CN202270389U - Slurry defoaming device - Google Patents

Slurry defoaming device Download PDF

Info

Publication number
CN202270389U
CN202270389U CN201120352931XU CN201120352931U CN202270389U CN 202270389 U CN202270389 U CN 202270389U CN 201120352931X U CN201120352931X U CN 201120352931XU CN 201120352931 U CN201120352931 U CN 201120352931U CN 202270389 U CN202270389 U CN 202270389U
Authority
CN
China
Prior art keywords
slurry
defoaming device
pulp
vacuum
outlet
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.)
Expired - Fee Related
Application number
CN201120352931XU
Other languages
Chinese (zh)
Inventor
曾庆成
霍存德
张景舒
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.)
YICHUN SINQUEST ENERGY RESOURCE CO Ltd
Original Assignee
YICHUN SINQUEST ENERGY RESOURCE CO Ltd
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 YICHUN SINQUEST ENERGY RESOURCE CO Ltd filed Critical YICHUN SINQUEST ENERGY RESOURCE CO Ltd
Priority to CN201120352931XU priority Critical patent/CN202270389U/en
Application granted granted Critical
Publication of CN202270389U publication Critical patent/CN202270389U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Degasification And Air Bubble Elimination (AREA)

Abstract

The utility model discloses a slurry defoaming device, which comprises a driving device and a vacuum container, wherein the vacuum container is provided with a slurry inlet and a slurry outlet. The slurry defoaming device also comprises a tray, a slurry inlet pipe arranged on the slurry inlet, a quantitative slurry feeding pump connected with the slurry inlet pipe, a slurry outlet pipe arranged on the slurry outlet, a quantitative slurry discharging pump connected with the slurry outlet pipe, and a controlling module, wherein the tray is arranged in the vacuum container and connected with the driving device through an axle, the outlet of the slurry outlet pipe is arranged above the tray, and the controlling module is respectively connected with the driving device, the quantitative slurry feeding pump and the quantitative slurry discharging pump. The slurry defoaming device has the advantages of simple structure and good defoaming effect.

Description

浆料脱泡装置Slurry degassing device

技术领域 technical field

本实用新型涉及一种脱泡装置,具体地说,是涉及一种适于配置后的高粘度浆料脱泡处理的浆料脱泡装置。The utility model relates to a degassing device, in particular to a slurry degassing device suitable for the degassing treatment of the prepared high-viscosity slurry.

背景技术 Background technique

锂离子电池具有电压高、比能量高、循环使用次数多、存储时间长等优点,广泛应用于电动汽车、电动自行车以及电动工具等大中型电动设备方面,因此对锂离子电池的性能、成本要求越来越高。现在的锂离子动力电池在涂布时,浆料供给是由泵供料的,极片的一致性好,没有厚的区域,但是浆料供给是在管路中进行,浆料中微小的气泡排不出来,会随着浆料涂敷到极片上,产生气泡,气泡破裂后产生一凹坑,从而造成电池析锂的现象,对电池产生安全隐患。Lithium-ion batteries have the advantages of high voltage, high specific energy, many cycle times, and long storage time. They are widely used in large and medium-sized electric equipment such as electric vehicles, electric bicycles, and electric tools. Therefore, the performance and cost requirements of lithium-ion batteries Higher and higher. When the current lithium-ion power battery is coated, the slurry supply is supplied by a pump. The consistency of the pole piece is good and there is no thick area, but the slurry supply is carried out in the pipeline, and the tiny air bubbles in the slurry If it cannot be discharged, bubbles will be generated as the slurry is applied to the pole piece, and a pit will be formed after the bubble bursts, which will cause the phenomenon of lithium precipitation in the battery and pose a safety hazard to the battery.

