CN203990334U - The manufacturing installation of a kind of suspension and colloid - Google Patents
The manufacturing installation of a kind of suspension and colloid Download PDFInfo
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- CN203990334U CN203990334U CN201420269875.7U CN201420269875U CN203990334U CN 203990334 U CN203990334 U CN 203990334U CN 201420269875 U CN201420269875 U CN 201420269875U CN 203990334 U CN203990334 U CN 203990334U
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- Colloid Chemistry (AREA)
Abstract
The utility model relates to the manufacturing installation of a kind of suspension and colloid, this device comprises and connects successively following equipment: store solvent basin and dose delivery system, pre-dispersed machine, intermediate storage tank, high speed dispersor, buffer memory is cooling and pre-deaeration agitator tank, suspension filtered purifier, vacuum defoaming device and product non-conservation tank, also comprise control system, described control system is integrated and is controlled above-mentioned each device.The utility model can effectively be prepared nano-powder material suspension and colloid, can thoroughly eliminate the aggregate in nano-powder material suspension, obtains suspension and the colloid of stable uniform.
Description
Technical field
The utility model relates to the technical field of suspension and colloid, specifically, relates to the manufacturing installation of a kind of suspension and colloid.
Background technology
Suspension and colloid preparation method and manufacturing installation system can be used for preparing high performance electrocondution slurry, ceramic coating, ceramic marking ink etc., along with the more and more attention of international community to environmental protection and the energy, above-mentioned every profession and trade all has more and more higher requirement to slurry.For example, the security of the development of the industries such as ev industry to portable power source, uniformity, stability and energy density have proposed more and more higher requirement.Therefore the preparation of lithium ion battery and super capacitor slurry has been proposed to more and more higher requirement.And for example, how that the nano materials such as CNT, Graphene, nano aluminium oxide, silica is dispersed in the industrialization process of Application of micron, the suspension without reunion of formation uniformity and colloid are to prepare high performance electrocondution slurry, ceramic coating, pottery marking inks etc., also become problem demanding prompt solution.
For another example, in the painting membrane process of battery and super capacitor slurry, in the preparation process of nano ceramic coat, and in the coating procedure of the conductive coating of LED film, the material of employing is nanometer increasingly, coating is ultrathin increasingly, this just requires these coating evenly necessary in whole coating procedure, stable, without reuniting, without sedimentation.
And along with the appearance of novel nano-material, the difficulty of manufacturing various suspension and composite by these nano materials is increasing.The heavy industrialization application of these materials needs more efficiently nano material dispersion technology.
But existing suspension and colloid technology of preparing include stirring technique, grinding technique, sand milling technology, high shear dispersion technology, high pressure homogenization technique etc.The length consuming time that these technology have, efficiency is low.Some operation easier are large, and consumptive material is expensive.Structure and the performance that can destroy nano material that have, what have cannot disperse above-mentioned novel nano-material even at all.
Existing feeding technique is all to utilize the way of vacuum draw powder body material to be added to the surface of solvent from the top of stirred vessel.This method not only causes powder body material to fly upward, the top cover that pollutes stirred vessel, forms dry and hard slurry at top, and very easily on paddle and in stirred vessel, forms the bulk reunion of powder body material, therefore mixing plant needs long-play, expends mass energy and disperses these aggregates.In addition, the every subjob of mixing plant top and paddle is complete, need to carefully clean, otherwise dry and hard slurry and aggregate can enter in lower batch of material, worsens product quality.
Existing suspension and colloid technology of preparing, in order to guarantee that final viscosity is in control range, conventionally adopt the way of adjusting solid content to adjust degree of being stained with, consequently the viscosity of suspension and colloid has reached control requirement, but the solid content of suspension and colloid has changed, at some, need in the product of accurate coating, the change of solid content will change the surface density of coating.Make painting process need all will adjust for a long time equipment in order to reach surface density control target at every turn.
