CN104437332B - A stirring reation kettle for cutting fluid - Google Patents
A stirring reation kettle for cutting fluid Download PDFInfo
- Publication number
- CN104437332B CN104437332B CN201410757270.7A CN201410757270A CN104437332B CN 104437332 B CN104437332 B CN 104437332B CN 201410757270 A CN201410757270 A CN 201410757270A CN 104437332 B CN104437332 B CN 104437332B
- Authority
- CN
- China
- Prior art keywords
- drainage
- drainage tube
- kettle body
- cylinder
- tube
- 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
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
- B01J19/20—Stationary reactors having moving elements inside in the form of helices, e.g. screw reactors
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Accessories For Mixers (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种化工机械设备,具体涉及一种用于切削液的搅拌反应釜。The invention relates to chemical machinery equipment, in particular to a stirring reaction kettle for cutting fluid.
背景技术Background technique
切削液生产过程中使用的反应设备一般有两类,搅拌反应釜和管式反应器,其中搅拌反应釜应用最为广泛。其中搅拌反应釜的特点是相接触面积大,传质、传热效率高,温度声、操作灵活性大(可进行间隙操作、半间歇操作、连续操作),便于控制和改变反应条件。There are generally two types of reaction equipment used in the production of cutting fluids, stirred reactors and tubular reactors, among which stirred reactors are the most widely used. Among them, the stirred reactor is characterized by large phase contact area, high mass transfer and heat transfer efficiency, low temperature, high operational flexibility (interval operation, semi-batch operation, continuous operation), and easy control and change of reaction conditions.
搅拌反应釜中搅拌所起的作用相当关键。搅拌作用有:两种或两种以上互溶液体混合均匀;形成乳浊液或悬浮液。搅拌器型式的不同对搅拌效果影响很大。反应釜放大的核心之一就是搅拌器的放大。Stirring in a stirred reactor plays a critical role. Stirring action: mix two or more miscible liquids evenly; form emulsion or suspension. The difference in the type of agitator has a great influence on the stirring effect. One of the cores of reactor scale-up is the scale-up of the stirrer.
然而现有的搅拌器多是在一个平流层上的搅拌 ,如中国专利CN203648523所公开的加热搅拌反应釜,包括罐体、加热器和搅拌器,罐体的罐壁设有中空夹层,搅拌器包括搅拌叶,搅拌叶水平位于罐体内,罐壁内层向内设有凸起,加热器设于凸起处的罐壁夹层内,搅拌叶与凸起处位于同一平面。However, most of the existing stirrers are stirred on a stratosphere, such as the heating and stirring reactor disclosed in Chinese patent CN203648523, comprising a tank, a heater and a stirrer, the tank wall of the tank is provided with a hollow interlayer, and the stirrer The mixing blade is included, the stirring blade is horizontally located in the tank, the inner layer of the tank wall is provided with a protrusion inwardly, the heater is arranged in the interlayer of the tank wall at the protrusion, and the stirring blade and the protrusion are located on the same plane.
中国专利CN203648523中所设置的搅拌器主要作用于个别水平面,搅拌的效果主要集中在平流层内的液体混合,搅拌器对于整个反应釜的高度方向的液体搅拌能力弱,不利于反应物的均匀混合。The agitator set in the Chinese patent CN203648523 mainly acts on individual horizontal surfaces, and the stirring effect is mainly concentrated on the liquid mixing in the stratosphere. The agitator has a weak ability to stir the liquid in the height direction of the entire reactor, which is not conducive to the uniform mixing of reactants .
发明内容Contents of the invention
本发明所要解决的技术问题是提供一种通过液体在高度方向的流动促使反应物均匀混合的的搅拌反应釜。The technical problem to be solved by the present invention is to provide a stirred reactor in which reactants are uniformly mixed through the flow of liquid in the height direction.
