CN208356787U - A kind of high-temperature spray consersion unit - Google Patents
A kind of high-temperature spray consersion unit Download PDFInfo
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- CN208356787U CN208356787U CN201820734093.4U CN201820734093U CN208356787U CN 208356787 U CN208356787 U CN 208356787U CN 201820734093 U CN201820734093 U CN 201820734093U CN 208356787 U CN208356787 U CN 208356787U
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Abstract
The utility model is suitable for technical field of material, provide a kind of high-temperature spray consersion unit, including feed proportioning system, atomization system, material-receiving system and air-channel system, atomization system includes multiple atomisation towers with atomization chamber, feed proportioning system includes multiple for providing the atomizer of the first liquid phase reactor object into the atomization chamber, and the first liquid phase reactor object for being provided to multiple atomization chambers from multiple atomizers is identical or different.The utility model is by being arranged multiple atomisation towers, and the atomization chamber of each atomisation tower connects an atomizer, the first liquid phase reactor object that multiple atomizers are provided to multiple atomization chambers is identical or different, it can be realized in multiple atomisation towers while carrying out atomization reaction, and different reactions can occur in different atomization chambers, multiple product is obtained in multiple atomization chambers simultaneously, to realize the preparation of lot of materials or a large amount of different characteristic materials, the high-throughput preparation of high-temperature atomizing reaction is realized.
Description
Technical field
The utility model belongs to technical field of material, in particular to a kind of high-temperature spray consersion unit.
Background technique
High-temperature spray reaction be it is a kind of feed liquid is separated into tiny droplet using atomizer, and carry out in the high temperature environment
Pyrolysis reacts the technology to form powder product with gas raw material.Feed liquid is after being atomized, if surface area moment increases
Dry times, increases with the contact area of high-temperature gas or reaction gas, significantly improve reaction rate.Although temperature when spray reaction
It is relatively high, but when contacting feed liquid droplet, major part heat is all used for moisture evaporation, so temperature of outgoing air is not high, for some
Heat sensitive material also can guarantee its product quality.It can make product that powder or hollow sphere be made after spray reaction, therefore product has
Good dispersibility and dissolubility.Spray reaction production process is simple, is suitable for serialization large-scale production.
" high throughput preparation " is the preparation for being completed in a short time a large amount of different characteristic materials or product.High throughput preparation
With many merits and application: firstly, it can be calculated for material simulation provides the basic data of magnanimity, obtaining material database
To enrich；Secondly, the result that can be calculated for material simulation provides experimental verification, computation model is made to be optimized, be corrected；More
Importantly, high-throughput preparation has better comparativity and repeatability, thus can rapidly provide valuable research at
Fruit, the screening and optimization of direct accelerated material.Other than the application in terms of investigation of materials, high throughput preparation can use product
Production, while the product of different constituent element contents, feature or different technical parameters is prepared, be conducive to the efficient utilization of energy,
Be conducive to the steady production of product.Therefore, high-throughput preparation is received in larger range by material and chemical industrial field,
It is widely used in the research and development and industrialization of metal, ceramics, inorganic compound, macromolecule, catalyst and other material, such as Corning Incorporated
PMN-PT electro-optic ceramics is prepared using high throughput and and realizes optical communication device industrialization, Intel Company and Samsung
Using the technical research phase change memory alloy and high dielectric material, Symyx company prepares novel chemical catalysis using high throughput
Agent etc..
But at present in terms of high-temperature spray reaction, there are no relevant high-throughput Preparation equipments, therefore, high-temperature spray
Consersion unit realize high-throughput preparation will be greatly promoted multicomponent composite granule, thin-film material preparation and can be simultaneously
Carry out the production of a variety of chemical products.
Utility model content
The purpose of this utility model is to provide a kind of high-temperature spray consersion units, it is intended to solve the spray of prior art high temperature
The technical issues of high-throughput preparation, is not yet realized in mist reaction.
The utility model is realized in this way a kind of high-temperature spray consersion unit, including feed proportioning system, atomization system, receipts
Material system and air-channel system, the atomization system include multiple atomisation towers, and each atomisation tower includes atomization chamber, the atomization chamber
One end is equipped with feed inlet, and the other end of the atomization chamber is equipped with discharge port, and the feed proportioning system includes multiple is used for the mist
Change the atomizer of the first liquid phase reactor object of intracavitary offer, each atomisation tower connects an atomizer, the air-channel system
Compressed air source unit including being connected to the feed inlet of the atomisation tower, the material-receiving system include the discharging for being connected to the atomisation tower
Mouthful separator, it is identical or not to be provided to the first liquid phase reactor object in multiple atomization chambers from multiple atomizers
Together.
