CN110606806B - 一种纳米钌催化合成伯胺的方法 - Google Patents

一种纳米钌催化合成伯胺的方法 Download PDF

Info

Publication number
CN110606806B
CN110606806B CN201910946310.5A CN201910946310A CN110606806B CN 110606806 B CN110606806 B CN 110606806B CN 201910946310 A CN201910946310 A CN 201910946310A CN 110606806 B CN110606806 B CN 110606806B
Authority
CN
China
Prior art keywords
primary amine
catalyst
nano ruthenium
synthesizing
catalysis
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201910946310.5A
Other languages
English (en)
Other versions
CN110606806A (zh
Inventor
蒋和雁
臧翠翠
高雪
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chongqing Technology and Business University
Original Assignee
Chongqing Technology and Business University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Chongqing Technology and Business University filed Critical Chongqing Technology and Business University
Priority to CN201910946310.5A priority Critical patent/CN110606806B/zh
Publication of CN110606806A publication Critical patent/CN110606806A/zh
Application granted granted Critical
Publication of CN110606806B publication Critical patent/CN110606806B/zh
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/46Ruthenium, rhodium, osmium or iridium
    • B01J23/462Ruthenium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/084Y-type faujasite
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0277Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature
    • B01J31/0278Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre
    • B01J31/0281Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre the nitrogen being a ring member
    • B01J31/0284Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre the nitrogen being a ring member of an aromatic ring, e.g. pyridinium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0277Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature
    • B01J31/0278Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre
    • B01J31/0285Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre also containing elements or functional groups covered by B01J31/0201 - B01J31/0274
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/26Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/19Catalysts containing parts with different compositions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/391Physical properties of the active metal ingredient
    • B01J35/393Metal or metal oxide crystallite size
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C209/00Preparation of compounds containing amino groups bound to a carbon skeleton
    • C07C209/24Preparation of compounds containing amino groups bound to a carbon skeleton by reductive alkylation of ammonia, amines or compounds having groups reducible to amino groups, with carbonyl compounds
    • C07C209/26Preparation of compounds containing amino groups bound to a carbon skeleton by reductive alkylation of ammonia, amines or compounds having groups reducible to amino groups, with carbonyl compounds by reduction with hydrogen
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C213/00Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton
    • C07C213/02Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton by reactions involving the formation of amino groups from compounds containing hydroxy groups or etherified or esterified hydroxy groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D307/00Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
    • C07D307/02Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
    • C07D307/34Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
    • C07D307/38Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with substituted hydrocarbon radicals attached to ring carbon atoms
    • C07D307/52Radicals substituted by nitrogen atoms not forming part of a nitro radical
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/584Recycling of catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

本发明公开了一种纳米钌催化合成伯胺的方法,包括将醛基化合物在PEG功能化离子液体稳定的纳米钌及HY沸石分子筛催化剂存在下与氨水、氢气一步反应生成伯胺,反应完成后通过温度控制实现催化剂与产物的高效分离。催化剂循环使用5次,催化活性和化学选择性都能得到较好的保持。本发明合成路线简单,合成方法新颖,工艺简便,产品收率和纯度高,催化剂廉价易得,不影响环境,适于工业化生产。