为解决上述技术问题,本发明提供如下技术方案:In order to solve the above technical problems, the present invention provides the following technical solutions:
用于切削液的搅拌反应釜,包括釜体、进料管、设于釜体内的搅拌桨,该搅拌桨与电机的输出轴连接,还包括一个引流筒,该引流筒的上筒口连接在上盖下方的釜体内壁上,搅拌桨设于所述引流筒内;所述引流筒的筒底设有引流孔,所述搅拌桨包括螺旋风叶以及与电机输出轴固接的连接轴,所述螺旋风叶固定在连接轴上,高度位置处于螺旋风叶上方的引流筒筒壁上设有引流孔。A stirring reaction kettle for cutting fluid, including a kettle body, a feed pipe, a stirring paddle arranged in the kettle body, the stirring paddle is connected with the output shaft of the motor, and a drainage tube, the upper cylinder port of the drainage tube is connected to the upper On the inner wall of the kettle below the cover, the stirring paddle is arranged in the drainage tube; the bottom of the drainage tube is provided with a drainage hole, and the stirring paddle includes a spiral fan blade and a connecting shaft fixedly connected with the output shaft of the motor. The spiral fan blades are fixed on the connecting shaft, and drainage holes are arranged on the wall of the drainage tube whose height position is above the spiral fan blades.
采用本发明用于切削液的搅拌反应釜,具有如下效果:Adopting the stirring reaction kettle for cutting fluid of the present invention has the following effects:
1、在螺旋风叶上方的引流筒筒壁上设有引流孔,这样由进料管进入到引流筒内液体会先先螺旋风叶、引流筒底部的引流孔落入釜体底部,待液位上升到所述螺旋风叶上方的引流筒筒壁上时,所述螺旋风叶的转动具有向下方“排水“的效果,使液体受到螺旋风叶作用向下急流,同时位于螺旋风叶上方的引流筒筒壁处的液体会从引流孔处流入到引流筒内来补充引流筒内的液位,进而会有一部分底层的液体上涌,从而以引流向筒为中心形成一个水液循环。不仅有平流流动还会有上下涌动。1. There is a drainage hole on the wall of the drainage tube above the spiral fan blade, so that the liquid entering the drainage tube from the feed pipe will first fall into the bottom of the kettle body through the drainage hole at the bottom of the spiral fan blade and the drainage tube. When the position rises to the wall of the drainage tube above the spiral fan blade, the rotation of the spiral fan blade has the effect of "drainage" downward, making the liquid flow downward under the action of the spiral fan blade, and at the same time it is located above the spiral fan blade The liquid at the wall of the drainage tube will flow into the drainage tube from the drainage hole to supplement the liquid level in the drainage tube, and then a part of the bottom liquid will rise up, thus forming a water circulation centered on the drainage tube. There is not only advective flow but also up and down surge.
2、本发明用于切削液的搅拌反应釜在引流筒底与螺旋风叶上均设有引流孔,唯独在螺旋风吓所同一高度位置的引流筒处不设置引流孔,目的就是为了避免螺旋风叶将搅拌动力转移动水流的水平流动中。2. The agitated reaction kettle for cutting fluid of the present invention is provided with drainage holes at the bottom of the drainage tube and on the spiral fan blades, but no drainage holes are provided at the drainage tube at the same height as the spiral fan, the purpose is to avoid The spiral fan transfers the stirring power to the horizontal flow of the moving water.
3、本发明用于切削液的搅拌反应釜通过液体在高度方向的涌动,促使反应物均匀混合,同时也存在平流流动,比现有技术的混合液要更为均匀。3. The stirred reactor for cutting fluid of the present invention promotes uniform mixing of the reactants through the surge of the liquid in the height direction, and at the same time there is advection flow, which is more uniform than the mixed solution of the prior art.