The feed inlet is set to the lower end of the atomization chamber, and the discharge port is set to the upper end of the atomization chamber, the mist
Change system further includes an at least atomizer, and the atomizer is connected to the feed inlet of multiple atomisation towers, and the atomizer is used
In providing the second liquid phase reactant of atomization into the atomization chamber.
Each atomization chamber connects an atomizer, multiple atomizers provided into multiple atomization chambers second
Liquid phase reactor object is identical or different.
The second liquid phase reactant and the first liquid phase reactor object are identical or different.
The atomizer is connected between the feed inlet and the compressed air source unit, and the inertia that the compressed air source unit provides is protected
It protects gas or reaction gas and enters the atomization chamber through the atomizer.
The separator is cyclone separator, and the material-receiving system further includes being connected to the cyclone separator and the mist
Change the air blower between device.
The feed proportioning system further includes the measurer for being connected to multiple atomizers, and the measurer includes multiple matches
Expect area, each ingredient area is connected to an atomizer.
The high-temperature spray consersion unit further includes the linked system being connected between the atomization system and material-receiving system,
The linked system adjusts the atomization system and the material-receiving system for linking.
The atomization system further includes the vibrator for being connected to the atomisation tower, and the vibrator drives the atomisation tower shake
It is dynamic.
The high-temperature spray consersion unit further includes heating system, and the heating system includes heater, has heating chamber
Heated shell and the insulating layer that is covered in outside the heated shell, the heater heats the heated shell, more
A atomisation tower is set in the heating chamber.
The beneficial effect of high-temperature spray consersion unit provided by the utility model is: by the way that multiple atomisation towers are arranged, and
And the atomization chamber of each atomisation tower connects an atomizer, the cyclone separator of the discharge port connection material-receiving system of atomisation tower, energy
Enough realize carries out atomization reaction simultaneously in multiple atomisation towers, and can allow for the material of different ratio through different atomizers
Into corresponding atomization chamber, different products is obtained after reaction, to realize lot of materials or a large amount of different characteristic materials
Preparation realizes the high-throughput preparation of high-temperature atomizing reaction.
Detailed description of the invention
Fig. 1 is the construction module schematic diagram of high-temperature spray consersion unit provided by the embodiment of the utility model.
Meaning marked in the figure are as follows:
100- high-temperature spray consersion unit, 1- feed proportioning system, 10- atomizer, 11- measurer, 12- surge tank, 13-
One flow control valve, 14- first flow detector, 2- atomization system, 20- atomisation tower, 21- atomization chamber, 22- feed inlet, 23- go out
Material mouth, 24- atomizer, 25- vibrator, 3- material-receiving system, 30- cyclone separator, 31- air blower, 4- air-channel system, 40- gas
Source device, 41- gas cushion, 5- heating system, 51- heating device, 52- heating chamber, 53- insulating layer, 54- heated shell,
6- linked system.
Specific embodiment
In order to make the purpose of the utility model, technical solutions and advantages more clearly understood, below in conjunction with attached drawing and implementation
Example, the present invention will be further described in detail.It should be appreciated that specific embodiment described herein is only to explain this
Utility model is not used to limit the utility model.
It should be noted that when component is referred to as " being fixed on " or " being set to " another component, it can directly or
It connects on another component.When a component is known as " being connected to " another component, it be can be directly or indirectly
It is connected on another component.The orientation or positional relationship of the instructions such as term " on ", "lower", "left", "right" is based on attached drawing
Shown in orientation or positional relationship, be merely for convenience of describing, rather than the device or element of indication or suggestion meaning must have
There is specific orientation, be constructed and operated in a specific orientation, therefore should not be understood as the limitation to this patent.Term " first ",
" second " is used merely to facilitate description purpose, is not understood to indicate or imply relative importance or implicitly indicates technical characteristic
Quantity.The meaning of " plurality " is two or more, unless otherwise specifically defined.
In order to illustrate technical solution described in the utility model, carried out specifically below in conjunction with specific accompanying drawings and embodiments
It is bright.