For secondary cell and ultracapacitor, the reunion of the reunion of conductive powder body and active material powder will cause the rising of their internal resistances and the decline of capacity, and therefore has a strong impact on uniformity and the stability of product.
Negative effect for fear of the aggregate of powder body material in suspension to rear operation, need to carry out filtration, purification to the aggregate of suspension conventionally, and while containing a large amount of aggregate in suspension, the filter efficiency of suspension is extremely low, sometimes even cannot normally produce.
In sum, along with the particularly appearance of nano-powder material of new material, the technology of preparing of suspension has been proposed to more and more higher requirement.Existing suspension technology of preparing cannot meet the requirement of technological progress.Need to there be new suspension and colloid preparation method and manufacturing installation to solve problem.
Utility model content
In order to overcome the above-mentioned deficiency of prior art, the utility model provides the manufacturing installation of a kind of new suspension and colloid.The utility model can thoroughly be eliminated the aggregate in nano-powder material suspension, does not destroy structure, pattern and the surface coating layer of nano-powder material simultaneously, prepares suspension and the colloid of stable uniform, for good condition has been created in the fine finishining of rear operation.
For achieving the above object, the technical scheme that the utility model adopts is:
The manufacturing installation of a kind of suspension and colloid, connect successively following equipment: store solvent basin and dose delivery system, pre-dispersed machine, intermediate storage tank, high speed dispersor, buffer memory is cooling and pre-deaeration agitator tank, suspension filtered purifier, vacuum defoaming device and product non-conservation tank, also comprise control system, control system is integrated and is controlled above-mentioned each device.
As preferred version, in high speed dispersor, be provided with taper or the circular dispersion wheel of High Rotation Speed, there is groove on dispersion wheel surface, and dispersion wheel overcoat has taper or the circular dispersion slot of correspondingly-shaped.Dispersion wheel by High Rotation Speed and and taper or circular dispersion slot between the aggregate of centrifugal shock dispersing solid material of the interaction shearing, friction and the solids in suspension material that produce.
Another preferred version is, on the inwall of dispersion slot, is processed with groove, and this dispersion slot two-layerly consists of inside and outside, comprises adiabatic anti-caking cut-layer and Forced water cooling layer.
Another preferred version is, the gap between the taper of High Rotation Speed or circular dispersion wheel and taper or circular dispersion slot is adjustable between 1-3 millimeter, and the adjustment in gap is to increase and decrease to realize by the pad between taper or circular dispersion wheel and main shaft.
Another preferred version is that the top of high speed dispersion wheel is provided with guide ring.
Another preferred version is on the top main shaft of high-speed rotary part, to be provided with the umbrella shape deflector of High Rotation Speed.Deflector can guide the liquid that enters dispersion slot to circulate, and can take away the heat that high speed dispersion produces simultaneously.
Another preferred version is that dispersion wheel and dispersion slot are all processed by metal and the nonmetallic materials of high intensity wear-resistant.
Preparation method described in the utility model and apparatus system, be suitable for the preparation of various suspension and colloid.Be particularly suitable for the preparation of nano-powder material suspension.
Accompanying drawing explanation
Fig. 1 is the manufacturing system figure of suspension of the present utility model and colloid;
Fig. 2 is the section of structure of pre-dispersed equipment in Fig. 1 manufacturing system;
Fig. 3 is the section of structure of Fig. 1 manufacturing system high speed dispersal device;
Fig. 4 is the section of structure of vacuum defoamation machine in Fig. 1 manufacturing system;
Fig. 5 is structural representation cooling in Fig. 1 and pre-deaeration system.
The specific embodiment
Preferred embodiment of the present utility model is below provided, to help further, understand the utility model, but protection domain of the present utility model is not limited in these embodiment.