进一步,所述进料管从釜体侧壁穿入到釜体内;进料管管口入到引流筒内;所述釜体上设有辅料的对接接口,该对接接口通过导流管通入到所述引流筒内。Further, the feed pipe penetrates into the kettle body from the side wall of the kettle body; the mouth of the feed pipe enters the drainage tube; the kettle body is provided with a docking interface for auxiliary materials, and the docking interface is passed through the guide tube into the drainage tube.
采用导流管与进料管分别添加主料与辅料,同时两者均先通入到引流筒内,避免加热过程中加入的辅料,未及搅拌打散就与局部主料完全反应。Use the diversion tube and feeding tube to add the main material and the auxiliary material respectively, and at the same time, both of them are passed into the drainage tube first, so as to avoid the auxiliary material added during the heating process, which will completely react with the local main material before stirring and breaking up.
进一步,还包括设于引流筒内的引流管,所述连接轴设于引流管内,且在所述连接轴上设有绞龙叶片,所述引流管上下均开口,其中上开口固定固定在釜体内壁上,所述导流管穿入到引流管内,且导流管管口处于所述绞龙叶片上方。Further, it also includes a drainage tube arranged in the drainage tube, the connecting shaft is arranged in the drainage tube, and an auger blade is arranged on the connecting shaft, the upper and lower openings of the drainage tube are fixed, and the upper opening is fixed on the kettle. On the inner body wall, the guide tube penetrates into the drainage tube, and the nozzle of the guide tube is above the blade of the auger.
通过引流管,使辅料的导入与主料的导入相对独立,即便在导流筒内,两者基本不接触,只有在落入釜体底部时,两者才能算是充分混合(避免刚导入时,两者提前集中反应)。Through the drainage tube, the introduction of auxiliary materials and the introduction of main materials are relatively independent. Even in the guide tube, the two basically do not touch. Both concentrated in advance).
进一步,在高度位置处于所述进料管管口上方的引流管侧壁上设有小型引流孔。Further, a small drainage hole is provided on the side wall of the drainage tube at a height position above the mouth of the feeding tube.
落入釜体底部的混合液待液面上升后,能通过小型引流孔回到引流管内,所述引流管的内空间不构成水流循环的障碍。小型引流孔的高度位置处于所述进料管管口上方,也是为了避免刚开始带着初速度导入到引流筒内的主料直接进入引流管内。After the liquid level rises, the mixed liquid falling into the bottom of the kettle body can return to the drainage pipe through the small drainage hole, and the inner space of the drainage pipe does not constitute an obstacle to the water circulation. The height position of the small drainage hole is above the mouth of the feed tube, also to avoid the main material that is initially introduced into the drainage tube with initial velocity directly into the drainage tube.
附图说明Description of drawings
图1为本发明用于切削液的搅拌反应釜实施例中实施例一的结构示意图。Fig. 1 is a schematic structural view of Embodiment 1 of the embodiments of the stirred reactor for cutting fluid in the present invention.
图2为本发明用于切削液的搅拌反应釜实施例中实施例二的局部结构示意图。Fig. 2 is a partial structural schematic diagram of Embodiment 2 of the embodiment of the stirred reactor for cutting fluid in the present invention.