Referring to Fig. 1, the utility model provides a kind of high-temperature spray consersion unit 100, including feed proportioning system 1, atomization system
System 2, material-receiving system 3 and air-channel system 4, atomization system 2 include multiple atomisation towers 20, and each atomisation tower 20 includes atomization chamber 21,
The lower end of atomization chamber 21 is equipped with feed inlet 22, and the upper end of atomization chamber 21 is equipped with discharge port 23, feed proportioning system 1 include it is multiple for
The atomizer 10 of the first liquid phase reactor object is provided in atomization chamber 21, an atomizer 10 is connected on the inside of an atomisation tower 20
End, air-channel system 4 include the compressed air source unit 40 for being connected to the feed inlet 22 of atomisation tower 20, and material-receiving system 3 includes being connected to atomization
The cyclone separator 30 of the discharge port 23 of tower 20 is provided to the first liquid phase reactor of multiple atomization chambers 21 from multiple atomizers 10
Object is identical or different.
The progress of high-temperature spray consersion unit 100 provided by the utility model compared with the existing technology is:
By the way that multiple atomisation towers 20, and the one atomization spray of inner upper end connection of the atomization chamber 21 of each atomisation tower 20 is arranged
Mouth 10, the discharge port 23 of atomisation tower 20 connect the cyclone separator 30 of material-receiving system 3, and multiple atomizers 10 are provided to multiple mists
The the first liquid phase reactor object for changing chamber 21 is identical or different, can be realized in multiple atomisation towers 20 while carrying out atomization reaction, and
It can allow for the material of different ratio to react in different atomization chambers 21, while obtaining multiple product, to realize a large amount of
The preparation of material or a large amount of different characteristic materials realizes the high-throughput preparation of high-temperature atomizing reaction.
Specifically, referring to Fig. 1, feed proportioning system 1 further includes measurer 11, and measurer 11 and atomizer are connected to
Surge tank 12 between 10.Measurer 11 is used for the addition of the first liquid phase reactor object, which can be one kind
Substance is also possible to the mixture of many kinds of substance.Surge tank 12 is for further mixing the first liquid phase reactor object, adjusting first
The air etc. that liquid phase reactor logistics may be mixed with to the speed of atomizer 10 or discharge, so that the first liquid phase reactor object is with more
Stable state enters atomizer 10, then smoothly reaches in atomization chamber 21 in droplets.Measurer 11 may include
Multiple ingredient areas (not shown), surge tank 12 may include multiple buffering area (not shown), each ingredient area and a buffer area and
The connection of one atomizer 10.For example, being sprayed when the target product in multiple atomization chambers 21 is identical product through atomizer 10
Out and enter atomization chamber 21 the first liquid phase reactor object and multiple atomization chambers 21 in occur reaction be respectively it is identical, this
When, same first liquid phase reactor object is added in multiple ingredient areas of measurer 11, the first liquid phase reactor object is through buffering
The atomizer 10 in multiple atomisation towers 20 is reached after the multiple buffering area of tank 12 simultaneously；When the target in multiple atomization chambers 21 produces
When object is a variety of products, the first different liquid phase reactor objects is added in assistant ingredients area, is arrived separately at through different buffer areas
In corresponding atomizer 10 and atomization chamber 21, different products is obtained after reaction.
First flow regulating valve 13 and first flow detector 14 are equipped between atomizer 10 and surge tank 12, it is first-class
Amount detector 14 is used to detect the flow for the first liquid phase reactor object for flowing to atomizer 10, and first flow regulating valve 13 is for adjusting
The uninterrupted of the first liquid phase reactor object sprayed from atomizer 10 is saved, and the gear of atomizer 10 is adjustable, so as to
The drop size in atomization chamber 21 is adjusted, and then influences the feature of product.Preferably, each atomizer 10 corresponding one first
Flow control valve 13 and a first flow detector 14, to be independently adjustable or control the first liquid phase into each atomization chamber 21
The flow of reactant.It can be said that even if what is be added in measurer 11 is same first liquid phase reactor object, when in atomization chamber 21
In the case that amount of droplets is different with size, it is also possible to obtain the different product of different characteristic such as particle size.
Feed proportioning system 1 can also be used in the cleaning of atomization chamber 21.When replacing product material or periodic inspection, can match
Water is added in the measurer 11 of material system 1, water mist is made to flow through surge tank 12 and enters atomization chamber 21, is most discharged afterwards through discharge port 23
And achieve the purpose that cleaning.
Compressed air source unit 40 is for generating inert protective gas or reaction gas in air-channel system 4, compressed air source unit 40 with
Gas cushion 41, inert protective gas or reaction gas are also connected between feed inlet 22 through gas cushion 41 and charging
Mouth 22 is provided to atomization chamber 21.