为了去除浆料中的气泡,传统方法是于制浆完成后在真空条件下,通过搅拌浆料容器中的浆料以实现脱泡,如授权公告号为CN201930581U的中国实用新型专利公开的一种脱泡机,其通过在自转的同时能够公转的副容器的设置,来提高脱泡效果,这种结构的脱泡机气泡脱出速度高、脱泡效果好,适用于大粘度浆料的脱泡,但是,由于其需要设置传动组件来驱动联动杆、多个副搅拌桨及驱动副容器的自转和公转,结构复杂。In order to remove the air bubbles in the slurry, the traditional method is to achieve degassing by stirring the slurry in the slurry container under vacuum conditions after the pulping is completed, as disclosed in a Chinese utility model patent with the authorized announcement number CN201930581U Degassing machine, which improves the degassing effect by setting the auxiliary container that can revolve while rotating. The degassing machine with this structure has high bubble degassing speed and good degassing effect, and is suitable for degassing of large viscosity slurry However, the structure is complicated because it needs to set a transmission assembly to drive the linkage rod, multiple auxiliary stirring paddles and drive the rotation and revolution of the auxiliary container.

实用新型内容 Utility model content

本实用新型的所要解决的技术问题是针对现有技术中的浆料脱泡装置存在的不足,提供一种结构简单且脱泡效果好的浆料脱泡装置。The technical problem to be solved by the utility model is to provide a slurry degassing device with a simple structure and good degassing effect in view of the shortcomings of the slurry degassing device in the prior art.

为了解决上述技术问题,本实用新型的浆料脱泡装置包括驱动装置和真空容器,所述真空容器上具有进浆口和出浆口,本实用新型的浆料脱泡装置还包括:一托盘、一设置于所述进浆口的进浆管、一与所述进浆管相连的定量供料泵、一设置于所述出浆口的出浆管、一与所述出浆管相连的定量出料泵以及一控制模块。其中,所述托盘设置在所述真空容器内且通过一轴与所述驱动装置连接;所述进浆管的出口位于所述托盘的上方;所述控制模块与所述驱动装置、所述定量供料泵和所述定量出料泵分别相连。In order to solve the above technical problems, the slurry degassing device of the present utility model includes a driving device and a vacuum container, and the vacuum container has a slurry inlet and a slurry outlet. The slurry degassing device of the present utility model also includes: a tray , a slurry inlet pipe arranged at the slurry inlet, a quantitative feeding pump connected with the slurry inlet pipe, a slurry outlet pipe arranged at the slurry outlet, a slurry outlet connected with the slurry outlet Quantitative discharge pump and a control module. Wherein, the tray is arranged in the vacuum container and is connected with the driving device through a shaft; the outlet of the slurry feeding pipe is located above the tray; the control module is connected with the driving device, the quantitative The feed pump is connected to the quantitative discharge pump respectively.

上述的浆料脱泡装置,其中,所述真空容器内设置有一与所述控制模块连接的液位感应器。In the above slurry degassing device, a liquid level sensor connected to the control module is arranged in the vacuum container.

上述的浆料脱泡装置,其中,所述真空容器的容量为200~400L。In the above-mentioned slurry degassing device, the capacity of the vacuum container is 200-400L.

上述的浆料脱泡装置,其中,所述真空容器包括相互一体成型的柱形容器体和锥形容器体,所述锥形容器体相对处于所述柱形容器体的下方,所述进浆口设置在所述柱形容器体上,所述出浆口设置在所述锥形容器体上。The above-mentioned slurry degassing device, wherein, the vacuum container includes a cylindrical container body and a conical container body integrally formed with each other, the conical container body is relatively below the cylindrical container body, and the slurry inlet The mouth is arranged on the cylindrical container body, and the slurry outlet is arranged on the tapered container body.

上述的浆料脱泡装置,其中,所述柱形容器体上设置有一真空阀门,所述真空阀门与一抽真空装置相连。In the above-mentioned slurry degassing device, a vacuum valve is arranged on the cylindrical container body, and the vacuum valve is connected with a vacuum pumping device.

上述的浆料脱泡装置,其中,所述驱动装置通过一固定盘安装在所述柱形容器体上,所述固定盘上具有与所述进浆口相对应的以供所述进浆管穿过的通孔。The above-mentioned slurry degassing device, wherein, the driving device is installed on the cylindrical container body through a fixed plate, and the fixed plate has a corresponding slurry inlet for the slurry inlet pipe through holes.

上述的浆料脱泡装置,其中,所述托盘的边缘设置有30~50mm的凸起。In the above-mentioned slurry degassing device, a protrusion of 30-50 mm is provided on the edge of the tray.