具体实施方式Detailed ways
下面通过具体实施方式对本发明作进一步详细的说明:The present invention will be described in further detail below by means of specific embodiments:
说明书附图中的附图标记包括:釜体10、阀门11、进料管20、引流筒31、引流孔33、引流管40、小型引流孔41、对接接口50、导流管51、上盖60、电机61、连接轴62、搅拌桨63、绞龙叶片64。The reference signs in the drawings of the description include:
实施例一Embodiment one
如图1所示,本发明用于切削液的搅拌反应釜,包括反应釜釜体10以及设于反应釜釜体10上的上盖60以及设于上盖60上的电机61,所述电机61其输出轴穿过上盖60并介入到釜体10内。As shown in Fig. 1, the stirring reactor for cutting fluid of the present invention includes a
本发明用于切削液的搅拌反应釜,包括设于釜体10内的搅拌桨63,该搅拌桨63与电机61的输出轴连接,还包括一个引流筒31,该引流筒31的上筒口连接在上盖60下方的釜体10内壁上,搅拌桨63设于所述引流筒31内。The stirring reaction kettle for cutting fluid of the present invention includes a
所述引流筒31在满足强度、刚度要求的前提下,尽量选用轻质材料,以达到减轻质量的目的,本实施例中采用厚铝板卷焊而成。Under the premise of meeting the strength and rigidity requirements, the
所述搅拌桨63设于引流筒31内,所述引流筒31的筒底设有引流孔33,所述搅拌桨63包括螺旋风叶以及与电机61输出轴固接的连接轴62,所述螺旋风叶固定在连接轴62上,高度位置处于螺旋风叶上方的引流筒31筒壁上设有引流孔33。The stirring
引流孔33的大小应根据引流筒31的截面直径来设计,如引流筒31截面为直径12cm的圆形,那引流孔33应设为直径为1~2cm的圆孔。The size of the
本发明用于切削液的搅拌反应釜的进料管20从釜体10侧壁穿入到釜体10内,搅拌桨63上方的引流筒31筒壁上还设有一个进料口,所述进料管20管口与该进料口对接。所述釜体10上设有辅料对接接口50,该对接接口50通过导流管51通入到所述引流筒31内。The
所述釜体10下部设有阀门11,用于将反应完全的成品引出釜体10。The lower part of the
实施例二Embodiment two
如图2所示,本实施例与实施例一的区别在于,本实施例还包括设于引流筒31内的引流管40,所述连接轴62设于引流管40内,且在所述连接轴62上设有绞龙叶片64,所述引流管40上下均开口,其中上开口固定固定在釜体10内壁上,所述导流管51穿入到引流管40内,且导流管51管口处于所述绞龙叶片64上方,在高度位置处于所述进料管20管口上方的引流管40侧壁上设有小型引流孔41,此处的小型引流孔41是引流管40直径的十二分之一至十分之一之间。As shown in Figure 2, the difference between this embodiment and Embodiment 1 is that this embodiment also includes a
如图1、2所示,进料管管口正对的引流筒31侧壁上不设置有引流孔33,避免带有初速度的原料直接从侧壁上的引流孔33直接流到引流筒31外。As shown in Figures 1 and 2, there is no
以上所述的仅是本发明的实施例,方案中公知的具体结构及特性等常识在此未作过多描述。应当指出,对于本领域的技术人员来说,在不脱离本发明结构的前提下,还可以作出若干变形和改进,如两实施例中的引流筒31与引流管40表面涂防热涂层。这些也应该视为本发明的保护范围,这些都不会影响本发明实施的效果和专利的实用性。本申请要求的保护范围应当以其权利要求的内容为准,说明书中的具体实施方式等记载可以用于解释权利要求的内容。What is described above is only an embodiment of the present invention, and common knowledge such as specific structures and characteristics known in the scheme are not described here too much. It should be pointed out that those skilled in the art can make some modifications and improvements without departing from the structure of the present invention, such as coating the surface of the
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410757270.7A CN104437332B (en) | 2014-12-11 | 2014-12-11 | A stirring reation kettle for cutting fluid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410757270.7A CN104437332B (en) | 2014-12-11 | 2014-12-11 | A stirring reation kettle for cutting fluid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104437332A CN104437332A (en) | 2015-03-25 |
| CN104437332B true CN104437332B (en) | 2023-04-07 |
Family
ID=52884542
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410757270.7A Active CN104437332B (en) | 2014-12-11 | 2014-12-11 | A stirring reation kettle for cutting fluid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104437332B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR3090410B1 (en) * | 2018-12-19 | 2020-12-25 | Ifp Energies Now | Tubular screw conveyor reactor |
| CN111054291B (en) * | 2019-12-24 | 2023-09-01 | 南方锰业集团有限责任公司 | Reaction kettle of spiral net cover type stirrer |