Referring to Fig. 1, atomization system 2 further includes atomizer 24, which is connected to the charging of 21 lower end of atomization chamber
Mouth 22.The lower end feed inlet 22 through atomisation tower 20 enters atomization after the atomizer 24 may be used to the atomization of second liquid phase reactant
Chamber 21.The second liquid phase reactant can be identical as the first liquid phase reactor object, can also be different from the first liquid phase reactor object.It is preferred that
Ground, each atomization chamber 21 connect an atomizer 24, can make different second liquid phase reactant entrance pair by atomizer 24
The atomization chamber 21 answered carries out different reactions in different atomisation towers 20 to realize.
Specifically, which can be ultrasonic atomizer 24.
Atomizer 24 can connect between feed inlet 22 and compressed air source unit 40, and the inertia that compressed air source unit 40 generates protects gas
Body or reaction gas pass through atomizer 24 and enter atomization chamber 21.Therefore, in the present embodiment, enter atomization chamber 21 through atomizer 24
Fluid can be second liquid phase reactant, be also possible to second liquid phase reactant and reaction gas, can also be reaction gas
Or inert protective gas etc., (dotted arrow show the first liquid phase reactor in Fig. 1 depending on specific high-temperature spray reaction type
The flow direction of object and second liquid phase reactant, solid arrow show the flow direction of gas).I.e. atomizer 24 is removed to have and be incited somebody to action
Other than the effect of second liquid phase reactant atomization, connection between compressed air source unit 40 and feed inlet 22, buffer function are also acted as, the
Enter between atomization chamber 21 after the atomization of two liquid phase reactor objects into the gas that atomization chamber 21 and compressed air source unit 40 generate and be independent of each other,
On the contrary, the second liquid phase reactant that the gas that compressed air source unit 40 generates, which enters atomizer 24, may additionally facilitate in atomizer 24 is atomized
After flow to atomization chamber 21.
The power adjustable of the atomizer 24, the flow of the second liquid phase reactant after atomization can be changed.Atomizer 24
Second flow regulating valve (not shown) and second flow monitor (not shown), second flow are also equipped between feed inlet 22
Detector is used to detect the flow for entering the first liquid phase reactor object of atomization chamber 21, inert protective gas or reaction gas, and second
The flow that flow control valve is used to adjust the first liquid phase reactor object into atomization chamber 21, inert protective gas or reaction gas is big
It is small.Preferably, a second flow regulating valve and one are installed between each atomizer 24 and the feed inlet 22 of an atomisation tower 20
Two flow monitoring instruments, can be independently adjusted or control the flow into the second liquid phase reactant of each atomisation tower 20, with
And the flow of inert protective gas or reaction gas, and then control the reaction in each atomisation tower 20.
Specifically, if the first liquid phase reactor object is different from second liquid phase reactant, it is equivalent to different liquid phase material point
Do not enter atomization chamber 21 through atomizer 10 and atomizer 24, concurrently raw reaction is contacted in atomization chamber 21, is conducive to so more
The offer of the reactive liquid phase material of kind, prepares product particularly suitable for a variety of liquid phase material reactivity.If the first liquid phase reactor
Object is identical as second liquid phase reactant, then is comparable to liquid phase material and enters atomisation tower through atomizer 10 and atomizer 24 simultaneously
20, the nebulization efficiency of liquid phase material is significantly improved in this way, to improve reaction rate, is particularly suitable for the heat of liquid phase material
Decompose the reaction such as preparation or drying-granulating.Further, inert protective gas enters atomization chamber 21 through the atomizer 24, especially suitable
It is reacted together in the thermal decomposition preparation of liquid phase material or drying-granulating etc., reaction gas enters atomization chamber 21 through the atomizer 24, especially
It is suitable for liquid phase material and gaseous phase materials reactivity prepares product.
Further, atomization system 2 further includes the vibrator 25 for being connected to each atomisation tower 20, and vibrator 25 drives each
Atomisation tower 20 shakes to prevent generation composition granule obtained in atomization chamber 21 etc. to be adhered on the inner wall of atomisation tower 20, and promotes
The flowing of fluid in atomization chamber 21.
Specifically, which can be electromagnetic vibrator or mechanical vibrator.Vibrator 25 is by motor (not shown)
Vibration is driven, and shakes power adjustable.Preferably, each atomisation tower 20 connects a vibrator 25, can be independently adjusted or
Control the response situation in each atomisation tower 20.