Fig. 1 discloses the overall structure figure of a kind of suspension and colloid preparation facilities system, and this manufacturing installation system mainly adds and pre-dispersed system 200, pre-dispersed suspension and colloid intermediate storage system 300, high speed dispersing device 400, suspension and colloid is cooling and pre-deaeration system 500, suspension and colloid filtration, purification system 600, vacuum defoamation system 700 suspension and colloid finished product turnaround system 800 and control system 900 form by solvent storage and dose delivery system 100, powder body material are on-line automatic.
Solvent storage and dose delivery system 100 include holding vessel 101, solvent filtration apparatus 102 and solvent delivery device 103; Holding vessel 101 design is used for storage of solvent and uses.It is with level display device (not shown), fluid level control device (not shown), solvent metering device (not shown).On holding vessel 101, be also provided with dry air or high pure nitrogen import, to avoid the impact of moisture in air on solvent.
Coordinate shown in Fig. 2, powder body material is on-line automatic to add and pre-dispersed system 200, premixed and the pre-dispersed equipment before suspension high speed dispersion, it include powder body material feed system 201, solvent circulation impeller 202, powder body material pre-dispersing device 203, pre-dispersed liquid agitator tank 204,, paddle 205, cooling system 206 and power set 207, belt gear 208, mechanical sealing system 209, slurry circulating line 210 and pre-dispersed cavity 211.Solvent circulation impeller 202, stirring arm 205 are located in pre-dispersed liquid agitator tank 204; Mechanical sealing system 209 is located at the below of pre-dispersed liquid agitator tank 204; Power set 207 are connected with solvent circulation impeller 202 by belt gear 208; Cooling system 206 is coated on outside pre-dispersed liquid agitator tank 204, to it, carries out cooling.The lower position of pre-dispersed cavity 211 is located in one end of slurry circulating line 210, and the upper position of pre-dispersed liquid agitator tank 204 is located in one end.
In use, power set 207 are drive motors, it rotates solution circulation impeller 202 by belt gear 208, and drive powder body material pre-dispersing device 203 High Rotation Speeds, solvent is drawn into pre-dispersed cavity 211 from pre-dispersed liquid agitator tank 204, and produce negative pressure of vacuum at powder body material feed system 201 and pre-dispersed cavity 211 interfaces, the powder body material in powder body material feed system 201 is drawn into pre-dispersed cavity 211.The solvent being inhaled into and powder body material are under mixed, the peptizaiton of pre-dispersing device 203, and solvent and powder body material are entered pre-dispersed liquid agitator tank 204 by tentatively mixed merga pass slurry circulating line 210; And further mix under the effect of paddle 205.Agitator tank 204, except playing suspension mixed effect, also has temp regulating function, nitrogen protection function, vacuum defoamation and auxiliary circulation function, automatic cleaning function.Powder body material is on-line automatic to add and pre-dispersed system 200, and its powder body material progressively evenly adds; Powder body material is directly sneaked in solvent; Powder body material is online pre-dispersed.Avoided increasing suddenly because powder body material once adds the viscosity causing; Avoided the formation of large-scale agglomerate; Avoided powder body material from solvent surface, to add airborne dust and the pollution problem of generation.
In addition, to the material dropping in pre-dispersed system 200, can be organic solvent and inorganic solvent (deionized water), include but not limited to nanometer grade powder material, Powdered Polymer Materials, additive etc.They can be lithium ion battery plus-negative plate materials, super capacitance electrode material, conductive agent, nano metal powder, nano-silicone wire/carbon alloy, nano-silicon and other nano inorganic powder materials.
Automatically the powder body material adding in pre-dispersed system takes the mode of continuous uniform to add, and adds the simultaneous solvent of powder and the high-speed circulating of suspension, in pre-dispersed good suspension and colloid, contains tiny aggregate.They are discharged from the bottom of agitator tank, through pump, are pumped into intermediate storage tank 300.