Description

一种纳米钌催化合成伯胺的方法
技术领域
本发明涉及一种纳米钌催化合成伯胺的方法。
背景技术
含氮化合物,特别是伯胺类化合物广泛用于合成聚合物,染料,表面活性剂,药物和农用化学品。利用氨作为氮源将醛或酮(尤其是天然产物中容易获取的醛或酮)直接胺化成伯胺是一种绿色环保的伯胺类化合物获取方法。
发明内容
本发明提供了一种纳米钌催化合成伯胺的方法,包括将醛基化合物在PEG功能化离子液体稳定的纳米钌及HY沸石分子筛催化剂存在下与氨水、氢气一步反应生成伯胺,反应完成后通过温度控制实现催化剂与产物的高效分离。催化剂循环使用多次,催化活性和化学选择性都能得到较好的保持。本发明合成路线简单, 合成方法新颖, 工艺简便, 产品收率和纯度高, 催化剂廉价易得, 不影响环境, 适于工业化生产。
所采用的技术方案是:一种纳米钌催化合成伯胺的方法,它包括如下内容:将醛基化合物在PEG功能化离子液体稳定的纳米钌及HY沸石分子筛催化剂存在下与氨水、氢气一步反应生成伯胺,反应完成后通过温度控制实现催化剂与产物的高效分离,回收的催化剂分离干燥后可循环使用。
上述的一种纳米钌催化合成伯胺的方法, 其特征是:它包括如下步骤:在无氧条件下,将醛基化合物在PEG功能化离子液体稳定的纳米钌及HY沸石分子筛催化剂存在下与氨水、氢气一步反应生成伯胺,反应完成后通过温度控制实现催化剂与产物的高效分离,回收的催化剂分离干燥后可循环使用。
上述的一种纳米钌催化合成伯胺的方法, 其特征是:醛基化合物与氨水、氢气一步反应生成伯胺的催化剂为PEG功能化离子液体稳定的纳米钌及HY沸石分子筛,PEG的分子量在200-20000之间,功能化离子液体阴离子为PF6,氨基酸阴离子,NTf2,OTf, BF4,AcO等。
上述的一种纳米钌催化合成伯胺的方法, 其特征是:所制备纳米钌催化剂的粒径在1-100nm之间,温控回收催化剂的温度控制在-50– +100oC 之间。
上述的一种纳米钌催化合成伯胺的方法, 其特征是:醛基化合物包括各种芳环有取代基团的醛基化合物,烷基侧链有取代基团的醛基化合物,醛基与芳环之间有取代基团的醛基化合物。
上述的一种纳米钌催化合成伯胺的方法, 其特征是:氨水的浓度为1%-34%之间,氢气压力为1-100atm之间。
本发明用于解决现有胺类化合物的合成方法路线长、收率低的问题。提出一种合成路线简单、合成方法新颖、工艺简便、收率高、原辅料价廉易得、环保、适用于工业生产的胺类化合物合成方法。
附图说明
图1是在[PEG-2000-BMIM][PF6]2制备的纳米钌的TEM图。
具体实施方式
下面结合实施例对本发明作进一步详细说明。
Figure RE-969267DEST_PATH_IMAGE001
本专利中所用到的部分PEG功能化离子液体结构。
本专利中在[PEG-2000-BMIM][PF6]2制备的纳米钌的TEM表明,Ru纳米颗粒粒径在1.5-3.0 nm之间(图1)。
本发明通过大量的实验、筛选、优化反应条件优选出下面合成路线:
实施例1
Figure RE-774674DEST_PATH_IMAGE002
在无氧条件下,向反应器中加入0.2mmol苯甲醛,0.0001mmol 0.3%纳米钌/[PEG-2000-BMIM][PF6]2,0.1g HY沸石分子筛,10equiv 氨水,充入1MPaH2,充分搅拌后升温至90oC反应5h,产物收率90.0%。分离出产物后催化剂进行干燥活化回收利用,第2-5次循环使用中目标产物收率分别为89.5%,92.3%,93.6%,91.5%。
实施例2
Figure RE-112115DEST_PATH_IMAGE003
在无氧条件下,向反应器中加入0.2mmol苯甲醛,0.0001mmol 0.3%纳米钌/[PEG-2000-BMIM][Pro]2,0.1g HY沸石分子筛,10equiv 氨水,充入1MPaH2,充分搅拌后升温至90oC反应5h, 产物收率93.6%。
实施例3
Figure RE-817903DEST_PATH_IMAGE004
在无氧条件下,向反应器中加入0.2mmol对甲氧基苯甲醛,0.0001mmol 0.3%纳米钌/[PEG-2000-BMIM][Pro]2,0.1g HY沸石分子筛,10equiv 氨水,充入1MPaH2,充分搅拌后升温至90oC反应5h, 产物收率83.5%。
实施例4
Figure RE-215386DEST_PATH_IMAGE005
在无氧条件下,向反应器中加入0.2mmol对氯苯甲醛,0.0001mmol 0.3%纳米钌/[PEG-2000-BMIM][Pro]2,0.1g HY沸石分子筛,10equiv 氨水,充入1MPaH2,充分搅拌后升温至90oC反应5h, 产物收率88.6%。
实施例5
Figure RE-508089DEST_PATH_IMAGE006
在无氧条件下,向反应器中加入0.2mmol间甲基苯甲醛,0.0001mmol 0.3%纳米钌/[PEG-2000-BMIM][Pro]2,0.1g HY沸石分子筛,10equiv 氨水,充入1MPaH2,充分搅拌后升温至90oC反应5h, 产物收率85.5%。
实施例6
Figure RE-649221DEST_PATH_IMAGE007
在无氧条件下,向反应器中加入0.2mmol呋喃甲醛,0.0001mmol 0.3%纳米钌/[PEG-2000-BMIM][Pro]2,0.1g HY沸石分子筛,10equiv 氨水,充入1MPaH2,充分搅拌后升温至90oC反应5h, 产物收率81.0%。
实施例7
Figure RE-147198DEST_PATH_IMAGE008
在无氧条件下,向反应器中加入0.2mmol苯乙酮,0.0001mmol 0.3%纳米钌/[PEG-2000-BMIM][Pro]2,0.1g HY沸石分子筛,10equiv 氨水,充入1MPaH2,充分搅拌后升温至100oC反应10h, 产物收率63.5%。
实施例8
Figure RE-981162DEST_PATH_IMAGE009
在无氧条件下,向反应器中加入0.2mmol2-醛基吡咯化合物,0.0001mmol 0.3%纳米钌/[PEG-2000-BMIM][Pro]2,0.1g HY沸石分子筛,10equiv 氨水,充入1MPaH2,充分搅拌后升温至100oC反应20h, 产物收率60.0%。