Referring to Fig. 1, material-receiving system 3 further includes the air blower 31 for being connected to cyclone separator 30, air blower 31 is for mentioning
Enter the power of cyclone separator 30 from the discharge port 23 of atomisation tower 20 for fluid.The power adjustable of air blower 31, to meet not
With the separation requirement of product.Further, air blower 31 can also be connected with cyclone separator 30 and gas cushion 41 it
Between, the gas outlet of cyclone separator 30 connects air blower 31, and the gas outlet of air blower 31 is connected to gas cushion 41, so that from
The reaction gas of the gas outlet discharge of cyclone separator 30 or inert protective gas etc. can be again introduced into atomization chamber 21 and be subject to benefit
With, so that gas effciency is improved, the pollution of reduction production cost and surrounding air
The quantity for the cyclone separator 30 connecting with the discharge port 23 of atomisation tower 20 can be one or more.If multiple mists
What reaction obtained in change chamber 21 is same product, then the discharge port 23 of multiple atomisation towers 20 can connect to same whirlwind point
From device 30, if what is carried out in multiple atomisation towers 20 is different reaction, what is obtained is different product, then different atomisation towers 20
Discharge port 23 be connected to different cyclone separators 30.Further, the series connection of multi-cyclone 30 can also be set,
To realize that the product of variety classes or feature is precisely separated collection.
The high-temperature spray consersion unit 100 of the utility model further includes heating system 5, and heating system 5 includes heating device
51, with the heated shell 54 of heating chamber 52, and it is covered in the insulating layer 53 outside heated shell 54, heating device 51 is to adding
Heating chamber 52 in hot shell 51 is heated, and multiple atomisation towers 20 are arranged in heating chamber 52, to guarantee each atomization chamber 21
Interior required reaction temperature.
Specifically, heated shell 54 can be metal shell, ceramic shell or glass shell etc..Heating device 51 can be with
It is microwave heating equipment 51, induction heating apparatus 51 or resistive heating device 51.The power adjustable of heating device 51, to meet not
With the temperature requirements of reaction.
Insulating layer 53 can be one of alumina silicate, mullite fiber, alumina fibre or aluminium oxide or a variety of.
Further, the high-temperature spray consersion unit 100 of the utility model further includes linked system 6, and linked system 6 connects
Between atomization system 2 and material-receiving system 3, for regulating and controlling atomization system 2 and material-receiving system 3 online, such as air blower 31 and atomization
The power of device 24.Linked system 6 is according to the spray amount of atomizer 24 or inert protective gas or reaction from compressed air source unit 40
The power of the amount adjustment air blower 31 of gas, when the amount of the spray amount of atomizer 24, inert protective gas or reaction gas increases
When, the power of air blower 31 is increased accordingly, so as to keep balance between material reaction and rewinding in entire reaction process.
High-temperature spray consersion unit provided by the embodiment of the utility model, can adjust the proportion of reaction mass, make difference
The reaction mass of proportion enters in corresponding atomization chamber through different atomizers and different atomizers, and then occurs different
Reaction, by adjusting first flow control valve and second flow control valve come change into the material drop in atomization chamber amount and
Speed changes droplet size, liquid into the material drop in atomization chamber by adjusting the gear and atomizer of atomizer
It drips the parameters such as viscosity, changes the flow parameter in atomization chamber by adjusting the power of vibrator, air blower and atomizer, it can
It realizes control to differential responses and its response parameter, such as changes residence time of the reaction mass in atomisation tower, decomposition temperature
Etc. parameters, to realize the high-throughput preparation of lot of materials and a large amount of different characteristic materials.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Made any modifications, equivalent replacements, and improvements etc., should be included in the utility model within the spirit and principle of utility model
Protection scope within.
Claims (10)
1. a kind of high-temperature spray consersion unit, which is characterized in that including feed proportioning system, atomization system, material-receiving system and gas circuit system
System, the atomization system includes multiple atomisation towers, and each atomisation tower includes atomization chamber, and one end of the atomization chamber is equipped with charging
Mouthful, the other end of the atomization chamber is equipped with discharge port, and the feed proportioning system includes multiple for mentioning into multiple atomization chambers
For the atomizer of the first liquid phase reactor object, each atomisation tower connects an atomizer, and the air-channel system includes
It is connected to the compressed air source unit of the feed inlet of the atomisation tower, the material-receiving system includes the discharge port for being connected to the atomisation tower
It is identical or different to be provided to the first liquid phase reactor object in multiple atomization chambers from multiple atomizers for separator.