The effect of pre-dispersed suspension and colloid intermediate storage system 300 is to guarantee to supply with continuously suspension and colloid to high speed dispersing device 400.Intermediate storage system is one, and with the storage tank 302 of stirring at low speed oar 301, intermediate storage system can continue to stir suspension and the colloid in storage tank, prevents that its sedimentation and viscosity from changing.Intermediate storage system can also reduce by the circulating water cooling system of storage tank periphery the temperature of suspension and colloid.Suspension and the colloid adjusted after temperature are transported to high speed dispersor 400 from tank bottom continuously through pump 310.In the porch of pump 310, be provided with the preliminary filter (not shown) of suspension and colloid.Object is to prevent that foreign matter from entering high speed dispersor and causing high speed dispersor to damage.
Fig. 3 is the profile of high speed dispersor.High speed dispersor 400 is by a taper or circular dispersion slot 410, and at taper or circular dispersion wheel 420, deflector 430, sealing device 440 and the high speed rotating shaft 450 of dispersion slot 410 interior High Rotation Speeds.The discharging portion 460 that the suspension on taper or circular dispersion slot 410 tops and colloid are discharged forms.
Dispersion slot 410 its inside are the liner 411 of a taper, outside is circulating cooling water leg 412, by the chilled water in cooling water jecket 412, force suspension and the colloid in cooling dispersion slot 410, the dispersion wheel 420 of dispersion slot 410 interior High Rotation Speeds is by high speed rotating shaft 450, and shaft coupling is driven by Fast frequency spindle motor 451.Between dispersion slot 410 and discharging portion 460, be provided with deflector 430.The top of dispersion slot 410 is discharging portions 460, the outside of discharging portion 460 is with recirculated cooling water cover 461, the bottom of dispersion slot 410 is provided with the inlet 413 of suspension and colloid, the side of discharging portion 460 is provided with the outlet 462 of suspension and colloid, and the suspension after high speed dispersion and colloid are discharged to outside.
Between the outer wall 421 of the taper liner 411 of dispersion slot 410 and the dispersion wheel 420 of High Rotation Speed, be formed with the gap of 1～3mm left and right, this gap can be adjusted by adjusting the height of the dispersion wheel 420 of High Rotation Speed.The manufacturing installation of this suspension and colloid also includes the pad in capable of regulating High Rotation Speed dispersion wheel 420 and dispersion slot 410 gaps, and this pad is located between dispersion wheel 420 and main shaft.On the surface of the outer wall 421 of dispersion wheel 420, be carved with crisscross groove (not shown), and be processed with the inside and outside manhole 423 connecting.
The liner 411 of dispersion slot 410, its material can be stainless steel, pottery and hardening oxidation aluminium alloy, crisscross groove can be carved with in its surface.The material of the dispersion wheel 420 of High Rotation Speed on the other side can be stainless steel, pottery and hardening oxidation aluminium alloy or coating hard ceramic material on the outer surface of conical part.As above-mentioned ceramic material or ceramic coated, its object is increasing the anti-wear performance of parts, eliminates metal material abrasion and the metal impurities that cause pollute simultaneously.
The dispersion wheel 420 of High Rotation Speed, Fast frequency spindle motor 451 drives and High Rotation Speed through shaft coupling and high speed rotating shaft 450.Its outer wall 421 is (15～70 meter per second) with respect to the linear velocity between the liner 411 of dispersion slot
The suspension and the colloid that by dispersion slot 410 bottoms, are imported, this suspension and colloid are under dispersion wheel 420 effects of High Rotation Speed, clash into the liner 411 of dispersion slot 410, disengaging meeting due to suspension and colloid simultaneously produces vacuum at the outer wall of dispersion wheel 420, and the suspension of its inner side and colloid are inhaled to periphery by the manhole 423 on it.High Rotation Speed, mutually friction in opposite directions in suspension and the colloid gap between the liner 411 of dispersion slot 410 and the outer wall 421 of dispersion wheel 420.The effect of the guide ring 430 arranging due to the top of dispersion slot 410.Suspension and colloid are at the interior ring-type fluid column that forms a taper of dispersion slot 410.Suspension and colloid are under dispersion wheel 420, dispersion slot 410 and guide ring 430 threes' of High Rotation Speed interaction, and by clashing into, the ringing of shearing and rubbing, thoroughly disperses the aggregate in suspension and colloid.Gap width between the liner 411 of dispersion slot 410 and the dispersion wheel outer wall 421 of High Rotation Speed, dispersion wheel 420 linear velocities of rotation and the width of guide ring 430 also can be done different adjustment according to the character of suspension and colloid.