Claims (3)

1.一种纳米钌催化合成伯胺的方法,其特征在于,它包括如下步骤:在无氧条件下,将芳香醛基化合物在PEG功能化离子液体稳定的纳米钌及HY沸石分子筛催化剂存在下与氨水、氢气一步反应生成伯胺,反应完成后通过温度控制实现催化剂与产物的分离,回收的催化剂分离干燥后可循环使用,所述PEG功能化的离子液体为:
Figure FDA0003633118670000011
2.根据权利要求1所述的一种纳米钌催化合成伯胺的方法,其特征是:所制备纳米钌催化剂的粒径在1-100nm之间,温控回收催化剂的温度控制在-50–+100℃之间。
3.根据权利要求1所述的一种纳米钌催化合成伯胺的方法,其特征是:氨水的浓度为1%-34%之间,氢气压力为1-100atm之间。
CN201910946310.5A 2019-10-04 2019-10-04 一种纳米钌催化合成伯胺的方法 Active CN110606806B (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910946310.5A CN110606806B (zh) 2019-10-04 2019-10-04 一种纳米钌催化合成伯胺的方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910946310.5A CN110606806B (zh) 2019-10-04 2019-10-04 一种纳米钌催化合成伯胺的方法

Publications (2)

Publication Number Publication Date
CN110606806A CN110606806A (zh) 2019-12-24
CN110606806B true CN110606806B (zh) 2022-07-08

Family

ID=68894352

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910946310.5A Active CN110606806B (zh) 2019-10-04 2019-10-04 一种纳米钌催化合成伯胺的方法

Country Status (1)