2. high-temperature spray consersion unit as described in claim 1, which is characterized in that the feed inlet is set to the atomization chamber
Lower end, the discharge port are set to the upper end of the atomization chamber, and the atomization system further includes an at least atomizer, the atomizer
It is connected to the feed inlet of multiple atomisation towers, the second liquid phase that the atomizer is used to provide atomization into the atomization chamber is anti-
Answer object.
3. high-temperature spray consersion unit as claimed in claim 2, which is characterized in that each one atomization of atomization chamber connection
Device, the second liquid phase reactant that multiple atomizers are provided into multiple atomization chambers are identical or different.
4. high-temperature spray consersion unit as claimed in claim 2, which is characterized in that the second liquid phase reactant and the first liquid
Phase reaction object is identical or different.
5. high-temperature spray consersion unit as claimed in claim 2, which is characterized in that the atomizer is connected to the feed inlet
Between the compressed air source unit, the inert protective gas or reaction gas that the compressed air source unit provides enter institute through the atomizer
State atomization chamber.
6. high-temperature spray consersion unit the invention according to any one of claims 2 to 5, which is characterized in that the separator is rotation
Wind separator, the material-receiving system further include the air blower being connected between the cyclone separator and the atomizer.
7. the high-temperature spray consersion unit as described in any one of claims 1 to 5, which is characterized in that the feed proportioning system is also
Measurer including being connected to multiple atomizers, the measurer include multiple ingredient areas, and each ingredient area connects
It is connected to an atomizer.
8. the high-temperature spray consersion unit as described in any one of claims 1 to 5, which is characterized in that the high-temperature spray is anti-
Answering equipment further includes the linked system being connected between the atomization system and material-receiving system, and the linked system is adjusted for linking
Save the atomization system and the material-receiving system.
9. the high-temperature spray consersion unit as described in any one of claims 1 to 5, which is characterized in that the atomization system is also
Vibrator including being connected to the atomisation tower, the vibrator drive the atomisation tower vibration.
10. the high-temperature spray consersion unit as described in any one of claims 1 to 5, which is characterized in that the high-temperature spray is anti-
Answering equipment further includes heating system, and the heating system includes heater, the heated shell with heating chamber and is covered in institute
The insulating layer outside heated shell is stated, the heater heats the heated shell, and multiple atomisation towers are set to described
In heating chamber.
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| CN201820734093.4U CN208356787U (en) | 2018-05-16 | 2018-05-16 | A kind of high-temperature spray consersion unit |
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| CN201820734093.4U CN208356787U (en) | 2018-05-16 | 2018-05-16 | A kind of high-temperature spray consersion unit |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109848429A (en) * | 2019-03-05 | 2019-06-07 | 香港生产力促进局 | A combined device for preparing spherical metal powder by gas atomization |
| CN113830816A (en) * | 2021-04-28 | 2021-12-24 | 广东石油化工学院 | Process for synthesizing multi-metal nano oxide by using confined combustion effect in high-dispersion hot spot |
-
2018
- 2018-05-16 CN CN201820734093.4U patent/CN208356787U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109848429A (en) * | 2019-03-05 | 2019-06-07 | 香港生产力促进局 | A combined device for preparing spherical metal powder by gas atomization |
| CN113830816A (en) * | 2021-04-28 | 2021-12-24 | 广东石油化工学院 | Process for synthesizing multi-metal nano oxide by using confined combustion effect in high-dispersion hot spot |
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| TR01 | Transfer of patent right |
Effective date of registration: 20220516 Address after: 572732 No. 1, Hainan (Changjiang) clean energy high tech Industrial Park, Haiwei Town, Changjiang Li Autonomous County, Hainan Province Patentee after: Hainan Walker New Material Technology Co.,Ltd. Address before: 412000 R & D plant, phase 2.1, Xinma power innovation park, no.899 Xianyue Ring Road, Tianyuan District, Zhuzhou City, Hunan Province Patentee before: HUNAN TRAILBLAZER ENVIRONMENTAL PROTECTION TECHNOLOGY CO.,LTD. |
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| TR01 | Transfer of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: High temperature spray reaction equipment Effective date of registration: 20231227 Granted publication date: 20190111 Pledgee: Bank of China Hainan Branch Pledgor: Hainan Walker New Material Technology Co.,Ltd. Registration number: Y2023980075206 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right |