Enter suspension and the colloid of dispersion slot 410, under the effect of the dispersion wheel 420 of High Rotation Speed, liner 411 along dispersion slot 410 upwards climbs, guide functions due to guide ring 430, suspension and colloid will reflux and again circulate and disperse, until reach after required jitter time, just from the edge of guide ring 430, rise to discharging portion 460, and drain into cooling and pre-deaeration system 500 from the outlet of discharging portion 460.
Suspension and colloid are in dispersion slot 410, and the High Rotation Speed effect by dispersion wheel 420, applies powerful shearing, clash into and rubbing action, make the tiny reunion of suspension and colloid realize dispersion thoroughly.Because its energy applying is huge, suspension and colloid will produce a large amount of heats and steep temperature rise.For the temperature of suspension and colloid being controlled in the scope of process specification requirements, the periphery of dispersion slot 410, the inside of the periphery of discharging portion 460 and guide ring 430 is provided with cooling water circulation passageway, cooling to the pressure of suspension and colloid by cooling water, the temperature of suspension and colloid is controlled in the control range of technological standards.
Shown in figure 5, suspension and colloid are after high speed dispersor disperses, outlet 462 by high speed dispersor discharging portion 460 is expelled to cooling and pre-deaeration system 500, cooling and pre-deaeration system 500 includes agitator tank 501, shaft 502, stirring vane 503, power set 504, vacuum plant 505 and cooling device 507, and shaft 502 is connected with the output of power set 504; Stirring vane 503 is located on shaft 502, and on the bracing frame 506 of vacuum plant 505 agitator tanks 501, it communicates with agitator tank 501, and it is for applying negative pressure to agitator tank 501.Cooling device 507 is located on agitator tank 501 lower positions.
During use, start power set 504, in the present embodiment, it is drive motors, and it drives shaft 502 to rotate, and drives stirring vane 503 to rotate in agitator tank 501, and the suspension in agitator tank 501 and colloid are stirred.The recirculated cooling water cooling suspension of cooling device 507 and colloid prevent that its precipitation and viscosity from increasing on the stirring at low speed by agitator tank 501 and tank body; By vacuum plant 505, apply the bubble that negative pressure and low rate mixing partly eliminate in suspension and colloid again and reduce slurry viscosity, be beneficial to filtration and the purification of rear operation.
That is, because the periphery of system basin surrounds circulating cooling water jacket, suspension and colloid further mix under the effect of paddle 510, cooling, and under the effect of negative pressure, remove part bubble.Another effect cooling and pre-deaeration system is the stability that maintains suspension and colloid viscosity, blocks the impact of follow-up vacuum defoamation system on high speed dispersion operation.
Suspension and colloid through supercooling and pre-deaeration are delivered to filtration, purification system 600 through pump, suspension and colloid are after filter filters, enter successively purifier, the suspension after filtration, purification and colloid will filtering part aggregate and metal impurities.
Suspension after filtration, purification and colloid, under the negative pressure of vacuum effect of vacuum defoamation system 700, enter into the rotary drum 710 of vacuum defoamation system, under the centrifugal action producing in drum rotating to external expansion.On the surface of rotary drum, form thin film, the bubble in film breaks under vacuum action, and the suspension after deaeration and colloid gather at the edge of rotary drum 710, through being pumped into turnaround system 800.
Suspension after vacuum defoamation and colloid are transported to turnover basin (801,802,803) through pump.Turnover basin is comprised of paddle 810, circulating cooling chuck 820, Moving caster 830, automatic cleaning system 840, vacuum orifice 850 and level monitoring system 860.Suspension and colloid are delivered to after turnover basin, further stirring, deaeration and stabilization, and be transported to lower operation and further process processing.As coating, printing etc.