Country Link
CN (1) CN110606806B (zh)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114621108B (zh) * 2020-12-08 2023-01-13 中国科学院大连化学物理研究所 一种乙醛酸制备甘氨酸的方法
CN114230469B (zh) * 2021-12-15 2023-03-21 中国科学院大连化学物理研究所 负载型纳米钌锆锡复合氧化物的合成及在苯甲醛胺化合成苄胺中应用
CN114380699B (zh) * 2022-01-26 2023-07-04 山东新和成维生素有限公司 一种合成异佛尔酮二胺的方法、催化剂及其制备方法
CN114409548B (zh) * 2022-03-01 2023-05-26 苏州大学张家港工业技术研究院 一种光催化制备苯甲胺类化合物的方法

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5990323A (en) * 1998-10-23 1999-11-23 Eastman Chemical Company Preparation of amines
US8383859B2 (en) * 2007-03-30 2013-02-26 Avinash N. Thadani Methods of preparing primary, secondary and tertiary carbinamine compounds in the presence of ammonia

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5990323A (en) * 1998-10-23 1999-11-23 Eastman Chemical Company Preparation of amines
US8383859B2 (en) * 2007-03-30 2013-02-26 Avinash N. Thadani Methods of preparing primary, secondary and tertiary carbinamine compounds in the presence of ammonia

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
Facile and efficient amination of organic halides catalyzed by copper sulfate in PEG1000-DIL/methylcyclohexane temperature-dependent biphasic system DIL/methylcyclohexane temperature-dependent biphasic system;Hu, Yu-Lin etal;《Journal of the Chinese Chemical Society (Taipei, Taiwan)》;20101231;604-611 *
聚乙二醇功能化离子液体的制备及其在有机反应中的 应用;徐艺凇 等;《化学进展》;20151015;1400 ~ 1412 *

Also Published As

Publication number Publication date
CN110606806A (zh) 2019-12-24

Similar Documents

Publication Publication Date Title
CN110606806B (zh) 一种纳米钌催化合成伯胺的方法
Kisszekelyi et al. Asymmetric synthesis with cinchona-decorated cyclodextrin in a continuous-flow membrane reactor
CN105777535B (zh) 用于制备葡糖二酸的方法
CN107056649A (zh) 一种负载席夫碱配合物的金属有机骨架材料的制备方法及其应用
CN1772379A (zh) 甲基异丁基醇气相催化脱氢铜系催化剂、制备方法及应用方法
CN102372666A (zh) 连续催化精馏合成α-甲基吡啶的方法
CN100357266C (zh) 一种生产氨基甲酸甲酯的工艺
CN101481355A (zh) 一种2-取代苯并咪唑的制备方法
CN114085136A (zh) 一种催化糠醛制备环戊酮的方法
CN104829559A (zh) 一种由乙酰丙酸甲酯制备γ-戊内酯的方法
CN105080603B (zh) 一种硝基苯选择性加氢制苯胺用催化剂及其制备方法、使用方法
CN110871064A (zh) 一种碳材料组合处理液及其制备方法、碳材料及其应用
CN109748817B (zh) 一种由脂肪醛合成脂肪腈的方法
CN110871063B (zh) 一种碳材料处理液及其制备方法、碳材料及其应用
CN112679322A (zh) 一种超临界co2催化制备2,6-二羟基甲苯的方法
CN114605226A (zh) 一种连续合成1,1,1,3-四氯丙烷的方法
CN107721804B (zh) 一种经3-硝基邻二甲苯制备邻二甲苯的方法
CN109851509A (zh) 一种4,4′-二氨基二苯甲烷的制备方法
CN106631829A (zh) 一种提高苯胺合成二苯胺转化率的方法
EP3689845A1 (en) Method for directly producing ethanol from syngas
CN111349008A (zh) 一种制备乙醛酸的方法
CN105597842A (zh) 乙苯催化剂的再生方法
CN111100098A (zh) 一种以co2催化果糖脱水生成5-hmf的方法
CN108484353B (zh) 一种2,4-二氯-5-氟(三氯甲基)苯的合成方法
CN109180444B (zh) 使用二氧化碳加速氢化芳香化合物合成环己酮的方法

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant