanism is the same as the hemostatic drug aminocaproic acid, and its hemostatic effect is 5-10 times stronger than that of aminocaproic acid. It is mainly used for upper gastrointestinal bleeding, bleeding, surgical bleeding, and obstetric and gynecological bleeding. In addition, aminocarbic acid has certain effects on treating tonsil inflammation, tuberculosis and hemoptysis, acne, chloasma, etc. Although tranexamic acid is not a new drug, it is still the best and irreplaceable hemostatic drug in the world. There are two main methods for synthesizing tranexamic acid. One is the methyl acrylate method, which generates hemostatic acid through a series of reactions between methyl acrylate and chlorobutadiene; the other is the p-aminomethylbenzoic acid method. , tranexamic acid is generated from p-aminomethylbenzoic acid through catalytic hydrogenation and translocation. Since highly toxic cyanide is used in the methyl acrylate method, the p-aminomethylbenzoic acid method is mainly used in industry to produce tranexamic acid. Patent document US 3932497 describes the use of a Ru catalyst, loading Ru onto an inert carrier such as alumina, diatomaceous earth, activated carbon, barium sulfate, and calcium carbonate. The content of Ru in the catalyst is 1 to 10 wt%. When reacting at a temperature of 150°C and a hydrogen pressure of 100 kg/cm2, the conversion rate of p-aminomethylbenzoic acid is 100%, and the yield of p-aminomethylcyclohexylcarboxylic acid is 97%. Patent document JP 49062444 describes the use of Ru-C catalyst, adding 45g of p-aminomethylbenzoic acid, 16.7 gKOH, 100 ml H20 and 25g5% Ru-C into an autoclave at a temperature of 90°C and a hydrogen pressure of 90 kg/cm2 After reaction, 43.5g of p-aminomethylcyclohexylcarboxylic acid was obtained after product treatment. Patent document JP 58032848 describes the use of Rh catalyst, loading Rh on activated carbon to prepare a 5% Rh-C catalyst, the reaction temperature is 40°C, the hydrogen pressure is 30kg/cm2, the reaction is 3 hours, and the yield of aminomethylcyclohexanecarboxylic acid reaches 90%. The above patents do not report the method of transposition of aminomethylcyclohexanecarboxylic acid to generate tranexamic acid. Patent documents CN201410079178. The hydrogenation conversion rate is over 99.5%, and the yield is not recorded.

目前工业化生产多是采用以氨甲芳酸为原料,在硫酸水溶液中,在铂黑催化下低压加氢,得到顺反式对氨甲基环已酸。利用氢氧化钡除酸,然后以氢氧化钡为催化剂,在反应温度180-220℃、反应压力1-2.5Mpa下反应二十几个小时进行转位反应,经冷却、酸化得到氨甲环酸,收率80%左右。该工艺使用昂贵的铂作为催化剂,使生产成本大大增加;使用氢氧化钡作为中和剂和转位催化剂,产生的硫酸钡和碳酸钡具有很高的毒性,给环境带来很严重的危害。At present, industrial production mostly uses aminomethylaromatic acid as raw material, and uses low-pressure hydrogenation in sulfuric acid aqueous solution under the catalysis of platinum black to obtain cis-trans p-aminomethylcyclohexanoic acid. Use barium hydroxide to remove acid, and then use barium hydroxide as a catalyst to react for more than 20 hours at a reaction temperature of 180-220°C and a reaction pressure of 1-2.5Mpa to perform a translocation reaction. After cooling and acidification, tranexamic acid is obtained. , the yield is about 80%. This process uses expensive platinum as a catalyst, which greatly increases the production cost; it uses barium hydroxide as a neutralizer and translocation catalyst, and the barium sulfate and barium carbonate produced are highly toxic and cause serious harm to the environment.

发明内容Contents of the invention

本发明针对现有生产工艺存在的问题,提供了提出了一种氨甲环酸的制备方法,其包括如下步骤:In view of the problems existing in the existing production technology, the present invention provides a preparation method of tranexamic acid, which includes the following steps:

(1)将对氰基苯甲酸加到高压釜中,加入铂黑和溶剂,然后在50-100℃,0.05-0.2Mpa下加氢反应。结束反应,冷却后过滤,得到第一滤液;(1) Add p-cyanobenzoic acid to the autoclave, add platinum black and solvent, and then hydrogenate at 50-100°C, 0.05-0.2Mpa. End the reaction, cool and then filter to obtain the first filtrate;

(2)向第一滤液中通入一定量的液氨。加入5%钯碳催化剂,然后在100-150℃,2-4Mpa下加氢反应。结束反应,冷却后过滤,得到第二滤液;(2) Pour a certain amount of liquid ammonia into the first filtrate. Add 5% palladium carbon catalyst, and then hydrogenate at 100-150°C and 2-4Mpa. End the reaction, cool and then filter to obtain the second filtrate;

(3)将第二滤液减压浓缩至有固体析出,加入相对于所述第二滤液5倍重量的乙醇,冷却到0℃,过滤,用乙醇洗涤,固体真空干燥,得到氨甲环酸,收率90%以上。(3) Concentrate the second filtrate under reduced pressure until solid precipitates, add 5 times the weight of ethanol relative to the second filtrate, cool to 0°C, filter, wash with ethanol, and dry the solid in vacuum to obtain tranexamic acid, The yield is over 90%.

上述反应投料重量比优选为:对氰基苯甲酸:铂黑:液氨:5%钯碳催化剂:溶剂 =1:0.001:0.1:0.05:3;The weight ratio of the above reaction materials is preferably: p-cyanobenzoic acid: platinum black: liquid ammonia: 5% palladium carbon catalyst: solvent =1:0.001:0.1:0.05:3;

上述的溶剂为甲醇或乙醇;The above solvent is methanol or ethanol;

本发明的有益效果:采用廉价易得的对氰基苯甲酸为原料,通过2次加氢(苯环加氢和氰基加氢)一步合成氨甲环酸,收率90%以上。大大降低了生产成本,改善了生产环境,避免了有毒固废的产生和排放,大大提高了产品的质量。Beneficial effects of the present invention: using cheap and easily available p-cyanobenzoic acid as raw material, tranexamic acid is synthesized in one step through two hydrogenations (benzene ring hydrogenation and cyano group hydrogenation), with a yield of more than 90%. It greatly reduces production costs, improves the production environment, avoids the generation and discharge of toxic solid waste, and greatly improves product quality.

实施方式Implementation

以下实施例用来进一步说明本发明的内容,并不限制本发明的应用。实施例中的百分数一律是质量分数。The following examples are used to further illustrate the content of the present invention and do not limit the application of the present invention. The percentages in the examples are always mass fractions.

实施例1Example 1

一种氨甲环酸的制备方法,其包括如下步骤:A preparation method of tranexamic acid, which includes the following steps:

(1)将147g对氰基苯甲酸加到1000ml高压釜中,加入0.15g铂黑和441g甲醇,在100℃,0.05Mpa下加氢,HPLC跟踪,反应结束后,冷却,过滤,得到第一滤液,分出的催化剂可以直接套用;(1) Add 147g of p-cyanobenzoic acid to a 1000ml autoclave, add 0.15g of platinum black and 441g of methanol, hydrogenate at 100°C, 0.05Mpa, and track with HPLC. After the reaction is completed, cool and filter to obtain the first The filtrate and separated catalyst can be used directly;

(2)向第一滤液中通入14.7g液氨。加入7.35g的5%钯碳催化剂,然后在100℃,4Mpa下进行加氢反应。HPLC跟踪,反应结束后,冷却,过滤,得到第二滤液,分出的催化剂可以直接套用;(2) Pour 14.7g of liquid ammonia into the first filtrate. Add 7.35g of 5% palladium on carbon catalyst, and then perform hydrogenation reaction at 100°C and 4Mpa. HPLC tracking, after the reaction is completed, cool and filter to obtain the second filtrate, and the separated catalyst can be used directly;

(3)将第二滤液减压浓缩至有固体析出,加入5倍量的乙醇(重量比),冷却到0℃,过滤,用乙醇洗涤,固体真空干燥,得到142g氨甲环酸。(3) Concentrate the second filtrate under reduced pressure until solid precipitates, add 5 times the amount of ethanol (weight ratio), cool to 0°C, filter, wash with ethanol, and dry the solid in vacuum to obtain 142g of tranexamic acid.

实施例2Example 2

一种氨甲环酸的制备方法,其包括如下步骤:A preparation method of tranexamic acid, which includes the following steps:

(1)将147g对氰基苯甲酸加到1000ml高压釜中,加入0.15g铂黑和441g甲醇,在50℃,0.2Mpa下加氢,HPLC跟踪,反应结束后,冷却,过滤,得到第一滤液,分出的催化剂可以直接套用;(1) Add 147g of p-cyanobenzoic acid to a 1000ml autoclave, add 0.15g of platinum black and 441g of methanol, hydrogenate at 50°C, 0.2Mpa, and track with HPLC. After the reaction is completed, cool and filter to obtain the first The filtrate and separated catalyst can be used directly;

(2)向第一滤液中通入14.7g液氨。加入7.35g的5%钯碳催化剂,然后在150℃,2Mpa下进行加氢反应。HPLC跟踪,反应结束后,冷却,过滤,得到第二滤液,分出的催化剂可以直接套用;(2) Pour 14.7g of liquid ammonia into the first filtrate. Add 7.35g of 5% palladium on carbon catalyst, and then perform hydrogenation reaction at 150°C and 2Mpa. HPLC tracking, after the reaction is completed, cool and filter to obtain the second filtrate, and the separated catalyst can be used directly;

(3)将第二滤液减压浓缩至有固体析出,加入5倍量的乙醇(重量比),冷却到0℃,过滤,用乙醇洗涤,固体真空干燥,得到144g氨甲环酸。(3) Concentrate the second filtrate under reduced pressure until solid precipitates, add 5 times the amount of ethanol (weight ratio), cool to 0°C, filter, wash with ethanol, and dry the solid in vacuum to obtain 144g of tranexamic acid.

实施例3Example 3

一种氨甲环酸的制备方法,其包括如下步骤:A preparation method of tranexamic acid, which includes the following steps:

(1)将147g对氰基苯甲酸加到1000ml高压釜中,加入0.15g铂黑和441g甲醇,在75℃,0.13Mpa下加氢,HPLC跟踪,反应结束后,冷却,过滤,得到第一滤液,分出的催化剂可以直接套用;(1) Add 147g of p-cyanobenzoic acid to a 1000ml autoclave, add 0.15g of platinum black and 441g of methanol, hydrogenate at 75°C, 0.13Mpa, and track with HPLC. After the reaction is completed, cool and filter to obtain the first The filtrate and separated catalyst can be used directly;

(2)向第一滤液中通入14.7g液氨。加入7.35的g5%钯碳催化剂,然后在125℃,3Mpa下进行加氢反应。HPLC跟踪,反应结束后,冷却,过滤,得到第二滤液,分出的催化剂可以直接套用;(2) Pour 14.7g of liquid ammonia into the first filtrate. Add 7.35 g of 5% palladium carbon catalyst, and then perform hydrogenation reaction at 125°C and 3Mpa. HPLC tracking, after the reaction is completed, cool and filter to obtain the second filtrate, and the separated catalyst can be used directly;

(3)将第二滤液减压浓缩至有固体析出,加入5倍量的乙醇(重量比),冷却到0℃,过滤,用乙醇洗涤,固体真空干燥,得到143g氨甲环酸。(3) Concentrate the second filtrate under reduced pressure until solid precipitates, add 5 times the amount of ethanol (weight ratio), cool to 0°C, filter, wash with ethanol, and dry the solid in vacuum to obtain 143g of tranexamic acid.

上述实施例只为说明本发明的技术构思及特点,其目的在于让熟悉该项技术的人员能够了解本发明的内容,并不能以此限制本发明的保护范围。凡根据本发明精神中实质所做的等效变化和修饰,都应涵盖在本发明的保护范围之内。The above embodiments are only for illustrating the technical concepts and features of the present invention. Their purpose is to enable those familiar with the technology to understand the content of the present invention, and they are not intended to limit the scope of protection of the present invention. All equivalent changes and modifications made based on the essence of the spirit of the present invention should be included in the protection scope of the present invention.

Claims (3)

1. The preparation method of tranexamic acid is characterized by comprising the following steps:
(1) Adding p-cyanobenzoic acid into an autoclave, adding platinum black and a solvent, and then carrying out hydrogenation reaction under the conditions of 50-100 ℃ and 0.05-0.2 Mpa; after finishing the reaction, cooling and filtering to obtain a first filtrate;
(2) Introducing liquid ammonia into the first filtrate, adding 5% palladium-carbon catalyst, and then carrying out hydrogenation reaction at 100-150 ℃ and 2-4 Mpa; after finishing the reaction, cooling and filtering to obtain a second filtrate;
(3) Concentrating the second filtrate under reduced pressure until solid is separated out, adding ethanol which is 5 times of the weight of the second filtrate, cooling to 0 ℃, filtering, washing with ethanol, and drying the solid in vacuum to obtain tranexamic acid.
2. The preparation method according to claim 1, wherein the p-cyanobenzoic acid is as follows: platinum black: liquid ammonia: 5% palladium carbon catalyst: solvent = 1:0.001:0.1:0.05:3.
3. the process according to claim 1 or 2, wherein the solvent is methanol or ethanol.
CN202311412480.8A 2023-08-01 2023-10-30 A kind of preparation method of tranexamic acid Withdrawn CN117603068A (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH593238A5 (en) * 1974-05-10 1977-11-30 Asahi Chemical Ind 4-Aminomethyl cyclohexane carboxylic acid-1 prepn - in one step by hydrogenating lower alkyl para-cyanobenzoate using nickel catalyst in aq medium contg ammonia
CN101445475A (en) * 2008-12-30 2009-06-03 浙江工业大学 Method for preparing (trans)-4-cyclohexyl-L-proline
CN102665718A (en) * 2009-10-06 2012-09-12 米伦纽姆医药公司 Heterocyclic compounds useful as pdk1 inhibitors
CN108752226A (en) * 2018-05-15 2018-11-06 常州兰陵制药有限公司 The preparation method of tranexamic acid

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH593238A5 (en) * 1974-05-10 1977-11-30 Asahi Chemical Ind 4-Aminomethyl cyclohexane carboxylic acid-1 prepn - in one step by hydrogenating lower alkyl para-cyanobenzoate using nickel catalyst in aq medium contg ammonia
CN101445475A (en) * 2008-12-30 2009-06-03 浙江工业大学 Method for preparing (trans)-4-cyclohexyl-L-proline
CN102665718A (en) * 2009-10-06 2012-09-12 米伦纽姆医药公司 Heterocyclic compounds useful as pdk1 inhibitors
CN108752226A (en) * 2018-05-15 2018-11-06 常州兰陵制药有限公司 The preparation method of tranexamic acid

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