For above-mentioned each subsystem is integrated into automatic manufacturing system.Control system 900, by PLC, is all carried out online control by solvent storage and dose delivery system to each subsystem of turnaround system.Not only control each subsystem startup, stop and moving, monitor the operational factors such as temperature, pressure, flow, liquid level, speed, rotating speed, vacuum of each subsystem operation, the service data of each equipment in register system, and each equipment in system is sent to operational order, make the operation of system realize intellectuality and automation.
In the present embodiment, powder body material is on-line automatic adds and pre-dispersed system, not only solved the airborne dust problem of traditional feed way, and solved the problem that the reinforced bulk agglomeration traits producing in enormous quantities and suspension and colloid viscosity sharply increase, improve greatly pre-dispersed efficiency, effectively solved the pre-dispersed difficult problem of similar ultra-fine CNT.
High speed dispersor in the present embodiment, by taper or circular dispersion slot, taper or circular dispersion wheel and the constructed high-speed dispersion system of guide ring, can be by applying huge energy, by shearing, clash into and friction, make the aggregate high degree of dispersion of the special nano-powder material of powder body material in suspension and colloid.Form that solid content is consistent, viscosity stabilization, not free settling and suspension and the colloid of again reuniting.Owing to there is not the aggregate not disperseing in suspension and colloid, not only can improve the filtration treatment efficiency of rear operation but also greatly improve uniformity and the stability of suspension and colloid.
Vacuum defoamation machine in the present embodiment, can eliminate the bubble in suspension and colloid effectively, can stable suspension and the viscosity of colloid, improve its mobility and compactness.Coating and the printing quality of operation after improving.
Above-described embodiment is preferably embodiment of the utility model; but embodiment of the present utility model is not restricted to the described embodiments; other any do not deviate from change, the modification done under Spirit Essence of the present utility model and principle, substitutes, combination, simplify; all should be equivalent substitute mode, within being included in protection domain of the present utility model.
Claims (8)
1. the manufacturing installation of a suspension and colloid, it is characterized in that, connect successively following equipment: store solvent basin and dose delivery system, pre-dispersed machine, intermediate storage tank, high speed dispersor, buffer memory is cooling and pre-deaeration agitator tank, suspension filtered purifier, vacuum defoaming device and product non-conservation tank, also comprise control system, described control system is integrated and is controlled above-mentioned each device.
2. the manufacturing installation of suspension according to claim 1 and colloid, it is characterized in that, the taper or the circular dispersion wheel that in described high-speed dispersion system, are provided with High Rotation Speed, there is groove on the surface of described dispersion wheel, and described dispersion wheel overcoat has taper or the circular dispersion slot of correspondingly-shaped.
3. the manufacturing installation of suspension according to claim 2 and colloid, is characterized in that, on the inwall of described dispersion slot, is processed with groove, and described dispersion slot two-layerly consists of inside and outside, comprises adiabatic anti-caking cut-layer and Forced water cooling layer.
4. the manufacturing installation of suspension according to claim 3 and colloid, is characterized in that, dispersion wheel and the gap between dispersion slot of described High Rotation Speed are adjustable between 1-3 millimeter.
5. the manufacturing installation of suspension according to claim 4 and colloid, is characterized in that, it also further includes High Rotation Speed dispersion wheel described in capable of regulating and the pad in dispersion slot gap, and described pad is located between dispersion wheel and main shaft.
6. the manufacturing installation of suspension according to claim 2 and colloid, is characterized in that, the top of described high speed dispersion wheel is provided with guide ring.
7. the manufacturing installation of suspension according to claim 2 and colloid, is characterized in that, is provided with the umbrella shape deflector of High Rotation Speed on the top main shaft of described high-speed rotary part.
8. the manufacturing installation of suspension according to claim 2 and colloid, is characterized in that, described dispersion wheel and dispersion slot are all processed by metal and the nonmetallic materials of high intensity wear-resistant.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420269875.7U CN203990334U (en) | 2014-05-23 | 2014-05-23 | The manufacturing installation of a kind of suspension and colloid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420269875.7U CN203990334U (en) | 2014-05-23 | 2014-05-23 | The manufacturing installation of a kind of suspension and colloid |
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| CN203990334U true CN203990334U (en) | 2014-12-10 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420269875.7U Expired - Lifetime CN203990334U (en) | 2014-05-23 | 2014-05-23 | The manufacturing installation of a kind of suspension and colloid |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105080376A (en) * | 2014-05-23 | 2015-11-25 | 深圳市尚水智能设备有限公司 | Suspension and colloid preparation method, and apparatus system and application thereof |
| CN105233771A (en) * | 2015-10-13 | 2016-01-13 | 广东裕田霸力科技股份有限公司 | Adhesive production system |
| JP2017202431A (en) * | 2016-05-09 | 2017-11-16 | 日本スピンドル製造株式会社 | Dispersive mixing device and its operational method |
| CN107596937A (en) * | 2017-11-01 | 2018-01-19 | 东莞大蜥蜴智能系统有限公司 | A kind of novel lithium battery on-line continuous pulp making process equipment production line |
| CN108970554A (en) * | 2017-05-31 | 2018-12-11 | 未来与挑战株式会社 | High temperature and pressure is generated with aerosol and hybrid system |
| CN110559695A (en) * | 2019-08-29 | 2019-12-13 | 安徽銮威化工科技开发有限公司 | graphene oxide modified organic silicon defoaming agent and preparation method thereof |
-
2014
- 2014-05-23 CN CN201420269875.7U patent/CN203990334U/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105080376A (en) * | 2014-05-23 | 2015-11-25 | 深圳市尚水智能设备有限公司 | Suspension and colloid preparation method, and apparatus system and application thereof |
| CN105080376B (en) * | 2014-05-23 | 2018-09-04 | 深圳市尚水智能设备有限公司 | Manufacturing method and apparatus system and the application of a kind of suspension and colloid |
| CN105233771A (en) * | 2015-10-13 | 2016-01-13 | 广东裕田霸力科技股份有限公司 | Adhesive production system |
| JP2017202431A (en) * | 2016-05-09 | 2017-11-16 | 日本スピンドル製造株式会社 | Dispersive mixing device and its operational method |
| CN108970554A (en) * | 2017-05-31 | 2018-12-11 | 未来与挑战株式会社 | High temperature and pressure is generated with aerosol and hybrid system |
| CN107596937A (en) * | 2017-11-01 | 2018-01-19 | 东莞大蜥蜴智能系统有限公司 | A kind of novel lithium battery on-line continuous pulp making process equipment production line |
| CN110559695A (en) * | 2019-08-29 | 2019-12-13 | 安徽銮威化工科技开发有限公司 | graphene oxide modified organic silicon defoaming agent and preparation method thereof |
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Inventor after: Jin Xudong Inventor after: Tan Yulin Inventor after: Yan Yongjun Inventor before: Yan Yongjun |
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Free format text: CORRECT: INVENTOR; FROM: YAN YONGJUN TO: JIN XUDONG TAN YULIN YAN YONGJUN |
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Address after: 518118 Pingzhi main plant 201, Huakong SEG plant, No. 6, Lanzhu East Road, Zhukeng community, Longtian street, Pingshan District, Shenzhen, Guangdong Patentee after: Shenzhen Shangshui Intelligent Co.,Ltd. Address before: Room 302, Building 10, Third Industrial Zone, Kuiyong Street, Longgang District, Shenzhen City, Guangdong Province (office space) Patentee before: SHENZHEN SHANGSHUI INTELLIGENT EQUIPMENT Co.,Ltd. |
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Granted publication date: 20141210 |