上述的浆料脱泡装置,其中,所述进浆管的出口与所述托盘的上表面具有40~60mm的距离。The above slurry degassing device, wherein, the outlet of the slurry inlet pipe has a distance of 40-60 mm from the upper surface of the tray.

上述的浆料脱泡装置,其中,所述进浆管上设置有供浆阀门。In the above slurry degassing device, a slurry supply valve is arranged on the slurry inlet pipe.

上述的浆料脱泡装置,其中,所述出浆管上设置有出浆阀门。The above slurry degassing device, wherein, the slurry outlet pipe is provided with a slurry outlet valve.

本实用新型的有益功效在于,通过定量供料泵将浆料打在托盘上,驱动装置带动托盘高速旋转,利用离心力的作用将浆料打在真空容器的壁上,浆料由于受冲击作用和真空的作用,气泡将快速被真空破掉,达到除泡的目的;并且,进料泵和出料泵皆采用定量泵,能使供料与出料的量相同。本实用新型不仅结构简单,且浆料脱泡效果好。还有,浆料脱泡过程中不占用制浆设备,提高了制浆设备的利用率,减少了设备的投资,为连续化生产提供了保障。The beneficial effect of the utility model is that the slurry is hit on the tray by the quantitative feeding pump, the driving device drives the tray to rotate at high speed, and the slurry is hit on the wall of the vacuum container by the centrifugal force. With the action of vacuum, the bubbles will be quickly broken by the vacuum to achieve the purpose of defoaming; moreover, both the feed pump and the discharge pump are quantitative pumps, which can make the amount of feed and discharge the same. The utility model not only has a simple structure, but also has good slurry degassing effect. In addition, the slurry degassing process does not occupy the pulping equipment, which improves the utilization rate of the pulping equipment, reduces the investment in equipment, and provides a guarantee for continuous production.

以下结合附图和具体实施例对本实用新型进行详细描述,但不作为对本实用新型的限定。The utility model will be described in detail below in conjunction with the accompanying drawings and specific embodiments, but not as a limitation of the utility model.

附图说明 Description of drawings

图1为本实用新型的浆料脱泡装置的结构图。Fig. 1 is a structural diagram of a slurry degassing device of the present invention.

其中,附图标记Among them, reference signs

1-驱动装置1-Drive unit

2-真空阀门2- Vacuum valve

3-固定盘3- Fixed plate

4-轴4-axis

5-定量供料泵5- Quantitative feeding pump

6-供浆阀门6-Slurry supply valve

7-液位感应器7- Liquid level sensor

8-托盘8-tray

81-凸起81-raised

82-上表面82-upper surface

9-真空容器9- Vacuum container

91-柱形容器体91-cylindrical container body

911-进浆口911-Pulp inlet

92-锥形容器体92-tapered container body

921-出浆口921-Pulp outlet

10-定量出料泵10-quantitative discharge pump

11-控制模块11-Control Module

12-出浆阀门12-Slurry valve

13-进浆管13-Slurry inlet pipe

14-出浆管14-Pulp outlet pipe

具体实施方式 Detailed ways

下面结合附图对本实用新型的浆料脱泡装置作具体的描述:The slurry degassing device of the present utility model is described in detail below in conjunction with the accompanying drawings:

参阅图1本实用新型的浆料脱泡装置的结构图,如图所示,本实用新型的浆料脱泡装置,包括驱动装置1、真空容器9、托盘8、进浆管13、定量供料泵5、出浆管14、定量出料泵10和控制模块11。控制模块11与驱动装置1、定量供料泵5和定量出料泵10分别相连。Referring to Fig. 1 the structural diagram of the slurry degassing device of the present utility model, as shown in the figure, the slurry degassing device of the present utility model comprises a driving device 1, a vacuum container 9, a tray 8, a slurry inlet pipe 13, a quantitative supply A material pump 5, a slurry discharge pipe 14, a quantitative discharge pump 10 and a control module 11. The control module 11 is connected with the driving device 1 , the quantitative feeding pump 5 and the quantitative discharging pump 10 respectively.

作为较佳的实施例,真空容器9的容量为200~400L,且真空容器9包括相互一体成型的柱形容器体91和锥形容器体92,锥形容器体92相对处于柱形容器体91的下方,一进浆口911设置在柱形容器体91上,一出浆口921设置在锥形容器体92上。该柱形容器体91上设置有一真空阀门2,该真空阀门2与一抽真空装置(图中未示出)相连,该抽真空装置可以是真空机,以将真空容器抽成真空。驱动装置1通过一固定盘3安装在柱形容器体91上,固定盘91上具有与进浆口911相对应的以供进浆管13穿过的通孔,该驱动装置1可以采用电机,电机下方延伸一轴4,该轴4上固定连接托盘8,通过这样的设置将托盘8设置在真空容器9内,托盘8的边缘有30-50mm的凸起81。进浆管13设置于进浆口911,且进浆管13的出口位于托盘8的上方,进浆管13的出口与托盘8的上表面82较佳具有40~60mm的距离。定量供料泵5与进浆管13相连,且进浆管13上设置有供浆阀门6。出浆管14设置于出浆口921,定量出料泵10与出浆管14相连,出浆管14上设置有出浆阀门12。As a preferred embodiment, the capacity of the vacuum container 9 is 200-400L, and the vacuum container 9 includes a cylindrical container body 91 and a conical container body 92 that are integrally formed with each other, and the conical container body 92 is relatively located in the cylindrical container body 91. Below, a slurry inlet 911 is arranged on the cylindrical container body 91 , and a slurry outlet 921 is arranged on the conical container body 92 . A vacuum valve 2 is arranged on the cylindrical container body 91, and the vacuum valve 2 is connected with a vacuum device (not shown in the figure), and the vacuum device can be a vacuum machine to evacuate the vacuum container. The driving device 1 is installed on the cylindrical container body 91 through a fixed disk 3, and the fixed disk 91 has a through hole corresponding to the slurry inlet 911 for the slurry inlet pipe 13 to pass through. The driving device 1 can adopt a motor, A shaft 4 extends below the motor, and the shaft 4 is fixedly connected to the tray 8, and the tray 8 is arranged in the vacuum container 9 through such an arrangement, and the edge of the tray 8 has a protrusion 81 of 30-50 mm. The pulp inlet pipe 13 is arranged at the pulp inlet 911 , and the outlet of the pulp inlet pipe 13 is located above the tray 8 , and the distance between the outlet of the pulp inlet pipe 13 and the upper surface 82 of the tray 8 is preferably 40-60 mm. Quantitative feeding pump 5 is connected with slurry feeding pipe 13, and slurry feeding valve 6 is arranged on slurry feeding pipe 13. The pulp outlet pipe 14 is arranged at the pulp outlet 921, the quantitative discharge pump 10 is connected with the pulp outlet pipe 14, and the pulp outlet pipe 14 is provided with a pulp outlet valve 12.

进一步地,在真空容器9内设置有一与控制模块11连接的液位感应器7。Further, a liquid level sensor 7 connected to the control module 11 is arranged in the vacuum container 9 .

本实用新型的工作过程可以设置为:关闭供浆阀门6和出浆阀门12,打开真空阀门2,通过一抽真空装置对真空容器9内进行抽真空操作,当真空容器9内真空度达到-0.095MPa以上时,开启供浆阀门6,开启定量供料泵5,设定好流量,浆料经进浆管13流到托盘8上时,开启电机1(即驱动装置),设定转速(如,将转速设定为3000-4000转/分),由于离心力的作用,浆料被高速转动的转盘8摔到真空容器9的壁上,浆料中的气泡被真空破掉,当浆料液位达到容器的一半时,开启出浆阀门12,开启定量出料泵10,设定与进料相同的流量,除泡后的浆料被出料泵10移送出来。经过验证,用此方法除泡后的浆料完全没有气泡,能很好地满足锂离子动力电池涂布的要求。The working process of the present utility model can be set as follows: close the slurry supply valve 6 and the slurry output valve 12, open the vacuum valve 2, and carry out vacuuming operation in the vacuum container 9 through a vacuum pumping device, when the vacuum degree in the vacuum container 9 reaches- When it is above 0.095MPa, open the slurry supply valve 6, open the quantitative feed pump 5, set the flow rate, and when the slurry flows to the tray 8 through the slurry inlet pipe 13, open the motor 1 (that is, the driving device) and set the speed ( Such as, the rotating speed is set to 3000-4000 rpm), due to the effect of centrifugal force, the slurry is dropped on the wall of the vacuum container 9 by the rotating disk 8 rotating at high speed, and the air bubbles in the slurry are broken by the vacuum, when the slurry When the liquid level reaches half of the container, open the slurry discharge valve 12, turn on the quantitative discharge pump 10, set the same flow rate as the feed, and the defoamed slurry is transferred out by the discharge pump 10. It has been verified that the slurry after defoaming by this method has no bubbles at all, which can well meet the requirements of lithium ion power battery coating.

需要说明的是,真空容器9并不局限于上述结构,可以为其它形状。It should be noted that the vacuum container 9 is not limited to the above structure, and may be in other shapes.

当然,本实用新型还可有其它多种实施例,在不背离本实用新型精神及其实质的情况下,熟悉本领域的技术人员当可根据本实用新型作出各种相应的改变和变形,但这些相应的改变和变形都应属于本实用新型所附的权利要求的保护范围。Of course, the utility model can also have other various embodiments, and those skilled in the art can make various corresponding changes and deformations according to the utility model without departing from the spirit and essence of the utility model, but These corresponding changes and deformations should all belong to the protection scope of the appended claims of the present utility model.

Claims (10)

1. a slurry defoaming device comprises drive unit and vacuum tank, has stock inlet and grout outlet on the said vacuum tank, it is characterized in that, also comprises:
One pallet, said pallet are arranged in the said vacuum tank and through one and are connected with said drive unit;
One is arranged at the pulp-inlet pipe of said stock inlet, and the outlet of said pulp-inlet pipe is positioned at the top of said pallet;
The one quantitative charging pump that links to each other with said pulp-inlet pipe;
One is arranged at the grout outlet of said grout outlet;
The one quantitative discharging pump that links to each other with said grout outlet; And
One control module, said control module links to each other respectively with said drive unit, said quantitative charging pump and said quantitative discharging pump.
2. slurry defoaming device according to claim 1 is characterized in that, is provided with the level sensor that is connected with said control module in the said vacuum tank.
3. slurry defoaming device according to claim 1 is characterized in that, the capacity of said vacuum tank is 200~400L.
4. slurry defoaming device according to claim 1; It is characterized in that; Said vacuum tank comprises mutual integrated cylindrical container body and conical vessel body; Said conical vessel body is in the below of said cylindrical container body relatively, and said stock inlet is arranged on the said cylindrical container body, and said grout outlet is arranged on the said conical vessel body.
5. slurry defoaming device according to claim 4 is characterized in that, said cylindrical container body is provided with a vacuum valve, and said vacuum valve links to each other with a vacuum extractor.
6. slurry defoaming device according to claim 4 is characterized in that, said drive unit is installed on the said cylindrical container body through a fixed disk, has on the said fixed disk and the corresponding through hole that passes for said pulp-inlet pipe of said stock inlet.
7. according to any described slurry defoaming device among the claim 1-6, it is characterized in that the edge of said pallet is provided with the convexity of 30~50mm.
8. according to any described slurry defoaming device among the claim 1-6, it is characterized in that the outlet of said pulp-inlet pipe and the upper surface of said pallet have the distance of 40~60mm.
9. according to any described slurry defoaming device among the claim 1-6, it is characterized in that said pulp-inlet pipe is provided with the confession slurry valve.
10. according to any described slurry defoaming device among the claim 1-6, it is characterized in that said grout outlet is provided with the pulp valve.
CN201120352931XU 2011-09-20 2011-09-20 Slurry defoaming device Expired - Fee Related CN202270389U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201120352931XU CN202270389U (en) 2011-09-20 2011-09-20 Slurry defoaming device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201120352931XU CN202270389U (en) 2011-09-20 2011-09-20 Slurry defoaming device

Publications (1)

Publication Number Publication Date
CN202270389U true CN202270389U (en) 2012-06-13

Family

ID=46190781

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201120352931XU Expired - Fee Related CN202270389U (en) 2011-09-20 2011-09-20 Slurry defoaming device

Country Status (1)

Country Link
CN (1) CN202270389U (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103488199A (en) * 2013-09-17 2014-01-01 深圳市基泰智能设备有限公司 Device and method for controlling feeding and discharging of defoaming mechanism
CN103721866A (en) * 2013-12-31 2014-04-16 绵阳世诺科技有限公司 Vacuum bubble centrifugal separation device
CN105841774A (en) * 2016-04-08 2016-08-10 深圳市沃维斯环保科技有限公司 Defoaming mechanism for liquid level detection, liquid level detecting device and evaporating device
CN107774016A (en) * 2017-11-29 2018-03-09 东莞市琅菱机械有限公司 An online vacuum defoaming device
CN114160524A (en) * 2021-12-06 2022-03-11 苏州领湃新能源科技有限公司 Ultrasonic device, cleaning method and device, and defoaming machine
CN116154609A (en) * 2023-04-04 2023-05-23 深圳市光为光通信科技有限公司 Photoelectric co-packaging method based on VCSEL (vertical cavity surface emitting laser) laser

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103488199A (en) * 2013-09-17 2014-01-01 深圳市基泰智能设备有限公司 Device and method for controlling feeding and discharging of defoaming mechanism
CN103488199B (en) * 2013-09-17 2016-08-17 广东基泰智能设备有限公司 Defoaming mechanism input and output material controls Apparatus and method for
CN103721866A (en) * 2013-12-31 2014-04-16 绵阳世诺科技有限公司 Vacuum bubble centrifugal separation device
CN105841774A (en) * 2016-04-08 2016-08-10 深圳市沃维斯环保科技有限公司 Defoaming mechanism for liquid level detection, liquid level detecting device and evaporating device
CN105841774B (en) * 2016-04-08 2022-05-20 深圳市沃维斯环保科技有限公司 Defoaming mechanism for liquid level detection, liquid level detection device and evaporation device
CN107774016A (en) * 2017-11-29 2018-03-09 东莞市琅菱机械有限公司 An online vacuum defoaming device
CN114160524A (en) * 2021-12-06 2022-03-11 苏州领湃新能源科技有限公司 Ultrasonic device, cleaning method and device, and defoaming machine
CN116154609A (en) * 2023-04-04 2023-05-23 深圳市光为光通信科技有限公司 Photoelectric co-packaging method based on VCSEL (vertical cavity surface emitting laser) laser

Similar Documents

Publication Publication Date Title
CN202270389U (en) Slurry defoaming device
CN203018215U (en) Mechanical agitation type flotation machine
CN107774016A (en) An online vacuum defoaming device
CN205759891U (en) A kind of spiral gas-liquid separator
CN109467173A (en) A kind of energy-saving sewage settler
CN102886156B (en) Slurry bubble deaeration device and method
CN109654036B (en) Anti-blocking sewage discharge self-sucking pump for outdoor use
CN204981998U (en) Rare earth extraction groove device
CN208055838U (en) A kind of Landscape Construction line-marking vehicle
CN204185546U (en) A kind of aluminium melt purifying equipment getter graphite rotator
CN206334389U (en) Astragalus polyose multistage continuous extracting device
CN205164202U (en) Vertical deaeration machine
CN207384959U (en) A kind of processing coating filter device
CN205501387U (en) Waste lead -acid storage battery retrieves plumbous mud agitating unit
CN215428551U (en) Pulping system
CN205127963U (en) Polymer polymerization jar
CN109133238B (en) Aeration machine for domestic sewage convenient to increase work efficiency and can generate electricity
CN203451529U (en) Material hull-breaking device in anaerobic jar
CN204746624U (en) Mining froth flotation machine
CN202826150U (en) Membrane washing machine
CN214717522U (en) A kind of silver ore roughing flotation machine stirring device
CN207137435U (en) Defoaming device for the resin dedicated latex of polyvinyl chloride
CN112973896A (en) Excess sludge wall breaking device
CN103147251A (en) Prepressing type water distribution device
CN220661424U (en) Dissolving device for polyethylene recovery

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120613

Termination date: 20120920