Citations (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1404163A (en) * | 1972-09-29 | 1975-08-28 | Mitsui Toatsu Chemicals | Polymerization reactor |
| CN86202953U (en) * | 1986-05-08 | 1987-07-15 | 苏州造漆厂 | Circulating stirring device |
| CN1117892A (en) * | 1994-04-18 | 1996-03-06 | 普拉塞尔技术有限公司 | Variable liquid level eductor/impeller gas-liquid mixing apparatus and process |
| CN1159437A (en) * | 1995-12-28 | 1997-09-17 | 普拉塞尔技术有限公司 | High-effect heat transfer and mass transfer for gas phase heterogeneous reaction |
| CN2559406Y (en) * | 2002-07-19 | 2003-07-09 | 南风化工集团股份有限公司 | Mixer with propeller |
| CN101054473A (en) * | 2006-04-10 | 2007-10-17 | 浙江龙盛集团股份有限公司 | Coupling production equipment and production process |
| CN201454534U (en) * | 2009-04-10 | 2010-05-12 | 天津大学 | Multiple Conduit Loop Reactor |
| CN201701758U (en) * | 2010-06-13 | 2011-01-12 | 丽珠集团福州福兴医药有限公司 | Evaporator |
| CN102839384A (en) * | 2011-06-21 | 2012-12-26 | 叶姝菡 | Compulsory internal recycle fluorination electrolysis reactor |
| CN202983560U (en) * | 2012-11-29 | 2013-06-12 | 山东泰德新能源有限公司 | Intermittent high shear emulsifying machine |
| CN203648523U (en) * | 2013-11-12 | 2014-06-18 | 重庆德蒙特科技发展有限公司 | Heating stirring reaction kettle |
| CN203944388U (en) * | 2014-06-10 | 2014-11-19 | 赣县鑫亿化工有限公司 | A kind of decentralized antimicrobial fluid reactor |
| CN204352873U (en) * | 2014-12-11 | 2015-05-27 | 重庆欣欣向荣精细化工有限公司 | For the stirred autoclave of cutting fluid |
| CN206518955U (en) * | 2017-03-04 | 2017-09-26 | 潍坊硕邑化学有限公司 | Automatically the filtering tank diameter cleared up |
-
2014
- 2014-12-11 CN CN201410757270.7A patent/CN104437332B/en active Active
Patent Citations (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1404163A (en) * | 1972-09-29 | 1975-08-28 | Mitsui Toatsu Chemicals | Polymerization reactor |
| CN86202953U (en) * | 1986-05-08 | 1987-07-15 | 苏州造漆厂 | Circulating stirring device |
| CN1117892A (en) * | 1994-04-18 | 1996-03-06 | 普拉塞尔技术有限公司 | Variable liquid level eductor/impeller gas-liquid mixing apparatus and process |
| CN1159437A (en) * | 1995-12-28 | 1997-09-17 | 普拉塞尔技术有限公司 | High-effect heat transfer and mass transfer for gas phase heterogeneous reaction |
| CN2559406Y (en) * | 2002-07-19 | 2003-07-09 | 南风化工集团股份有限公司 | Mixer with propeller |
| CN101054473A (en) * | 2006-04-10 | 2007-10-17 | 浙江龙盛集团股份有限公司 | Coupling production equipment and production process |
| CN201454534U (en) * | 2009-04-10 | 2010-05-12 | 天津大学 | Multiple Conduit Loop Reactor |
| CN201701758U (en) * | 2010-06-13 | 2011-01-12 | 丽珠集团福州福兴医药有限公司 | Evaporator |
| CN102839384A (en) * | 2011-06-21 | 2012-12-26 | 叶姝菡 | Compulsory internal recycle fluorination electrolysis reactor |
| CN202983560U (en) * | 2012-11-29 | 2013-06-12 | 山东泰德新能源有限公司 | Intermittent high shear emulsifying machine |
| CN203648523U (en) * | 2013-11-12 | 2014-06-18 | 重庆德蒙特科技发展有限公司 | Heating stirring reaction kettle |
| CN203944388U (en) * | 2014-06-10 | 2014-11-19 | 赣县鑫亿化工有限公司 | A kind of decentralized antimicrobial fluid reactor |
| CN204352873U (en) * | 2014-12-11 | 2015-05-27 | 重庆欣欣向荣精细化工有限公司 | For the stirred autoclave of cutting fluid |
| CN206518955U (en) * | 2017-03-04 | 2017-09-26 | 潍坊硕邑化学有限公司 | Automatically the filtering tank diameter cleared up |
Non-Patent Citations (2)
| Title |
|---|
| 分段进气多级环流反应器流动与传质特性研究;李绍果等;《化学工程》;20130715(第07期);全文 * |
| 王凯等.加料时首先进行导流筒.《混合设备设计》.北京:机械工业出版社,2000, * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104437332A (en) | 2015-03-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204485863U (en) | A kind of two-way stirring formula heating reactor | |
| CN104437329B (en) | Compound Tank Reactor | |
| CN104437332B (en) | A stirring reation kettle for cutting fluid | |
| CN204429158U (en) | A kind of dairy products detection agitating device | |
| CN202185277U (en) | Sealed constant-temperature high-speed stirring cup for laboratory | |
| CN204338161U (en) | A kind of temperature control reactor | |
| CN205761146U (en) | A kind of rotation frame chemical reaction still | |
| CN202876812U (en) | Reaction kettle for producing petrochemical products | |
| CN205269671U (en) | Two spiral shell belt reation kettle | |
| CN205269629U (en) | Raw materials recycle mixing type reation kettle | |
| CN203935841U (en) | A kind of efficient circulation reactor | |
| CN204644247U (en) | A kind of oil sludge prepares the activation pot of reclaimed rubber | |
| CN204122119U (en) | A kind of constant temperature high efficiency reactor | |
| CN206046019U (en) | A kind of cement water reducing agent reactor | |
| CN202778491U (en) | Reaction kettle | |
| CN205700549U (en) | A reaction kettle for the preparation of pure plant-based cutting fluid | |
| CN207042346U (en) | Nucleotides crystallization kettle double control stirs oar system | |
| CN204352863U (en) | Compound tank reactor | |
| CN205084682U (en) | Preparation oil gas field anti -corrosion paint's reaction unit | |
| CN204911493U (en) | Rapid mixing reation kettle | |
| CN204320315U (en) | A reaction kettle with a feed pipe extending into the bottom of the kettle | |
| CN203990634U (en) | A kind of vertical response still with function of temperature control | |
| CN204352873U (en) | For the stirred autoclave of cutting fluid | |
| CN202860506U (en) | High-pressure kettle reactor | |
| CN206325442U (en) | A kind of printing adhesive preparation mixing plant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | 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 | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 401220 No.2, Huanan No.1 Branch Road, Yanjia chemical industry park, Changshou District, Chongqing Patentee after: Chongqing Xinxin Xiangrong Fine Chemical Co.,Ltd. Address before: No.2, Huanan 1st branch road, Yanjia Chemical Industrial Park, Changshou District, Chongqing Patentee before: CHONGQING THRIVE CHEMICAL Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20241031 Address after: 401220 No.2, Huanan No.1 Branch Road, Yanjia chemical industry park, Changshou District, Chongqing Patentee after: Chongqing Xinxin Xiangrong Fine Chemical Co.,Ltd. Country or region after: China Patentee after: THIRD MILITARY MEDICAL University Address before: 401220 No.2, Huanan No.1 Branch Road, Yanjia chemical industry park, Changshou District, Chongqing Patentee before: Chongqing Xinxin Xiangrong Fine Chemical Co.,Ltd. Country or region before: China |